Loading...
HomeMy WebLinkAbout1891 RUTHERFORD RD; ; AS980113; Permit5/18/22, 10:51 AM Job Address: Permit Type: Parcel No: Lot#: Reference No.: PC#: Project Title: Applicant: AS980113 Permit Data City of Carlsbad AUTOMATIC SPRINKLER-COMM Permit No: AS980113 1891 RUTHERFORD Status: ISSUED RD ASC Applied 7/9/1998 2121202800 Approved: 7/15/1998 48 Issued: 7/15/1998 Inspector: SHELL BLDG O/H SPRINKLERS Owner: ACTION FIRE SYSTEMS DIVERSIFIED CARLSBAD 47&48 LL 9185 HARNESS STREET SPRING VALLEY CA 619 462-9210 Fees($) 742 Add'I Fees ($) 0 Total($) Balance($) 742 0 1/1 THERE ARE NO PLANS ASSOCIATED WITH THIS PERMIT ACTION ~IRE SYSTEMS ~ 185 HAHNESS ST. SPRING VALLEY, CA. 91977-3948 11 CALCUU~TION :j:j:l 11 HYDRAULIC CALCULATIONS FOH CRC LOT *•L~8 CARLSBAD, U~ .. FILE NUMBER: 98-762 7 ···-'3 -·-98 OCCUPANCY CLASS IF I CAT I DI-J ~ DENSITV: L C • +...J AREA OF APPLICATION: COVERAGE PER SPRINKLER: gpm/sq. f t. sq. ft. NUMBER OF SPRINKLERS CALCULATED: 3 "► s pr i n I-< 1 er s TOTAL SPRINKLER WATER FLOW REQUIRED: i583. i gpm TOT AL l.-J ATER F< E Q U I f< ED ( i n c l u d i n g h o s e ) : 2 0 B ;3. 1 y pm FLOW AND PRESSURE (@ BOR): 1583. 1gpm@ 69.6 psi SPRINKLER ORIFICE SIZE: 5/8 NAME OF CONTRACTOR: CORNERSTONE CONSTRUCTION DESIGN/LAYOUT BY: BRIAN WEI T inch AUTHORITY HAVING JURISDICTION: CARLSBAD FIRE DEPT. crn,rrnACTlJF< CEF<T IF I CAT ION NUMBi:::F<: C-·· 16 3881 GtZ1 CALCULATIONS BY HASS COMPUTER PROG1AM (LICENSE# 8926J521 l-ms SYSTEMS, INC .. {.~TLANTA, Gt4 .... Date: 11/01/91 SPRIN~<LER SYSTEM HYDRAULIC m~r~L..YSIS JOB TITLE: CARLSBAD RESEARCH CENTER -LOT #48 CALC #1 ROOF WATER SUPPLY DATA SOUHCE NODE TAG Lil STATIC PREBS. <PSI> 120.0 RES ID. PRESS. (PSI) 115.0 FLOW @ (GPM> 1530.0 AGGREGATE FLOW ANALYSIS: TOTf°'.'.)L FLOW AT SOUHCE TOTAL HOSE STREAM f-lLLDWANCE OTHER HOSE STREAM ALLOWANCE£; TOTAL DISCHARGE FROM ACTIVE NODE ANALYSIS DATA , NODE TAG ELEVATION NODE TYPE <FT> 1tZt1 28.8 ~<=11. 50 102 28.B I-<= 11. 50 11213 28.8 K=11.50 104 28.8 K=l 1. 50 1e,5 28.8 ~{= 11. 50 11216 28.8 K= 11. ~30 11217 28.8 K=11. 50 11218 28.8 '"":::::11. 5121 112tCJ 28.8 •<=11. 50 11121 28.8 '""=11. 5121 1 1 1 28.8 •<=11. 50 112 28.8 K=l 1. 50 113 28.8 K=11. 50 114 28.8 K=l 1. 50 115 28.8 K=11. 50 116 28.8 I·<= 11. 50 117 28.8 •<= 11. 50 118 28.8 K=l 1. 50 11 C.) 28.8 •<=11. 50 120 28.8 K== 11. ~5121 121 28.8 K=i 1. 50 122 28.8 I,= 11. 50 123 28.8 K= 11. :=;1t.1 124 28.8 K= 11. 5Q.i 125 28.8 ~<= 11. 50 126 28.8 K=l 1. 50 127 28.8 K== 11. 50 12a i.~8. a I-<= 11. 50 12C) 28.8 •<=11. 50 130 28.8 K=l 1. 50 131 28.8 K=11. 50 132 28.8 K= 11. 5121 133 28.8 K=11. 50 134 28.8 K=l 1. 50 A\..HUL. TOTAL PRESS. 1]1 DEMAND <PSI) <GPM) 111. 2 i::~,~83. 1 2083. 1 AT SOURCE 400.0 100.0 SPRINKLERS 1 ~i83. 1 PRESSUF<E DI SCH(4RGE (PSI> <GPM) 15.4 4c:· ,_J. 1 14.6 43.<) 14.2 4~;. 3 1-4-. 1 .l~3. 2 1 Lt. 1 4-· .. -, ~-a::. 14.3 '+3 • .(.~ 14.8 Lt4. 2 15.8 45.6 17.4 48.0 16.2 46.2, 15.3 45.0 14. C) 44. '+ 14.8 4Lt. 2 1 L~. f3 44. i.::'. 1 L►• 9 Lt4. 4 15.3 45.0 16.3 46.4 17.9 4f3.7 16.3 46. ~i 15.4 41::.~ ,_J. 1 15. !ll 44.5 1 't. 8 44.3 1 Lt. 8 L~4. 3 15.Qt 44. :5 1=i .. 4 L►5. 2 16.4 46. ti 18.0 Lt8. 8 ".:-~121. 6 5i::'.. i~~ 20. 1 51.5 20. 0 51. '+ 20.0 51.4 20.2 51.6 20.8 52.4 2i::'.. 1 54. 1 REQ"D PRESSu <PSI) 84.8 GPM '3PM GPM GPM SPRINKLER SYSTEM HYDRAULIC ANALYSIS JOB TiiLE: CARLSBAD RESEARCH CENTER -LOT #48 CALC #1 ROOF JDE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE 151 15i.=:'. 153 . 154 155 156 157 158 159 160 161 162 163 164 165 166 167 168 if,C.) 17121 171 172 173 174 175 176 1T1 178 179 180 181 182 183 184 21211 202 203 21214 20~5 206 f:07 208 209 1 2 3 7 8 9 1121 1 1 ( FT> <PSI> < GPM > 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 c~a. 8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 26.tZI 26.0 26.0 26.0 26.121 26.0 26. 121 26.0 26. 121 26.0 26.0 51. 1 51.2 51. 3 51.5 51.6 51. 7 51. 8 ~52. 0 52. 1 51.2 51.4 51. 5 51. 7 51.9 ~52. tZI 52.2 52.4 L~B. e, 48.4 48.7 49. 1 4.9 • .l~ 1+9. 8 50 .. 2 ~"50. 5 ~50. 9 4B.6 49.0 49.3 50. ~i ~s0. a '+0. 8 4121. 8 1+0. 8 L~ 1. b 41.6 41.6 .li,1,. 3 41. 3 37 .. 7 31. 1 53.5 37.7 53.5 53.6 38.7 53.7 39.8 54 .. 0 Page 2 SPRINKLER SYSTEM HYDRAULIC ANALYSIS JOB TITLE: CARLSBAD RESEARCH CENTER -LOT #48 CALC #1 ROOF JDE TAG ELEVATION NODE tYPE PRESSURE DISCHARGE 12 13 14 14A 15 16 17 18 19 20 21 22 22A 25 26 27 28 2S> 30 30A 31 TOR BOR U5 U4 U3 U2 U1 <FT> <PSI> <GPM) 26.0 26. 121 26.0 26.0 26.0 26.121 26.0 26.0 2("\. 121 26.0 26.0 26.0 28.8 26.0 26.0 28.8 2E.\. 0 26.0 26.0 i::'.6. 0 26.0 26.0 28.8 26.0 25.5 0.5 -3.0 2.0 2.0 -3.0 -3.0 HOSE STREAM SOURCE 40.3 54.6 it-1.IL~ 41.2 41 • .lt, 54.5 41.7 5.lt-. 4 41.9 ~54 • .lt, 41.9 .lt-1. 3 ~j4. Li- .lt-2. 0 41.6 4.lt-. 7 45.9 53.9 ,•-1. l ,j ... "+ 42. 121 .l1.,1. 8 55.0 57.2 6•::.). 6 71 .. .lt, 7'+. <) 79.9 83. Li- 84. 8 100. Qt 1683. 1 Page 3 .,, '\ SPRIN~<LER SYSTEM HYDRAULIC ANt4LYSIS Page 4 JOB TITLE: CARLSBAD RESEARCH CENTER -LOT 4f48 Cf~LC #1 ROOF PIPE DATA PIPE TAG G! <GPM) DH)<IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL<FPS) HW(C) <FT) SUM. NODES <FT> ( K) <PSI> (8PM) F.L./FT <PSI> Pipe: 1 168.6 2.203 PL 20. 33 PF 6.6 1 26.0 0.0 37.7 !l1. 0 14.2 120 FTG T2L PE 0.0 2 26.0 0.0 31. 1 ll'f. 0 0. 181 TL 36.33 PV 1. '+ Pipe: 2 168.6 2.203 PL 70.00 PF 11 •• 5 2 26.0 0.0 31. 1 0.0 14.2 120 FTG T PE 1.2 101 28.8 11. 5 15 • .l. 45. 1 0. 181 TL 8tL1. 00 PV 1.4 Pipe: 7 ..., 123.5 2.203 PL 8.00 PF 0.8 HH 28.8 11. 5 15.4 4c:· ..J. 1 10.4 120 FTG PE 0. tL1 102 28.8 11. 5 14.6 L.3. q 0. 102 TL 8.00 PV 0.7 Pipe: L• 79.6 2.203 PL 8.00 PF 0.4 102 ~~8. 8 11.5 14.6 43.9 6.7 120 FTG PE 0.0 103 28.8 11.5 14.2 43.3 0. 0l•5 TL 8. 0tL1 PV 0.3 Pipe: c::-..J 36.3 2.203 PL 8.00 PF 0. 1 103 28.8 11.5 14.2 L•3 ■ 3 3. 1 121l.1 FTG PE 0.0 104 28.8 11.5 14. 1 43.2 0.011 TL 8.00 PV 0. 1 Pipe: 6 -6.9 2.203 PL 8.00 PF 0.0 104 28.8 11. 5 14. 1 43.2• 0.6 120 FTG PE 0.'21 ' 105 28.8 11. 5 1 L• • 1 4-;• -::, ..., • i.;., 0. !l100 TL 8.00 PV 0.0 Pipe: 7 --50. 1 2.203 PL 8. 0Q' PF 0. i:.:'. 11215 28.8 11. 5 11 •• 1 47 ·::. w. L.. L •• 2 120 FTG PE 0.0 106 28.8 11.5 1 .l ~--.. ~ 43.4 0.01() TL 8.00 PV 0. 1 Pipe: 8 -93.6 2.203 PL 8.00 PF 0 ,::-• ..J . 106 28.8 11.5 1 .l •• 3 43.4 7. •-=J 120 FTG PE 0. IZI 107 28.8 11. 5 14.8 1•4. 2 0.061 TL 8.00 PV 0.4 Pipe: 9 --137.'3 2.203 PL 8.00 PF 1.0 11217 28.8 11. 5 14.8 4 1-t. 2 11.6 120 FTG PE 0.0 108 28.8 11. 5 15.8 45.6 0 .. 1 .-·,i:::-C...J TL 8.00 PV 0.9 Pipe: 10 -183.4 2.203 PL 8.00 PF 1.7 10B 28.8 11. 5 15.8 45.6 1 ,::.~ i. ..J. t 120 FTG PE 0.0 11219 28.8 11. 5 17. 4. 1.8. 0 0.212 TL 8. !l10 PV 1.6 Pipe: 11 -·-231. 4 2.203 PL 87.00 PF 34.B 1121<3 28.8 11. 5 17.4 48.0 1 Cj. 5 120 FTG 2T PE Li:::: 3 26.0 0.0 53.5 0. IL' 0.325 TL 107.1210 pt.,t 2.6 Pipe: 12 179.0 2.203 PL 80.00 PF 20.2 4 26.0 121. 0 37.7 0. 0 15. 1 120 FTG ~:'.T PE 1.2 110 28.8 11.5 16.2 46.3 0 .. 202 TL 100.00 PV 1 c:· ■ ,_I Pipe: 13 132 .. 6 2.203 PL 8.00 PF 0. <-) 110 28.8 11.5 16.2 46.3 11. 2 120 FTG PE 0.0 1 1 1 ~:'.8. 8 11. 5 1 C: ~ ... ..J •• ~ 45.0 0. 116 TL 8.00 P\J 0.8 ..... .... SPRINKLER SYSTEM HYDF<AULIC ANALYSIS Page 5 JOB TITLE: CARLSBAD HESEARCH CENTER ·-LOT #4H CALC #1 ~lOOF PIPE DATA (cont'd) PIPE TAG G~<GPM> DIA<IN) LENGTH PRESS. EMD ELEV. NOZ. PT DISC. VEL<FPS> Hli-J < C) <FT> SUM. NODES <FT> <K> <PSI> <GPM> F.L./FT <PSI> Pipe: 14 87.6 2.203 PL 8.00 PF e,. 4 1 1 1 28.8 11. 5 15.3 .lt-5. 0 7.4 121l' FTG PE 0. e, 112 2a. 8 . 11. 5 14.9 4.lt-. 4 0.054 TL 8.00 PV 0. "t Pipe: 15 43.2 2.203 PL 8.00 PF 0. 1 112 28.8 11. 5 1 .l,-. 9 .lt-4. 4 3.6 lc:0 FTG PE 0.0 113 28.8 11. 5 14.8 44.2 0.015 TL 8.00 PV 0. 1 Pipe: 16 -1.0 2.203 PL 8.00 PF 0. 12, 113 28.8 11. 5 14.8 .lt-1►• f: 0. 1 120 FTG PE 0. Q, 114 28.8 11. 5 14.8 44.2 . 0.000 TL 8. 00 PV 0.0 , Pipe: 17 -1►5. 1 2.203 PL 8.00 PF 0. 1 114 28.8 11.5 14.8 44.2 3.8 li::'.0 FTG PE 0.0 115 28.8 11.5 14.9 4.lt-• .lt-0.016 TL 8.00 PV 0. 1 Pipe: 18 -8·~-5 2.203 PL 8.00 PF 0. It 115 28.8 11. 5 11,-. Cj lt-1►• Lt-7.5 120 FTG PE 0.0 116 28.8 11. 5 1 i::.~ -~ ,J • ..., 45. IZt 0.056 TL 8.00 PV 0.4 Pipe: 19 -134.6 2. 21t)~; PL 8.00 PF 1.0 l.16 28.8 11. 5 15.3 45.0 11. 3 120 FTG PE 0.0 117 28.8 11. 5 16.3 Lt-6. lt-0. 119 TL 8.00 PV 0.C) Pipe: 20 ·-181. 0 2. 21213 PL 8.00 PF 1.7 117 28.8 11. 5 16.3 46. 1,. 15.2 120 FTG PE 0.0 118 28.8 11. 5 17.9 '-►8. 7 0. 21216 TL 8.00 PV 1.6 Pipe: 21 -229.7 2.203 PL 87.00 PF 34.3 118 28.8 11.5 17.9 48.7 19. 3 U~0 FTG 2T PE 1.2 i:::· ..J 26.0 0.0 53.5 0.0 0.321 TL 107.00 PV .-. i::: a::. ...... Pipe: 22 180.0 2.203 PL 80.00 PF 20. 1.,. 6 26.0 0. '0 38.0 0.0 1 c· -..:J. 1 120 FTG 2T PE 1. 2 11':) 28.8 11. 5 16.3 46 .. 5 0. 2tZ14 TL 11210.00 PV 1 r.;;-• ..J Pipe: 23 133. ~5 2. 202; PL 8.00 PF 0.9 115 28.8 11. 5 16.3 46.5 11. 2 120 FTG PE '21 .. tZI 12 121 28.B 11. 5 15.4 .l i::.-► ...... 1 Q,. 118 TL 8.00 PV 0.8 Pipe: 24 88. '+ 2 .. 203 PL 8.00 PF e,. I.► 12121 28.8 11. 5 15.4 L c:· ► '-' • 1 7" L't 120 FTG PE 0.0 121 28.8 11. 5 15.tZI .lt-4 .. 5 0.12155 TL 8. 0121 PV 0.4 Pipe: 25 .lt-3. 9 f:. 203 PL 8.00 PF 0. 1 121 i::'.8. 8 11. 5 15.0 1+4. 5 3. ·7 li:::0 FTG PE 0.0 1--•,.-, .::..::. 28.8 11.5 14.8 .l't"+. 3 0. 01 ~i TL 8.00 PV 121. 1 Pipe: 26 --121. 4 2.21213 PL 8. 00 PF 0. Ii.) 122 28.B 11. 5 11,-. 8 .lt-4. 3 0. 121 120 FTG PE 0.0 123 28 .. 8 11. 5 14.8 44.3 0. 01210 TL 8.00 PV 0.tZI ' ' SPHil'H{LER SYSTEM HYD Rf.~UL IC ANALYSIS P~ge 6 JOB TITLE: CARLSBAD RESEARCH CENTEH -LOT :1-1:48 CALC #1 ROOF PIPE DATA (cont'd) PIPE T~lG CJ. <GPM> DIA<IN> LENGTH PRESS. END ELElJ. NOZ. PT DISC. VEL(FPS) HW(C) (FT> SUM. NODES <FT> ( K) <PSI> <GPM) F. L. /FT <PSI) Pipe: 27 --4-4-. .. ., f~. 203 PL 8. 1210 PF 121. 1 ' 123 28.8 11. 5 11 •• 8 44.3 3.8 120 FTG PE 0. 0 124 28.8 11. 5 15.0 4L►• ~) 0.016 TL 8. 00 PV 0. 1 Pipe: 28 -89.2 2.203 PL 8.00 PF 0 • .l. 124 28.8 11. 5 15. 0 44.5 7.5 120 FTG PE 0. 121 125 28.8 11. 5 1 ~5 • .l. 45.2 e,. 056 TL 8.00 PV 0 • .l. Pipe: i::'.9 ···-134. -4. 2.203 PL 8.00 PF 1. 0 125 28.8 11. 5 15 • .lt 45.2 11. 3 120 FTG PE 0.tZI 126 28.8 11. ~j 16.4 '+6. 5 0. 119 TL 8.00 PV 0. <:) Pipe: ~30 -180.9 2.203 PL 8.00 PF 1.7 126 28.8 11. 5 16.4 46.5 1 ~3. 2 120 FTG PE 0. tZI 127 28.8 11.5 18.0 48. 8 0.206 TL 8.00 PV 1.6 Pipe: 31 --2i::'.9. 7 2.203 PL 87.00 PF 3Lt. 3 127 28.8 11. 5 18.0 48.8 19. 3 120 FTG 2T PE 1.2 7 26.121 0.0 5:~. 6 0.0 0.321 TL 107.00 PV -::, 1:;.-I-• ..J Pipe: 32 149.6 2.203 PL 96.00 PF 16.8 8 26.0 0.0 38.7 0.0 12.6 120 FTG 2T PE 1.2 128 28.8 11.6 20. E., 52. i:~ e,. 1.l•5 TL 11 6. Q)0 PV 1. 1 Pipe: "-',••"'\, ~~ 97. '+ 2.203 PL 8. 1210 PF 0.5 128 28.8 11. 5 20. 6 52.2 8 .-, . .:::.. 120 FTG PE 0. tt1 129 28.8 11. 5 20. 1 51.5 0.066 TL 8.00 PV 0.5 Pipe: 3.L• L.5. C) 2.203 PL 8.00 PF 0. 1 12<.) 28.8 11.5 20. 1 51.5 3. C) 1 i::'.QI FTG PE 0.0 130 28.8 11. 5 20.0 51. L• fl1. 016 TL 8.00 PV 0. 1 Pipe: 35 --5. 5 2.203 PL 8. Q1Q) PF 1t:i. e, 131Zl 28.8 11. 5 20.0 51. Lt e,. 5 120 FTG PE 0.0 131 28.8 11. 5 2e,. ei 51. 4 0 .. 00121 TL 8.1210 PV 0. tZI Pipe: 36 -56.9 2. 20:~ PL 8.00 PF tt1. 2 131 28.8 11. 5 ~::0. 0 51. Lt 4.8 1 ~::e1 FTG PE 0.0 12;2 28.8 11. 5 20.2 51.6 0. 02L• TL 8.00 PV 0.2 Pipe: 37 ·-10B. 5 2 .. 21213 PL 8. 12.10 PF 0.6 13i::'. 2$.8 11. 5 20.2 51.6 9. 1 120 FTG PE 0.0 133 28.8 11.5 20.8 52. '+ fl,. 080 TL 8. ,,ei PV 0.6 Pipe: 38 ..!..161. 121 2.203 PL 8. ll.10 PF 1. 3 1 -;--;. -.-;J>,J 28.8 11. 5 20.8 52.4 1-:;-i:::-.. J • ...., 120 FTG PE 0. Ill 13Lt-28.8 11. 5 22. 1 54. 1 0. 166 TL 8. 00 PV 1.2 Pipe: 3<":) ···-215 . 1 2. 2Qt3 PL 87.00 PF 3tZI., '+ 134 28.8 11. 5 22. 1 ,::-1. ..J •• 1 18. 1 120 FTG 2T PE L2 CJ 26.0 0.0 ~53. 7 0.0 0.2H4 TL 107.00 PV ·=· -::, ...... I- ' ... SP RI Nl·<L E F< SYSTEM HYDF<AULIC ANALYBIS Page 7 JOB TITLE: Cf➔RLSBAD HESEAHCH CENTEI~ -·-LOT #'+8 Cf"'..'\LC #1 ROOF PIPE DATA (cont'd) PIPE TAG G! <GPM> DH'.l(IN> LENGTH PHESS. END ELEV. NOZ. PT DISC. VEL<FPS) HW(C) <FT> SUM. NODES <FT> ( K) <PSI) <GPM> F.L./FT <PSI> Pipe: 40 -86. Lt, 2.203 PL 231.00 PF 1'+. 2 10 26.0 0.0 39.8 0.0 7.3 120 FTG .l•T PE 0. lli 11 26.0 0.0 5.l •• 0 0. 0 0.053 TL 271.00 PV 0. '+ Pipe: 41 --86. 6 2.203 PL 231.00 PF 1 .l •• 3 12 26.0 0. 0 '+0. 3 0.0 7.3 120 FTG 4T PE 0. 121 13 26. fll 0.0 5 1•. 6 0.0 0.053 TL 271. 00 PV 0 • .[. Pipe: 42 -8.l►• 2 2.203 PL 231.00 PF 13.6 14 26.0 0.0 41.0 0.0 7. 1 120 FTG i.•T PE 0.0 15 26.0 0.0 ~54. 5 0.0 0.050 TL 271.00 PV 0.3 Pipe: 43 -82. ~i 2.203 PL 231. 00 PF 13. 1 16 i::'.6. 0 0.0 '+ 1. 4 It,). 0 6.9 120 FTG 4T PE 0.0 17 26.0 0.0 5.l►• 5 0.0 0. 0 1-1-8 TL 271. 00 PV 0.3 Pipe: 44 -81.3 2.203 PL 231.00 PF 12.7 18 26.0 0.0 41. 7 0.0 6.8 120 FTG 4T PE lli. 0 1_,:_) 26.0 0.0 54.4 0.0 0.047 TL 271.00 PV 121. 3 Pipe: .l•5 --80. 6 2. 21li3 PL 152. ~33 PF 8.0 212) 26.0 0.0 '+1. C) 121. 0 6.B 120 FTG 2T PE 1.2 17H 28.8 fli. 0 1►8. 6 0.0 tli. ll'1+6 TL 172.33 PV Q). 3 Pipe: L►b .. -B0. 6 2. 20~~ PL 8.00 PF 0. '+ 178 28.8 0.0 48.6 0.0 6.8 120 FTG PE 0. lli 179 28.8 0.0 49.0 0.0 0.046 TL B.00 pt) 0.3 Pipe: .lt,7 --80. 6 2.203 PL 8.00 PF 0 • .I.. 179 28.8 0. 0 1+9. 0 0.0 6.8 120 FTG PE 0. IZI 180 28.8 0.0 .l.9. 3 0. ll_i 0.046 TL 8.00 PV 0.3 Pipe: Lt-8 --80. 6 2.203 PL 8.00 PF 0. "+ 18QI 28.8 0. J2I 49.3 0.0· 6.8 120 FTG PE 0.0 181 28.8 121. 0 '•9. 7 0.0 0.046 TL 8.00 PV 0.3 Pipe: 49 -.. 80. 6 2.203 PL 8.00 PF 0.4 181 28.8 0.0 '+<). 7 0.0 6. 8 120 FTG PE 0.·0 182 28.8 0.0 50. 1 0.0 0.046 TL 8. 0!l1 PV 0.3 Pipe: 50 --80. ('\ ;.=::. ~~03 PL 8.00 PF 0. i.~ 1 Eh~ 28.8 0.0 50. 1 Q1. tZl 6.8 1212.1 FTG PE tZI. !l) 183 ~~8. 8 IZI. 0 ~30. 5 0.0 0. ll146 TL 8.00 PV 0.3 Pipe: 51 --B0. 6 2. 202:~ PL 8. lli0 PF 0 • .l. 183 28.8 0. IZI 5121.5 0.0 6.8 120 FTG PE ll,). IZI 18.lt 28.8 ll.i. 0 50.8 0. 0 0. 0 1t6 TL 8. 00 PV 0.3 Pipe: 52 ·-8121. 6 i.=::. 203 PL 30.67 PF 2.3 181+ 28.8 0.0 50.8 ll.i. 0 6.8 12121 FTG 2T PE 1.2 21 26.0 0.0 54.4 0. e, 0. 1Z146 TL 50.67 PV 0.3 .. ' SPRIN~<LER SYSTEM HYDRAULIC ANr~LYSIS Page B JOB TITLE: CARLSBAD RESEARCH CENTER --LOT :}=1:48 CALC #1 ROOF PIPE DATA (cont'd) PIPE TAG G! <GPM) DIA< IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL<FPS> H\.-J < C) <FT> SUM. NODES <FT> < K) <PSI) <GPM> F. L. /FT <PSI) Pipe: 53 . --7'=) • L• 2.203 PL 2./33 PF 121. 6 22 26.0 0.0 41. CJ 0.0 6.7 120 FTG T PE 1 .-, • a::. 22A 28.8 0.0 1+1. 3 0.0 IL,. 04~5 TL. 12.83 PV 0.3 Pipe: 54 -7CJ • L• 2. 2('13 PL 139. 17 PF 6.7 22A 28·. 8 0.0 41. 3 0.0 6.7 120 FTG T PE 0.0 169 28.8 0.0 l.8. 0 0.0 ll,. !l.145 TL 149. 17 PV 0.3 Pipe: i:::-c.~ ..J._J ···-79. 4 2.203 PL 8. ,~0 PF tZI .. 4 169 28.8 0.0 L.B. 0 0.0 6.7 120 FTG PE 0. 0 170 28.8 0.0 48.4 0.0 0.045 TL 8. 0121 PV 0.3 Pipe: 56 -79.4 2.203 PL 8.00 PF IL~. L. 170 28.8 0.0 L.B. 4 0.0 6.7 120 FTG PE 0.0 171 28.8 0.0 48.7 0.0 Qt.045 TL 8.00 PV Qt.3 Pipe: 57 ·-79. 4 2.203 PL 8.00 PF 0.4 171 28.8 0.0 L.B. 7 0.0 6.7 1 f'.IL'l FTG PE 0.0 172 28.8 0.0 '+9. 1 0.0 0.045 TL 8.00 PV 0.3 pi pE•: 58 -79 • .l. 2.203 PL 8.00 PF 0. L► 172 28.8 0. 0 49. 1 0.0 6.7 120 FTG PE 0. 121 173 28.8 0. JZI L•9. 4 0.0· 0.045 TL 8.00 PV 0.3 Pipe: 59 --79. L1. 2. 2e13 PL 8.00 PF 0. 1t 173 28.8 0.0 49.4 0.0 6.7 12fl'l FTG PE 0. 121 174 28.8 0.0 '+<L 8 0. 0 0.045 TL 8.00 PV 0.3 Pipe: 60 -79.4 2.203 PL 8.00 PF fll. 4 174 28.8 0.0 4'·L 8 0. 0 6.7 120 FTG PE 0.0 175 28.8 0.0 50.2 fl). 0 0.045 TL 8.00 PV 0.3 Pipe: 61 ·--79. L• ~::. 2e,3 PL 8. 1210 PF IZI. l~ 175 28.8 0.0 50.2 0.0 6.7 12('.) FTG PE ll,. 0 17& 28.8 121.0 5121. 5 121.121 0 . IL' 1.,. ~3 TL B.00 PV 0.3 Pipe: 62 --79 . 4 2. 202; PL 8.00 PF 0. '+ 176 28.H 0.0 50.5 0.0 6.7 li='.0 FTG PE 0 .. 121 177 28.8 0.0 50.9 0. IJ) 0.045 TL 8.00 PV It) .. 3 Pipe: 63 -·•79 a 4 2. 203 PL 30.67 PF ·:::, ·:.· L-. ,_, 1 Tl 28.8 0.0 50.9 121.0 6.7 12ft) FTG 2T PE 1 .-. • a::. 23 26.0 0.0 54.4 0.0 0.045 TL 50.67 PV 0.3 Pipe: 6L• , -96. 3 2. 21£'3 PL 2.83 PF It). 8 , 24 26.0 0.0 '+2. 0. 0.0 B. 1 l.20 FTG T PE 1.2 21•A 28.8 0.0 Lt-1. 6 ll,. 0 0.064 TL 12.83 PV e:.,. 4 Pipe: 65 -·-<) E:,. :~ 2.203 PL 20.00 PF 1. I..) 24A 28.8 0.0 L~ 1. 6 0.0 8. 1 121f) FTG T PE 1.2 .-.c i:::....J 26.0 0.0 44.7 0. 0 0. Q't64 TL 3121.0121 PV 0. '+ .. SPRINKLEF< SYSTEM HYDRAULIC f.~NALYSIS Page 9 ' JOB TITLE: CAHLSBAD HESEAHCH CENTER ·-LOT ~*'+8 CALC #1 HOOF PIPE DATA (cont,d) PIPE Tf.~G G! <GPM> DIA(IN) LENGTH Pf<ESS. END ELEV. NOZ. PT DISC. VEL<FPS> Hv-J < C) (FT) SUM. NODES <FT> < K > <PSI> (GPM) F. L. /FT <PSI> Pipe: 66 --58. 1 2. 21213 PL 24. ~30 PF 1. 1 25 26.0 0.0 1•4. 7 0.0 1. •• 9 120 FTG 2T PE 0.121 26 26.0 0.0 1+5. 9 0.0 0.025 TL 44.50 PV 0.2 Pipe: 67 -9£.--..3 2.203 PL 87. 00 PF 6 .-, • a::. 26 26. 0 0.0 45.9 0. 0 8. 1 120 FTG T PE 0. e, 27 26.0 0. 0 52. 1 0.0 0.064 TL 97.00 PV !l'I. 4 Pipe: 68 --51. 5 2.203 PL 7.00 PF 0. f~ 27 26.0 0.0 52. 1 0. 0 1. •• 3 120 FTG L PE 1 ·=• . .__ 160 28.8 0. IL'I 51. 1 0.0 0.020 TL 10.00 PV 0. 1 Pipe: 69 -51 .5 2. 202; PL 8.00 PF 121. 2 160 28.8 0. 0 ~51. 1 0.0 i. --. .. ~ li::'.0 FTG PE 0.0 161 28.8 0.0 51.2 0. 0 0.020 TL 8.00 PV ('l. 1 Pipe: 70 -51. ~:j 2.203 PL 8.00 PF 0.2 161 28.8 0.0 51.2 0.0 .l •• 3 120 FTG PE 0.0 162 28.8 0.0 51.4 0.0 0.020 TL 8.00 pt.,t 0. 1 Pipe: 71 -·51. 5 2 . 212.'13 PL 8. l{.'10 PF 0 ·::, • I.- 16i::'. 28.8 0.0 51.4 0.0 L►" 3 li:::0 FTG PE Qi. IZt 163 28.8 0.0 51.5 0. e, 0.020 TL 8.00 PV 0. 1 Pipe: 72 --51. 5 2.203 PL 8.00 PF 0. c=~ 163 28.8 0.0 51. 5 0.0 1 •• 3 12Q'I FTG PE 0.0 164 28.8 0.0 51.7 0. 121 0.020 TL 8. IZIIZI PV 0. 1 Pipe: 73 -51 .5 2.203 PL 8.00 PF 0.2 164 28.8 0.0 51. 7 0.0 4 .... . ~ 120 FTG PE 0. Qt 16~3 28.8 0. l[.'I 51.9 0.0 0.020 TL 8.00 PV 0. 1 Pipe: 74 ·-51. 5 2. 2e,3 PL 8.00 PF e,. 2 165 28.8 0.0 51.CJ 0. 0, L •• 3 120 FTG PE 0.0 166 28.8 ei.'ei 52.0 0.0 tZI • t2l i::'. 121 TL 8.00 PV 0. 1 Pipe: 75 --51. 5 i.:~-203 PL 8.00 PF ll1. 2 166 28.8 0.0 52.0 IZI.IZI 1.~. 3 120 FTG PE 0. IZI 167 28.8 0.0 ,::.-, .-, ..JC. C Q'I. Qt 0. e,20 TL 8.00 PV 0. 1 Pipe: 76 -51.5 2. 2Qt3 PL 8. 0121 PF 0 ····, • a:::. 167 28.8 0.0 52.2 0.0 4 ~-, . ~ 120 FTG PE Q1. Q'I 168 28.8 0. e, 52.4 IL,. 0 0 .. 0i::'.0 TL 8. 0tZt PV 0. 1 Pipe: Tl --51. ~i 2 .. i:::02~ PL 5. 5~) PF ll'I. 3 168 28.8 0. Q, 52.4 0. 121 L~. 3 12121 FTG T PE 1.2 28 26.0 0. 0 53.9 tZl.0 Q'I. 021l'I TL 15.50 PV 0. 1 Pipe: 78 ·-96 . 3 3.314 PL 25. 17 PF 0.5 28 26.0 0.0 53.9 0. 0 3.6 120 FTG 2T PE 0. fl) 29 26.0 0.0 ~54. 4 0 .. 0 0.009 TL 55. 17 PV tZt. 1 .. SPFH N~<LER SYSTEM HYDRAULIC AN~~LYSI S Page H:'l JOB TITLE: CARLSBAD RESEARCH CENTEli -LOT #48 CALC #1 ROOF PIPE DATA (cont'd) PIPE TAG G! <GPM> DIA<IN> LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL<FPS) HW(C) <FT> SUM. NODES <FT> ( K) <PSI> <GPM> F.L./FT <PSI> Pipe: 79 -38.2 2.203 PL 56. 50 PF 1. 1 25 26.0 0.0 L►l► • 7 0.0 3.2 12e1 FTG 4T PE 0.0 26 26.0 0. 0 '+5. C) 0.0 0.012 TL 96.50 PV 0. 1 Pipe: 80 -44.8 2.203 PL 11. 00 PF 0.2 27 26.0 0.0 52. 1 0.0 3.8 120 FTG L PE 1 .-, • a::. 151 28.8 0.0 51. 1 0.0 0.016 TL 14. 0Q.'l PV l{.'l. 1 Pipe: 81 -44.8 2.203 PL 8.00 PF 12.i. 1 151 28.8 0.0 51. 1 0.0 ~;. 8 120 FTG PE 0. Q'l 152 28.8 0.0 51.2 0.0 0.016 TL 8.00 PV 0. l Pipe: 82 -44.8 2.203 PL 8.00 PF 0. 1 1 •==-·-, ..JC 28.8 0.0 ~51. i~ 0.0 3.8 120 FTG PE 0. 121 153 28.8 0.0 51.3 0.0 0.016 TL 8.00 PV ~). 1 Pipe: 83 --AL•. 8 2.203 PL 8.00 PF 0. 1 153 28.8 0.0 51.3 0.0 3.8 120 FTG PE 0.0 154 28.8 0.0 51.5 0.0 0.016 TL 8.00 PlJ 0. 1 Pipe: 84 -•l►l• • 8 2.203 PL 8.00 PF 0. 1 154 28.8 0. ,0 ~H. 5 0.0· 3.8 120 FTG PE 0. 121 155 28.8 0.0 51.6 0.0 Qi. 016 TL 8.00 PV 0. 1 Pipe: 85 -44.8 2. 20:~ PL 8.00 PF 0. 1 155 28.8 0.0 51.6 0.0 3.8 120 FTG PE 0. Qi 156 28.8 0.0 ~H. 7 0.0 0.016 TL 8.00 PV 0. 1 Pipe: 86 -4L►• 8 2.203 PL 8. Q.'10 PF 0. 1 156 28 .. 8 0.0 ~:-51. 7 e, .. 0 3.8 1 ~~0 FTG PE 0. IZI 1 5 7 28.8 Q.1. 0 51. 8 0.0 0. 1£116 TL 8. ll.'10 PV 0. 1 Pipe: 87 --4-'1·. a 2. 21213 PL 8.00 PF !Li. 1 157 28.8 0.0 51.8 Q.'l. 0 3.8 120 FTG PE 0.0 158 28.8 0.121 ~52. IZl 1Zt. 0 1Zt. tZl 16 TL 8 .. 1210 PV 0. 1 Pipe: 88 -.lt,lt, • 8 2.203 PL 8.0121 PF 0. 1 158 28.8 0.0 52.0 0,, 0 3.8 12e1 FTG PE 0.0 159 28.8 ({). 0 52. 1 0.0 0.1211-6 TL 8. 0Q.i P\J 0. 1 Pipe: 89 -44.8 2.203 PL 17.50 PF 0.6 15<) 28.8 0.0 52. 1 0. 121 3.8 120 FTG 2T PE 1 .-. • i:::. 28 26.0 0.0 53.<) 0.0 0.016 TL 37. 5121 PlJ 0. 1 Pipe: 90 0.0 i::'.. 703 PL 18.00 PF fll. 0 21211 i.?.8. 8 0.0 LHZI. 8 0.0 0.0 li::'.0 FTG PE 121. IZI 21Z12 28.8 0. 121 1t-0. 8 0. 0 Q.'l. 000 TL 18.00 PV 0. Q'l Pipe: •:) 1 Ill. 1 2.703 PL 15.00 PF Ill,, tlt 202 28.8 0.0 1.0. B 0.0 0.0 120 FTG T PE 0.0 30A 28.8 0. 0 1+0. 8 0.0 0. 00121 TL 27.00 PV 0.0 «. ' SPHINKLEF~ SYSTEM HYDF<AULIC {~NALYBI S Pc\Q e 11 JOB TITLE: CARLSBAD F<ESE~H1CH CENTEF< --LOT #48 CALC #1 ~100F PIPE DATA (cont"d) PIPE TAG G! <GPM> Dlf.~ < IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL<FPS) Ht,..J ( C) <FT) SUM. NODES <FT> 00 <PSI> <GPM) F.L./FT <PSI) Pipe: 92 •--0. e, 2. 703 PL 210.00 PF IZl. IZI 3tZIA 28.8 0.0 L.0. 8 0.0 0.0 121li FTG T PE 1.2 30 26.0 0. 0 .l•2. 0 0. 0 0. 01210 TL 222. e,0 PV 0. IZl Pipe: 9--,.:, 0.0 2.203 PL 3.00 PF Qi. 0 203 28.8 0 .. 0 4t21. 8 e,. 0 0. tZI U::0 FTG T PE e,. 0 31Zt~~ 28.8 0.0 L.0. 8 Q). 0 0.01210 TL 13.00 PV !Li. 0 Pipe: <)I+ 0. e, 2. 2e,3 PL 16.00 PF 0.0 204 28.8 0.0 L• 1 • 6 0.0 0.0 1f:0 FTG PE 0.0 20~j 28.8 0.0 '+1. 6 0. 0 • 0.000 TL 16. IZt!Li PV tZl .. 0 , Pipe: 95 0.0 2.203 PL 16.00 PF 121. 0 20~j 28.8 0. 0 Ld. 6 0. tZI 0.0 120 FTG PE 0. 121 20(, 28.8 0.0 id. 6 Q.i. 0 0. 121121121 TL 16.00 PV 0.0 Pipe: 9c; --tZI. tZI 2. 2e13 PL 1.00 PF 0 .. 0 2e,c; 28.8 Q.i. 0 41.6 0. 0 121. 0 120 FTG T PE 0. Qi 24A 28.8 0.0 41.6 0.0 0.000 TL 11.00 PV 0. IZt Pipe: 97 0. 12t 2.203 PL 16.00 PF 0.0 207 28.8 0. 0 41. 3 0. 121 ,;~. 0 li.~0 FTG PE Q.i. Qt 21218 28.8 0.0 L• 1. 3 (~. l{.i 0.000 TL 16.00 PV lli. 0 Pipe: 98 0.0 2.203 PL 16. 00 PF 0.0 2e,a 28.a 0.0 L• 1 • 3 0. l{.i 0. tZl 120 FTG PE 0.0 209 28.8 0. 121 41.3 0. 121 0.000 TL 16. 00 P'v' 0. 121 Pipe: 99 0.0 2.203 PL 1.00 PF 0.0 209 28.8 0.0 41.3 Qt. 0 0.0 120 FTG T PE 0.0 -4' 22r.:1 28.8 0.0 L• 1. 3 ,1. 0 0.000 TL 11. Qi0 PV 0.0 Pipe: 100 ·,-168. 6 L~. :310 PL 4.50 PF 0.0 1 26.0 0.'0 37.7 0.0 3 •.. 7 120 FTG PE 0. lli 4 26.tZI 0.121 37.7 121. 121 0. IZltZl7 TL 4. ~5121 PV IZt .. 1 Pipe: 101 --31+7. 6 L1 •• :H Qi PL 12.00 PF e,. 3 4 26. tZt 0.0 37.7 0.0 7.6 120 FTG PE 0. IZI 6 26. Ill 0. 0 38.0 121. 0 0.026 TL 12. Q)0 PV 0. L• Pipe: 102 ···-~527. 5 L•• 310 PL 12.00 PF 0.7 6 f:6. 0 0.0 38.0 0.0 11 .. 6 12e1 FTG PE 0. l{.i 8 26. t2l 0.0 38.7 e1. 0 0. IL.i57 TL 12. 0121 PV ,:.'l. ') Pipe: 103 -.. &77. c: 4. :-H0 PL 12.00 PF 1. 1 8 26.0 0.0 38.7 e,. 0 1 L• • ') 120 FTG PE 0.0 10 2t\. 0 0.0 39.8 0.0 0.0Cj0 TL 12. Q.i!Li P\..' 1 c::· • ._I Pipe: 104 --5')0. 8 4.310 PL 7.92 PF 121. 6 1 tZt 26.0 0.0 39.8 !Li. 0 13.0 12Q) FTG PE lli. Qi 12 26.0 0.0 40.3 0.0 0.070 TL 7.92 PV 1. l ., SPRINKLER SYSTEM HYDH~lUL IC t:'~Nr1L YS IS Page 1 .-, a::. JOB TITLE: CAHLSBAD RESEARCH CENTEH --LOT #48 CALC #1 HOOF PIPE DATA (cont'd) PIPE TnG G! <GPM> DIA<IN> LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL<FPS) HW<C> <FT> SUM. NODES <FT> 00 <PSI> <GPM> F. L. /FT <PSI) Pipe: 105 ·--~j04. 2 L~. 310 PL 12.00 PF tZt .. & 12 26.0 0.0 40.3 0.0 11. 1 120 FTG PE 0.0 14 26.0 0.0 '-1-l. 0 0.0 0.052 TL 12.00 p,; 0.8 Pipe: 106 -1.20. 0 1 •• 310 PL 7.00 PF ~). 3 14 26.0 0.0 41.0 0.0 9.2 120 FTG PE 0. Q) 1 .L•A 26.0 0.0 Li, 1. 2 0.0 0.037 TL 7.00 PV 0.6 Pipe: 107 ·--42121. Q, 4.310 PL ~5. 00 PF ,21. 2 14A 2('\. tZt 0.0 L1-1. 2 ~). 0 Cj. i::'. 120 FTG PE It). 0 16 26.0 0. 0 41. 4 0.0 0.037 TL 5.00 PV 0.6 Pipe: 108 -337.6 1•. 310 PL 12. Q10 PF Q1. 3 16 26.0 0.0 , ... 1. 4 Q.1. 0 7.4 120 FTG PE 0.0 18 26.0 0.0 41. 7 0.0 0.025 TL 12.00 PV 0. L• Pipe: 109 --256. 3 4.310 PL 12.00 PF 121. 2 18 26.0 0.0 Ld. 7 0.0 5.6 120 FTG PE 0.0 20 26.0 0.0 41.9 0.0 0.015 TL 12.00 PV 0 .. 2 Pipe: 110 --175. 7 L1-. 310 PL 9. :54 PF e,. 1 20 26. 0 0.0 41.9 121. 0 3 . •=) 120 FTG PE 0. ,z, 22 26.0 0.0 1,.1. ~ 0. I() 0.007 TL '-3. 54 PV 0. 1 Pipe: 111 .. -96. ;3 4.310 PL 16. e,0 PF lZI. 0 22 26.0 0.0 LJ-1. Cj 0.0 -::, L-.. 1 120 FTG PE Q1. Q) 24 26.0 0.0 1+2. 0 0. e, 0. tZt02 TL 16. tZttZt PV 0 .. Qt Pipe: 112 0.0 -4-. 310 PL 9.00 PF 0.0 24 26.0 0. Qt '-1-2. 0 0.0 0.0 120 FTG PE 0. 121 30 26.0 0.0 42.0 0.0 0.000 TL 9.00 PV (L1. 0 Pipe: 113 --231. Li-6.403 PL 12.00 PF 0. IZt 3 26.0 0.0 i:::·-:;• c::-.... ,..:;,, ..... , 0. Q.1 2 .. 3 12Q1 FTG PE t21. e, 1,-:.-...s 26.0 0.0 53.5 0. If.) 0. 0!t.)2 TL 12.00 PV 0. lZl Pipe: 114 -L1-61. 1 6. L►fl.'13 PL 12.00 PF Q). 1 5 26.0 0.0 c-.-~ i= ... J..., • ...., 0.0 Li-. 6 120 FTG PE 121. tZt 7 2€.\. 0 Q.~. 0 53.6 0.0 0. 0e16 TL 12.00 PV Q1. 1 Pipe: 115 --6 '➔ ,~,. <) G. 4tZt3 PL 12.00 PF Q). i::'. 7 26. 0 0. e, 53.6 0.0 6.9 120 FTG PE 0. 0 9 26.0 0. 0 1:::--i -, .._Jw • I 0 .. tZt 0. 014 TL 12.00 PV 0 .. 3 Pipe: 116 .!.-90~:i. 9 6. L•03 PL 12. 0Q1 PF ,~. -;;• ..... 9 26. IZI 0.0 ~33. 7 0. ,::i 9.0 U~0 FTG PE 0. Qt 1 1 26.0 0.0 5 11-. 0 0.0 0.022 TL 12. 1L1e1 PV e, . c;-..J Pipe: 117 ·--992. 3 6. '+tlt3 PL 5. ~::9 PF Qt.<) 1 1 2£,. 0 0.0 5'+. 0 0.0 C) • C) 12Q1 FTG T PE Q1. ll1 31 26.0 0.0 55. t21 0.0 0. lZti:::7 TL 35.29 PV 0.7 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 13 JOB TITLE: CARLSBAD RESEARCH CENTER -LOT #48 CALC #1 ROOF PIPE DATA (cont'd) PIPE TAG END ELEV. NOZ. NODES <FT> <K> Pipe: 118 31 26.0 0.0 TOR 25.5 0.0 Pipe: 119 TOR 25.5 0.0 BOR 0.5 H.S. Pipe: 120 BOR 0.5 H.S. U5 -3.0 0.0 U5 U4 U-, ~ U4 U3 U.-, .::. U2 Ul 29 23 23 21 21 19 19 17 17 15 15 13 Pipe: 121 2.0 Pipe: 122 2.0 ~~-0 Pipe: 123 2.0 0.0 -3.0 0.0 Pipe: 12Li- -3.0 0.0 -3.0 SRCE Pipe: 125 26.0 26. e, Pipe: 126 26.0 2C:~. 0 Pipe: 127 26.0 26. e, Pipe: 128 26.0 26.0 Pipe: 129 26.0 ~~6. 0 Pipe: 130 26.0 2(~. 0 0.0 0.0 0.,0 0.0 0.0 0.0 0. e, 0.0 Q<GPM> DIA<IN> LENGTH PRESS. PT DISC. t..,1EL <FPS) Ht,.J (C) (FT) <PSI> <GPM> F.L./FT SUM. <PSI> 55.0 57.2 57.2 69.6 69. 6 71. -4. 71. 4 74.9 79.9 "JL1-. 9 ··-1583. 1 0. 0 1 ~.=:;. 8 0. 0 -1582:;. 1 0.0 15.8 100. 12) -1683. 1 100 ■ 0 CJ • ~:_; v..~. 0 -1683. 1 0.0 10.a 0.0 6. itt2t3 PL 22. 75 120 FTG L IZt.063 TL 31.75 6. Ls-03 PL 25. 00 120 FTG 0.063 TL 25.00 t:3 .. 510 PL 10.00 140 FTG L 0. 013 TL 21. 97 7.987 PL 260.0121 15t2t FTG 7L fl~. 12116 TL 355. 20 PF PE PV PF PE PV PF PE PV PF PE PV FIXED PRESSURE LOSS DEVICE 0.121 5.0 psi, 1683.1 gpm e,. 0 -1683. 1 7.987 PL 12.00 PF 79.9 0.0 10.8 150 FTG T2L PE 83.4 0.0 0.016 TL 84.53 PV -1683. 1 7.987 PL 40.00 PF 83.4 0.0 10.8 150 FTG TG PE 84.8 <NIA> 0.016 TL 89.87 PV 54.4 54. Li- 54.4 54.4 54.4 5L1-• .l~ 54.5 ~L i:::-...J ~ • ._I 5.l~. 5 ~)LI-. b -96.3 6.403 PL 12.00 PF 0.0 1.0 120 FTG PE 0.0 0.000 TL 12.00 PV -175.7 6.403 PL 9.54 PF t;:.'l. tt.'l' 1. 8 120 FTG PE 0.0 0.001 TL 9.54 PV 121. 0 0. QI --2 5 (\ • 3 6 • L►,213 PL 1 2. 00 PF 2.G 120 FTG PE 0.002 TL 12.00 PV -·-337. 6 6. '-HZl3 PL 12. 00 PF 0.0 3.4 120 FTG PE 0.0 0.004 TL 12.00 PV --L~ 2Q) • !Lt 0. 0 '-~. 2 0.0 6. -4-1213 PL 12. ,Z10 12tZI FTG 0. 00~i TL 12. 00 PF PE pt.,.i -504.2 6.403 PL 12.00 PF 0.0 5.0 120 FTG PE 0.0 0.008 TL 12.00 PV 2. IZI fl~. 2 1..7 1.6 10.B 1. 7 0.3 1.5 0.6 c::· -1 :...J. , 0.8 L '~ 12i. 12.'t 0.8 12.~. 12.i 0. 121 0.0 0. 121 0.0 0. liJ 0. ll't 0. 121 0.0 0 .. 1/1 0. fll 0 . .l It). 1 ILi. IZt Q.'I. 1 0. 1 0.0 121. 2 SPRINKLER SYSTEM HYDRAULIC ANALYSIS JOB TITLE: CARLSBAD RESEARCH CENTER -LOT #48 CALC #1 ROOF PIPE DATA (cont'd> PIPE T~~G END ELEV. NODES (FT) Pipe: 131 1 ..... , ... , 26. 0 31 26.0 ·NOTES: NOZ. 00 121. 0 0.0 Q(GPM> DIA<IN> LENGTH PT D I SC. V EL ( FPS > Hl.--J ( C) ( FT> <PSI> <GPtrD F.L./FT .:..~-590. 8 6. 41213 PL 2.62 5'-t-. (. 0. It) i:::· ,_J • C) 121l~ FTG T 1:::-i:::-0 0. 0 12).010 TL 32.62 ..J,_J. PRESS. SUM. (PSI> PF 0 .. PE t21. pt,) 0. 3 Q't 2 (1) Calculations were performed by the HASS 5 .5.0 computer program under license no. 89263521 granted by HRS Systems, Inc. 2193 Ranchwood Dr., N.Eu Atlanta, GA 3121345 (2) The system has been balanced to provide an average imbalance at each node of 0.002 gpm and a maximum imbalance at any node of 0.118 gpm. ( 3) Velocity not used any pipe pressures are printed for in balancing the system. is 19. 5 ft/sec. information only, and are Maximum water veloci~y in (4) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP Pf➔GE:: F MATERIAL: DYNAFL HWC: 1i::'.0 Diameter Equi vc::il r::•nt Fittin~1 Lengths in Feet ( i r-.> E T L C B G A Ell Tee LNGELL CH~<VLV BFYVU.J (3ATVL\,,1 ALMC~-U·~ 2. f~tZl3 5. 0121 10.00 3. 0tZt 11.00 6. e,0 1. 00 10.00 2.703 6.00 12. Q.'10 i~. 01Zl 11~. e,0 7. e,0 1.00 10. t;:)0 3.314 7.00 15. 0121 5. e,ei 16.00 10. 12.'ltt) 1. 00 13.00 4·. 310 10.00 2~). 00 6.00 22. 1210 12. e11t.1 1►• 00 20. 01t.'l 6. -'1-03 14.00 3tZt. 00 9.00 :~2. ~~10 1 ILi. tZt0 3. 012, 2B. 0121 D DPVLl.) 10. @ZI 10.00 10. tZIIZI 1121. 00 1 ') .. Q)Q'.I SPRI N~'~LEH SYSTEM HYDf<►'=ll.lL IC AN(lL Yt:iI S JOB TITLE: CARLSBAD RESEARCH CENTER -LOT #48 CALC #1 ROOF WATER SUPPLY CURVE p F~! E - s s u H E - p s I 120*\\\\\ I \\\\\ I 110+ I :L,ZtlZI+ I 91Zt+ I 80+ I 70+ I I I 60+ 50+ 30+ I I * (--115. 0 p Si I~ 1530 Flo\.-', Test Point 0 X I============================== 20+ LEGEND X = Required Water Supply 84.85 psi@ 2083. 1 gpm 1121+ I 0 = Available Water Supply I 111. 15 psi (i::1 21Zt83. 1 gpm gpm II II II tZI +· -t-·--f-----·--·+--··-----·i-·-·-··--·--I-..... ·-·---.... --·t----·---··-·----·-,,_ ·1---.. -.... ·--.... ·--·---+· ........ ------··-----···-·i-···-··-_,, ··----.... --···-........... ,. 8001200 1600 2000 2400 2800 3200 3600 4000 FLOl..J <GPM) ACTION FIRE SYSTE1S 91H5 HARNESS ST. SPRING VALLEY, CA. 91977-3948 11 C~lLCUU-)T I ON # 1 A" HYDRAULIC CALCULr~T IONS FOH CRC LOT H"+8 c,~:lRLSB{-m, Ct=l. FI LE NUMBEf~: -::,l1-·-)'62 7--9--·98 ·--DES I GN DATA--· OCCUPANCY CLASSIFICATION: DENSITY:: AREA OF APPLICAJION: COVERAGE PER SPRINKLER: NUMBER OF SPRINKLERS CALCULATED~ TOTAL SPRINKLER WATER FLOW REQUIRED:: gpm/sq. ft. 31Z1t211Z1 sq. ft. 96 sq. ft. 34 sprinklers 1764. 1 gpm TOTHL W~➔TER REQUIRED ( including hose):: 226Lt-. i gpm FLOW AND PRESSURE (@ BOR): 1 7 t,'\ Lt,. 1 g pm @ 7 7 • 3 p S i SPRINKLER ORIFICE SIZE. 5/8 inch NAME OF CONH1(4CTOR: COF<NEf<STONE CONST f<UCT I OM DESIGN/L(,YOUT B't': BRIAN WEIT AUTHORITY HAl...1 ING J"URISDICTION:: CARLSBrm FIRE DEPT. CONTRACTOR CERTIFICATION NUMBER: C-16 38816Q CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE# 8926J521 HRS SYSTEMS , INC . ATU=lNH~, G~i SPFH M<LEF< SYSTEM HYDf<{~UL IC f:it''-'AL YSI S Pa~~e 1 Date:: 11/01/91 C::\762-·-lA JOB TITLE: CARLSBAD RESEARCH CENTER -LOT #48 CALC #1A ROOF WATER SUPPLY DATA SOURCE NODE TAG LJ 1 STATIC RES ID. FLOltJ PRESS. P~<ESS. 1]1 <PSI) <PSI> <GPM> 120.0 115.0 1530.121 AGGREGATE FLOW ANALYSIS: TOH:iL FLOW AT SOURCE TOTAL HOSE STREAM ALLOWANCE OTHEH HOSE STREf'.:iM ALLO~JANCES TOT{.'.\L DISCHARGE FHOM (4CT I VE NODE ANALYSIS DATA' NODE 11211 11212 11213 10L), 1 Q)~:i 106 11217 108 1 Qt'·) 110 1 1 1 112 113 114 115 116 1 17 118 1i9 120 12i 122 1 ·=· -;• i.... .. .> 124 12~5 126 127 128 129 130 131 132 133 134 TAG ELEVATION (FT) 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 2a.a 28.8 28.8 28.8 28.8 28.8 28.8 NODE TYPE AWHL. PRESS. 1:PSI) 1121·~-7 {ff SOURCE SPRINKLERS PRESSUF<E <PSI> 56.3 56.5 56. 7 56. () :57. 1 57.3 57.5 57 .. 7 57.9 ~56. 1 56.3 !56. 5 56.7 56.9 57. 1 57.7 56 .. Q) 56.2 ~56. 7 56.9 ~57. 1 a:::·-1 ·-:;• ._I I • ...> 57.5 ~3G. L1, ::;b. 6 56.8 57 .. IL~ 57 .. 5 ~:j7. 7 1]1 TOT~lL DEMAND <GPM) i::'.i::'.6 1+. 1 226L),. 1 .l),00. t2t 100. IZt 1 76.L•. 1 DISCHARGE <GPM} REG!, D PF{ESS. <PSI> ') 4. lt GPM GPM GPM GPM SPfU N~<LER SYSTEM HYDR~~UL IC ANt4L YS IS JOB TITLE: CARLSBAD RESEARCH CENTER -LOT #48 CALC #lA ROOF JODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE 151 152 153 154 155 156 157 1 ~.58 159 160 1('1 162 163 164 165 166 167 168 169 1 7tZl 171 172 173 174 175 176 177 178 179 180 181 182 183 184 21211 202 21213 2tZIL► 205 206 21217 208 2e,9 1 2 3 't r:::· ...J 6 ·7 I B -➔ 1 IZI 11 <FT) <PSI ) < GPM) 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 26. 26. 2t\. 26. 26. 26. 26. 26. 26. 26. 26. 8 8 B 8 B B 8 8 8 8 8 8 8 8 8 8 8 8 8 8 8 8 8 8 8 8 8 8 8 8 8 8 8 8 8 8 8 8 8 8 8 8 8 tZt 0 0 0 IZl 0 tZt 0 e, ei 0 ~<= 11. ~50 I-<= 11. 50 ~{=11. 50 I-<= 1 1. 50 •{= 11. 50 l-<= 11. ~5121 K=11. 50 I-<= 11. 50 ~•~:::::11. 50 I-<= 11. 50 K:::::11. 50 I·<= 11 • ~:itZt ~{=11. 50 I-<== 11. 5121 K==11. 50 I-<= 11. 5,:' ~\= 11. 50 I-<= 11. 50 K=11. 5Q'I K=l 1. ~50 K=11. 50 I-<= 11. 5tZt K=11. 50 I-<= 11. 5121 K=11. 50 I-<= 11. 50 •{=11. 50 I-<== 11. 50 •{= 11 • 5fl'I I-<= 11. 5tZI •<=11. 50 1-<=11. 5121 •<= 11. 50 I-<= 11. ~50 11 •• c:;; ..... , 1 "►• 2 11 •• 1 14. 1 14. 3 14. ':) 16. 0 1 -7 I • 8 20. c:· ,_J 15. 4 1 ~5 . l► 15. 4 1 i:::· .... , . 6 16. 3 17. c::· ,_J 19. 6 22 .. 7 27. 1 21. 4 20. 7 21l.'I. 4 i:::tZl. 4 20. 5 21. 0 22. 1 2L~. tZl 27. =· I.- 28. 0 27. 6 27. 6 27. -·, l 28 .. 2 29. 6 ·~·:::, uL.-• tZI ~5(1'.l. 8 50. 8 50 .. 8 '+7. <) L►7 • ':) 47. 9 L►8. 6 L~B. 6 l.1-8. 6 54. 7 55. 6 61. 7 5'+. 7 61. 7 C.:u I ...'>-'+. 7 {::d. 7 5it. 6 61. 7 -.:.::·L ,_J ~. L► 61. 7 43. B 43. 3 4 -:i· w• 2 43. 2 1►3. ,~· .::J 1►4. 3 '+5. 9 48. 5 52. 1 4c--~ ...., . 1 .l.5. 1 45. 1 I. i:::· • ,_J. c;; ,_J 1t6. '+ 48. 1 50. 9 54. 8 59. q i::"-, ..:.,~. 2 52. 3 i::;;.-, ..JC.. e, 51. (:) 52. 1 52. 7 51+. 0 56. I.~ 59. 9 60. 9 60. c;; ,_J 60. L► 60. c::-.... , 61. 1 62. 5 65. QI _., -· --· --·---··· -· -· _., -·-·-·-~ ----- ...... ..... -·- ---- ·---- ---- ...... ·--... _ ---· ----♦--- -. ... -- --·-···- --~ -· -- .... ··--·- ---- --·-· _,. ---- .,_ ·---- SPRINKLER SYSTEM HYDRAULIC ANALYSIS JOB TITLE: CARLSBAD ~1ESEt➔RCH CENTER ..... LOT :1=~-4-8 CALC # 1 A ROOF JODE H~G ELEVATION NODE TYPE PRESSURE DISCHARGE 12 13 14 14f4 15 16 17 18 1 '3 20 2 1 .::..:::.A 23 2.1.. 2Li-A 25 26 27 28 29 30 3Q1A 31 TOR BOH U5 U4 U3 U2 Ui <FT> <PSI) <GPM) 26.0 26.0 26.0 26.0 26.0 26. 121 26.0 26.0 26.0 26.0 26.0 26.0 28.8 26.0 26.0 28.8 26.0 26.0 26.0 26.0 26.0 26.0 28.8 26.0 25.5 0.5 -3.0 2.0 2.0 --3. 0 -3.0 HOSE sn1EAM SOURCE 60. 1 53.9 •=~~ ..... "7 , .. J.5. I ~i9. -'1- 53. 5 58 .. 9 53.0 58.3 57.8 52. 1 L1-8. 6 57.6 52.121 47.9 .l.1-2. 5 38.6 17.0 L1-0. 3 57. 11- 52. 0 5e,. 8 61.8 Tl . 3 83.8 88.8 92.6 SJL1-• L1. 1 Qt0. QI SPHIN~\LER SYSTEM HYDR~lUL. IC t4NALYSI S PagE• L► JOB TITLE: CAHLSBAD HESEAHCH CENTEH --LOT #4B CALC #lA HOOF' PIPE DATA PIPE TAG G! <GPM) Dlt:'.l<IN> LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW<C) CF--n SUM. NODES <FT) < K) <PSI> (GPM) F. L. /FT <PSI> Pipe: 1 --57. 1 2.203 PL 20. 33 PF e,. 9 1 26.0 0,. 0 5L►• 7 0. 0 L•• 8 120 FTG T2L PE 0.0 •::, ._ 26. e, 0.0 55.6 0. 0 0. 121~~4 TL 36.33 PV 0.2 Pipe: 2 --57. 1 2.203 PL 70.00 PF 2. Q.i 2 26.0 0. 0 55.6 0.0 4.8 120 FTG T PE 1.2 101 28.8 0.0 i:•-r .:Jt.,. 3 Q.i. 0 l[.i. e121~ TL Bili. 00 PV 0.2 Pipe: 3 ..... 57. 1 2.203 PL 8. !Li0 PF 0.2 HH 28.8 0.0 ~;6. 3 0.0 4.8 120 FTG PE 0. 0 1e,2 28.8 121. Qt 56.5 0. 12) 0.024 TL 8.00 PV 0. ~:'. Pipe:•: "I· -57.0 2.203 PL 8. 0Q.i PF IL•. 2 102 28.8 0. e, ~36. 5 121. 0 L1 .• 8 12121 FTG PE 0. ILi 103 28.8 0.0 56.7 0. 0 0. ll.124 TL 8.00 PV 0.2 Pipe: i:::-...J ..... 57. 1 2.203 PL 8.00 PF 0.2 11213 28.8 0.0 56. 7 0.0 L •• B 120 FTG PE l[.'i. 0 104 28.8 0.0 ~56. ':) 0. !l) 0. 1Z12L~ TL 8.00 PV 0.2 Pipe: f.\ -··57. 0 2.203 PL 8. ll.10 PF Q.i. 2 104 28.8 0.0 ~56. 9 0.0 4 .. 8 120 FTG PE 0. IZI 105 28. 8 0.0 57. 1 0.0 0. 02"• TL 8. Q,i('l PV 0.2 Pipe: -, I ..... 57. 1 2. 2e,3 PL 8.00 PF 0. ~:'. 11215 28.8 0.0 57. 1 Ill. 121 4.8 12Q.1 FTG PE !Li. 0 106 28.8 1Z1. 0 57.3 0.0 0. 02-4-TL 8.00 Pt..' 0.2 Pipe: 8 --57. Q,1 2. 2Q.i3 PL 8.00 PF 0.2 106 i~8. 8 0.0 57.3 0.0 '+. a 120 FTG PE tZI. IZt 1 tZl7 28.8 0.0 57.5 0. ll_'l 0.024 TL 8. 01l.'l PV 121. 2 Pipe: ') ·--5 7. 1 2. 21213 PL 8.00 PF 121. 2 107 28.8 0.0 57.5 Q,i. ill L~. 8 121l'l FTG PE 0.0 11218 28.8 ei. e, 57. 7 li..i. 0 0.024 TL 8.00 PV 0. ~:'. Pipe: 10 -··57. Q,'\ 2 .. 203 PL 8. l[.11[.1 PF 0.2 108 28.8 0. 121 57.7 0.0 L~. 8 120 FTG PE 0 .. Ill 10C) 28. 8 0.0 57.C) ll_'l. l[.i 0. 02"• TL 8.00 PV 0.2 Pipe: 11 ·--~57. l 2. ~~03 PL 87.00 PF 2.6 11219 28.8 0.0 57.9 0.0 4.a 120 FTG 2T PE 1. i:~ --:;-, .. .> 26.0 0.0 61. 7 e,. 121 IZI. 024 TL 107. 00 PV 0.2 Pipe: 12 --58. Si 2.203 PL 8!l'l. 00 PF 2.6 L~ 26 .. 0 0.0 5L►• 7 0.0 ~5. IZI 120 FTG 2T PE 1. ~:'. ' 11121 i:~8. 8 121. 0 56. 1 121. 0 ll.'l. 026 TL 100. 00 PV e1. 2 Pipe: 13 -·-58. ':) 2.203 PL 8.00 PF 0.2 11 e, 28.8 0.0 56. 1 0. 0 5.0 121Li FTG PE fl•. 0 111 28.8 0.0 56.3 0 .. 0 !li. 026 TL 8.00 P\.' 0.2 ' SPRIM\LER SYSTEM HYDHAULIC ANr~LYSIS Page i:::· ..J JOB TITLE: CA~<LSBAD RESEAHCH CENTER ···-LOT #L~B CALC #lA HOOF PIPE DATA (cont, d) ..j PIPE TAG Q(GPM> Dir~<IN> LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS> Hli<J (C) <FT> SUM. NODES <FT> ( K) <PSI> <GPM) F. L. /FT <PSI> Pipe: 14 ---~)8. () 2. 2,213 PL 8. 1210 pi:;:-,z,. 2 1 1 1 28. B 0. 0 56. 3 0. 0 ,::-..., . 0 120 FTG PE !l'l • 0 112 28. 8 tZl.tZI 56 .. 5 tZt.tZI 0.026 TL 8.00 PlJ 0. 2 Pipe: 15 -58. 9 2. 203 PL B. 0!l'l PF fl). 2 112 28.8 tZI. 0 56. i:-.-0.0 ..., i::~ ,J • 0 120 FTG PE 0. 121 113 28. B 0. tZ1 56. 7 0. '':i 0.026 TL 8. 00 PV 0. 2 Pipe: 16 ·--58. I.) 2. 2t2'3 PL 8.00 PF tZI. ·:::, I- 113 28. B 0. 0 56. 7 0. 0 5. tZI 120 FTG PE ILi. tZl 114 28.8 0. tZI 56. ',) 0. tZI 0. tZ126 TL 8.00 PV 0. 2 Pipe: 17 ·-58. 9 ·=· i.:~03 PL 8. 00 PF 0. .-, L-. C ' 114 28.8 0. 0 56. I.) t21. tZI 5.0 120 FTG PE 0. 0 115 28. 8 tZI. 0 57. 1 IL'l. ll'i tZt. 026 TL B. 00 pl.,.1 !li. 2 Pipe: 18 --~)8. ':) 2. 2iz,3 PL 8. 00 PF 0. 2 115 28.8 '1.'l. 0 57. 1 0. 0 c:· -..., . QI 12Q.'l FTG PE t21. 0 116 28. 8 0.0 ~57. 3 0. 0 0.026 TL 8.00 PV 0. 2 Pipe: 19 --58. 9 ·-· ...... 203 PL 8. 01L'l PF 0. 2 116 28. 8 0.0 57. 3 0. 0 L-::" ei 120 FTG PE tZI. 121 ~J. 117 28. 8 0. 0 c::-... , ...J I • 5 Q.'l. tZt ll•. 026 TL 8. Q.'10 plJ Qi. 2 Pipe: 20 -.. ~:;8. () 2.203 PL 8. 00 PF' 0. 2 117 28. 8 0. 0 c::--1 c::· 0. 0 ,--0 12Q.'l FTG PE 0. Ill ..J I • ..., .J • 118 28.8 tZI. 0 57. 7 tZI. 0 121. 026 TL 8. ll.10 PV ei. i::: Pipe: 21 -58. C) ·=· L-. 203 PL 87. 1£10 PF 2. 8 118 28.8 0.0 57.7 0. ei 1:::-0 1 ;:::1Zt FTG 2T PE L 2 ,.J. c.-..J 26. 0 0. 0 61. 7 0. tZI Q.'l. 026 TL 107. 00 PV !l1. 2 Pipe: •::,.•::,. ... -~59. 1 -:::, 203 PL 80. 01l.'i PF 2 • 6 '--'-L-. 6 26. 0 e,. 0 5.L •• 7 0. e, ,:· !l'l 12121 FTG 2T PE 1. 2 ..., . 11 {) 28. 8 0. 0 56. 0 0.0 0.026 TL 100. 00 Pl.-' tZI. ~~ Pipe: 23 --59 . 1 .-. 203 PL 8. 00 PF 0. 2 c. 11 '-) 28. 8 0. 0 ~)6. 0 e,. 0 1::.~ ..J. It) 120 FTG PE 0. e, 12e, 28. 8 0. e, 56. 2 0. 0 0. 026 TL 8 .. 0tL'i PV 0 .. 2 Pipe~ 2L~ ·--59. 1 ·::, L-. 203 PL 8. e10 PF 0. 2 12121 28. 8 0. 0 56. 2 Q). e, ~.). (~ i f:ll'l FTG PE (Li. 0 121 28. a 0. 0 56. 4 0. IZI e,. 026 TL 8.00 PV 121. i:::'. Pipe: 25 -··::.iC). 1 · ... • ...... 203 PL 8. 00 PF !l'i. 2 121 28. 8 0.0 56. 4 e,. 11..'i 5. IZI 120 FTG PE tZI. 121 122 28. 8 Q.'l. 0 i:::· r ...>b .. 7 0. ll.'l !l'l. ll'l26 TL 8. 00 PV 0. 2 Pipe: 26 --59. 1 2.203 PL a. 00 PF It). i:::'. 122 28. 8 0. tZl 56. 7 ll,'l. tZI c:· fl'\ 120 FTG PE 0. 0 ,.J. 123 28. 8 0.0 56. 9 0. tZI 0. 026 TL 8.00 PV 0. 2 SPF~ I N~<LEF< SYSTEM HYDH~lUL IC ANt4L YSI S Page 6 JOB TITLE: CARLSBAD HESEARCH CEMTEI~ ··-LOT #48 CALC ~HA HOOF PIPE DATA (cont' d) PIPE TAG Q(GPM> Din<IN> LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL<FPS) HW(C) <FT> SUM. NODES <FT) 00 <PSI> <GPM) F. L. /FT <PSI> Pipe: 27 --5':). 1 2. 203 PL 8.00 PF 121. 2 123 28. 8 0. 121 56. Cj 0. 0 ,::-.. J. !l) 120 FTG· PE 0. fl) 124 28.8 iti. 0 57. 1 0.tZI 0. 02G TL B. IZttLi pi..,1 tZI. 2 Pipe: 28 -59. 1 .-, i::03 PL 8. 00 PF e,. 2 C." 124 28.8 0. 0 c:.--7 ..JI• 1 0. IZl 1=· 0 12121 FTG PE 0. 0 ..., . 1 .-,i= C..J 28. 8 ei. Ill 57. 3 0. 0 0. IL'i26 TL 8. 01l.'i PV Q.). 2 Pipe: 29 ·-~jg. 1 2.203 PL 8.00 PF IZl.2 125 28. 8 Ill. 121 57. 3 e,. 0 s:::· .._,. tZI 120 FTG PE 121. Q.'l 126 28.8 0. 0 1:::-7 -..JI • r.~-121. ..., 0 Q). 026 TL 8. 00 PV 0. 2 Pipe: 30 -59. 1 2. 203 PL 8. 00 PF 0. 2 126 28.8 0.0 i;::-7 ..J I • 1::.~ 0. ...J 0 5.0 120 FTG PE 0. li..i 127 28. 8 0. 0 57. -7 I 0. e, 0. tLi26 TL 8. e,0 PV 0. 2 Pipe: 31 --59. 1 2. 203 PL 87. 00 PF ..... , 0 i:::.. 127 28. B 0. 0 57. -7 0. 121 i:::· fl) 120 FTG 2T PE 1. .. ::, I ..., . '- 7 26.0 0. 0 61. 7 0. 0 0.026 TL 107.00 P'v' 0. 2 Pipe: 32 --59. b 2. 203 PL 96. 0Q.'l PF 3. 1 B 26. 0 0.0 5L~. 6 e,. tZt i:::-0 120 FTG 2T PE 1. 2 ..., . 128 28. 8 0. e, 56. .l~ 0. tZi fl). lli26 TL 116. 0fl) PV 0 • 2 Pipe: 33 -·-59. b 2. 203 PL 8. 00 PF 0. ~~ 128 28. 8 0. 0 , ... ,. J'.~ 0. e, i:;:· ei 12lli FTG r.:cE 0 • ~) ..::Jt."l. ...;. 12'-) 28. 8 0. ii) 56. 6 0. 0 0. 026 TL 8.00 PV IZI. 2 Pipe: 3L► --59. [, 2. 202~ PL 8. 00 PF 0. .-. i::. 12'=) 28 .. 8 0. 0 56. 6 0. QI 1::-0 U::0 FTG PE ILi. IZl ..., . 1312.i 28. 8 0. flt 5("\. 8 fl). e, fl). 026 TL 8. 01Li PV fl). 2 Pipe: 3~-5 ···-59. 6 :::. 203 PL 8. QIIZI PF. 0. 2 13121 28. B 0. 0 56. 8 fl). fl) i:::· ..J. It) 12fl) FTG PE 0. tt) 131 28. 8 0. ~~ 57. IZI 0. ILl e,. IZli::~6 TL 8. 00 PV Ill. 2 Pipe: 36 -·59. 6 .···, 203 PL 8. 00 PF Q'l. 2 Ca 131 28.8 0. 0 57.0 0. l°l't 5. tZI 120 FTG PE 0 .. IZl 1 ·:.··-, wC. 28. 8 0. 0 i:::·7 -....J I • 3 0. fl) 0. 0f:6 TL 8. t21Q.'t PV 0. 2 Pipe: 37 --~59. 6 2.203 PL 8. tZIIZI PF 0. ·:::4 L- 132 28. 8 ei. 0 57. --:; .. .._, ei. t2l i:::· ..... , . 121 12Q.'t FTG PE 1Z1. Ill 1 ""'--. 28.8 0. 0 57. 1:::-0. t21 1Z1. 02G TL 8. 00 PV tZI. 2 ~~ ..., Pipe: 38 -··59. 6 ·::, a..... 203 PL 8. ll.10 PF 0. 2 133 2H.8 0.0 c:~-... , 5 0. e, r~-0 120 FTG PE ILi. 1Z1 ...JI" ...,,. 134 28. 8 0. tZl 57. -7 I 0. izi fl). '2126 TL 8. fL'\0 PV 0. 2 Pipe: 39 -··59. G · .. -• a..... 2,z,3 PL 87. 00 PF -::, ..... .. n 13.t'.t 28. 8 e,. 0 57. 7 fl). 0 i:::· ..., . 0 12Q.'t FTG 2T PE 1. 2 9 26.0 0 • e, 61. 7 0. e, 0. it.'t26 TL 107 .. e,0 PV e,. 2 SPRINl·<LEH SYSTEM HYDH~lULIC ANALYSIS Pc.-\Q e:• 7 JOB TITLE: CARLSBAD RESEARCH CENTEH -·-LOT #48 CALC #lA HOOF PIPE DATA (cont' d) PIPE Tf-'.lG G! (GPM) DIA<IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL<FPS) Hl.-J < C) <FT) SUM. NODES <FT) < K) (PSI) <GPM) F. L. /FT <PSI) Pipe: 40 ··-60. 4 2.203 PL 231. 1Zt0 PF 7. 3 10 26. 0 0 .. tZl 5L►• L► Ill. 0 5. 1 121l't FTG L•T PE 121. 0 1 1 26. 0 0. 0 61. 7 0. Q.'t 0.027 TL 271.00 P'vl 0. 2 Pipe: L►f -··53. 1 ·::, L-. 203 PL 231. 00 PF i:::· ,_1., B 12 26. 0 0. 0 54. 3 ei. 0 L►., i::.· 120 FTG L. T PE 0. Q1 ....J 13 26.0 0. 0 60. 1 0. fl'\ 0. 021 TL 271. 1t.'t0 PV 0. 1 Pipe: 42 ·--51.. 6 ·::, 21Zt3 PL 231. 1210 PF i:::-i;;.- L-. ._J. ....J 1 '+ 26. 0 0. 0 a::.·-·. ._J.::,. 9 0. 0 1, .. 3 12ll'l FTG L•T PE 0. 0 15 26.0 0. 0 59. 4 e1. !2.'t 0.020 TL 271. 1Zt0 PV tZl. .t Pipe: L►3 --50. 8 ·=· L-. 203 PL 231. !i.'t0 PF i:::· ,_,. 3 16 26.0 0. e, 53. c::-0. tZI Li• • ... ~·-120 i::.--TG '+T PE IZI. 121 ._J ,..J 17 26. 0 0.0 58. Cj !i.'t. !i.1 121. lli2tZI TL 271. 0il't Pt...' 0. 1 Pipe: 4'+ --~3e,. 6 2. 2!i.'t3 PL 231.00 PF i::.-3 ._J. 18 26. 0 0. 0 53. 0 QJ. 0 l► • 3 121l'l FTG L•T PE 0. ei 19 26. 0 0. e, 58.3 0. 0 e,. 1Zt21L't TL 271.00 P'.,' 0. 1 Pipe: 1•5 143. 5 2 .. 203 PL 1 :.:_;2. 33 PF ·::, -;-L. .. '--'. 1 20 26. 0 0.0 52. 4 0. e, 1 f:. 1 120 FTG 2T PE 1 ····, • i::. 178 28. 8 11. 5 28 .. 0 60. 9 0. 13.i'.• TL 172. --... ·-·. ..::,..,:_, pt.) 1. It) Pipe: 46 82. 6 2. 212,3 PL 8.00 PF ~:). 't 178 28. 8 11. c:-..J 28. fi.1 61t.'t. 9 7. 0 121l't FTG PE 0. 0 179 28.8 11. 5 27.6 60. 1:::· 0.048 TL 8.00 PV tZl. . ..., . ...J \..J Pipe: L~7 22. 1 2. 203 PL 8. !i.10 PF ll'l. 0 179 28. 8 11. 5 27. 6 6tZ1. 5 1.9 12tZt FTG PE !Li. IZI 1ae, 28. 8 11.5 27. 6 60. L1. lli. 001+ TL 8. 00 pt.,1 Ill. 0 Pipe: 48 --38. 3 ·::, L-. 21213 PL 8. e10 PF 0. 1 1a0 28. 8 1 j_,. i:::· ..) 27. 6 6Q1. L• "7;· ..., . 2 12e, FTG PE 0. 0 181 28. 8 11. 5 27. 7 &e,. 5 0.012 TL, 8. 00 PV tZI. 1 Pipe: 1,.9 -·-98. 8 2. 20~: PL 8. t2til't PF e,. 5 1 a 1 28. 8 11. c:-~::7. 7 60. 5 a. 7 12il't FTG PE 0. e, ....J \..J 182 28. 8 11. 5 28. 2 61. 1 0. !i.167 TL 8. 00 PV 0. c:· ,_I Pipe: 50 ·-15'). ·::.) 2.203 PL 8 .. lltQ.'l pr:--1. ··.(" ,_., 1a2 28. 8 11. ,::· 2a. 2 61. 1 12;. c::-120 FTG PE lli. e1 ._J ._J 18:3 28.8 11. i:·-2<3. 6 62 .. r..:· e1. 164 TL 8. 01L't PV 1. ~~ ,.J ....J Pipe: 51 -··22f~. ;;:;:· ,_I ·::• L-. 21l'l3 PL 8. (!)0 PF -::, L-. Lj. 183 28.8 11. L-· 2'3. 6 62. i::.-1 t1. .. 7 120 FTG PE 0. e, ,.J ,J ' 184 28. 8 11. c .. ..) --;• ·::-....,.._. ei ,. i:-· t_'\ .::., • IL• Ill., 31212 TL 8. !i.10 PV -::, L-. L1 . Pipe: 52 ·--287. ,::.-2.203 PL 30.67 pi::-~::4. 6 ....J 184 28. 8 11. i:::-._J 32. 0 65. tZl 21, .• 2 120 FTG 2T PE 1.. -::-..... 21 26.0 0. 0 57.8 0.0 e,. .lt86 TL 50.67 PV -·;-..., . <) SPHIM<LEH SYSTEM HYD F~r.:1UL 1 C r~M4LYS1 S Page 8 JOB TITLE: CARLSBAD HESEAHCH CENTER -LOT HLi-8 Ct➔LC #lA HOOF PIPE DATA (cont' d) PIPE TAG Q(GPM> DIA<IN) LENGTH PRESb. END ELEV. NOZ. PT DISC. tJEL (FPS) H~J < C) <FT) SUM. NODES <FT> 00 (PSI> <GPM> F. L. /FT <PSI> Pipe: 53 169. 2 2.203 PL 2. 83 PF ·=· I...,. 3 22 26. 0 0. 0 52. 1 0. 0 1 .li-. 2 12e, FTG T PE 1. 2 22A 28. B 0. 0 48.6 0. 121 0. 182 TL 1 .::, 1.-. 83 PV 1. i. Pipe: 5.l► 169. 2 ·::, 2eI3 PL 139. 17 PF ·::,, ·::, 1.-. 1.-I • 1.- 22A 28. 8 0. 0 '+8. 6 0. 0 14. 2 120 FTG T PE 0. tZt 169 28. 8 11. C ,.J 21. L), 53. 2 ll.1. 182 TL 1 .l►Cj. 17 PV 1. -'► Pipe: 5~5 116. 1 ·:.':• 1.-. 2il'l3 PL 8. 00 PF 0. 7 16<) 28. 8 11. c:.-21. .l. 53. -:.~, '.:>. 8 120 FTG PE e,. Q'I -....J 1.- 170 28. 8 11. 5 20. 7 r::: ,•-, 3 !Li. 091 TL 8. 00 PV 0. 6 ..JC ■ Pipe: 56 63. 8 2. 203 PL 8. 00 PF ll'I • . -. .::.. 1·n~ 28. 8 11. 5 2eI. 7 52. 3 t:. .. ,.J. 4 120 FTG PE 0. tZI 171 28. B 11. 5 20. L► 52. tZI 0. Q.130 TL 8. ll'l0 PV 0. ·=-.• ,._ Pipe: 57 11. 8 · ... • 1.-. 203 PL 8. 00 PF--0. 12) 171 28. 8 11. 5 20. 4 52. 0 1. tL1 1212.1 FTG PE 0. 0 172 28. 8 11. 5 20. 4 51. 9 0. 001 TL a. 0e, PV 0. 121 Pipe: 58 --.l1-0 . 1 -::., 1.-. 212)3 PL 8. 12.'lll'I PF 0. 1 172 28 .. 8 11. 1:::· 20. l► 51 • !-) Hl· 4 120 FTG PE 0. IZI ,.J ,.., . 173 28. 8 1 {. i:::· ,.J 20. i::: 52. ,.J 1 tt'I. 013 TL 8. fl'l0 P\J 0. 1 Pipe: 59 ·-92. 2 ·:::. 21Zt3 PL 8. 00 PF 121. i::· 1.-. ,.J 173 28. 8 11. c::· ,.J 20. i::-..) 52. 1 .. ,' I • 8 1i.::0 FTG PE 0. Q'I 17lt 28. 8 11. ,:;.~ ... J 21. 0 52. 7 0. 0~5') TL 8. e,e1 P'.,' 0 .. it Pipe: 60 -1 L•l• • C) ·::, 1.-. 21213 PL 8. 00 PF 1. 1 174 28. 8 11. c~~ 21. 0 5i:~. 7 12. 2 li::'.0 FTG PE IZt. tZI -..J 175 28. 8 11. i:::-·:::,·=· 1 a:::·' 0 0. 1 -,;.-, TL 8. 00 PV 1. ll1 ._, I... I.-. ..J-'·• • ...> I Pipe: 61 ····198. 9 c .. 203 PL a. 00 PF ·::, 1.-. IZI 175 28. 8 11. 5 22. 1 i:::·1. ._J t. Q) 16 .. -7 I 12'1.'1 FTG PE t21. IZI 176 28. 8 11. c:.~ 2L1-. tZI 56. Li-ILi . 2L1-6 TL 8. 00 P\r' 1. t) .....J Pi pe: 62 --255. 2:; ·::, 203 PL 8. 00 PF -•. 1 1.-. '-'• 176 28.8 11. i:::-,.J 24. 0 56. 4 21. 5 120 FTG PE 0 .. 1Z1 177 28. 8 11. 5 27. 2 ~/:>. 9 ll'I. 390 TL 8. IZlll'I P\rl 2:;. 1 Pipe: 63 ·--3 15. 2 ,::, 21213 PL 30. 67 PF 29 .. .. •-. 1.-. i:::. 177 28. 8 11. 5 27. 2 59. Cj 26. ,::-120 FTG 2T PE 1. 2 ,.J 23 26. 0 0. ll'I ~57. 6 0. Qt 0" 576 TL 50. 67 pl.} 4. -;,• Pipe: 611-188. i:::· ·::, 203 PL -::, B-;• PF ........ 9 ,.J 1..-. 1.-. ._. a::.. 24 26. 0 0. tZl 5i:~. IZt tZI. ll'I 1 ~3 . () 120 FTG T PE 1. 2 24.:l 28. 8 121. tZI 47. 9 tZI. 0 0. 222; TL 12. 83 PV L -7 I Pipe: 65 188. c·-.J 2. 21213 PL 20. 1210 PF G. -T l 24(~ 28. B 0. tZI L•7 • C) tZI. IL'I 15. 9 120 FTG T PE 1. 2 25 26. 0 0. 121 4·::, "-• c::-,.J e,. 0 0. 223 TL 3,z,. IL'l0 PV 1. 1 SPFHM<LEF< SYSTEM HYDF<AULIC ANALYBIS Page <:1 JOB TITLE: CARLSBAD RESEARCH CENTEH -·· LOT :j:~48 CALC #lA ROOF PIPE DATA (cont• d) PIPE Tf.4G C! <GPM) DIA<IN> LENGTH PRESS. END ELE'v'. NOZ. PT DISC. t.,1EL <FPS) H~J ( C) (FT) SUM. NODES <FT> 00 <PSI> ( GP1·t1) F. L. /FT (PSI) Pipe: 66 113. 7 2. 2Q)3 PL 21.,-. 5121 PF -:;-..., . 9 25 26. 0 0. 0 4--, a::. • t::· 0. ..... 0 9. 6 120 FTG 2T PE 0. 0 26 26.121 0. 121 :~8. 6 Qi. 121 Q1. lZl87 TL 44. ~30 PV IZI. 6 Pipe: 67 188. i:::· ,_I ·=· L... 203 PL 87. 12)0 ·PF 21. 6 26 26. tZl 121. 0 38.6 121. 0 15. 9 120 FTG T PE 0. ~~I 27 26. 0 0. 0 17. 0 0. 0 0.223 TL 97. 00 Pl,,• 1. -7 I Pipe: 68 71. 4 2.203 PL 7. 0121 PF 0. Lt- 27 26. 0 121. e, 17. fi 0. it:1 ,. b. !li 12it.'I FTG L PE 1. 2 160 28. 8 11. 1:::-1 i::.--4 45. 1 0.037 TL 10. 00 PV 0. ..... ,._J ..J. i:;-_ , Pipe: 69 26. 3 2. 203 PL 8. 1Li1Zt PF !Li. 0 160 28. 8 11.5 15. 4 , ,:·~ Lt-..:,. 1 2. 2 120 FTG PE 0. ,~, 161 28. 8 11. 5 15. .l. I. i:::· ·I-..J. 1 0. 0e1€." TL 8. fi0 PV 0. IZl Pipe: 70 --18. 8 2.203 PL 8. 1210 PF' Ill. It) 161 28. 8 11. 5 15. 4 Lt-5. 1 1. 6 i21l.'I FTG PE 0. 0 162 28.8 11. 1:::-,._J 1 •==-,_J. 4 4i::.~ ,._J. 1 IZI. 003 TL 8.00 Pl,,I 0. 0 Pipe: 71 r -·. --t_'\.:,. 9 ·=· L-. 203 PL 8. !lilZt PF 0. 2 162 28. 8 11. c::-15. 4 45. 1 •= 4 120 FTG PE 0. Ql ,_J ,_J. 163 28. 8 11. 5 15. 6 Lt-5. i:::· ..... , 121 • !l)30 TL 8. 0121 PV tt.'l. 2 Pipe: 72 ···-10':). .. ._ 2. 203 PL 8.00 PF 0. 6 .. ., 163 28. 8 11. a::· 1 c:· 6 , i:.-c:-9. 2 120 FTG PE it). Q) ..J ..J. "·•..) . .._, 161+ 28 .. a 11. c:.~ 16. 3 -4-t~. "• 1Li .. 0B1 TL 8 .. 00 PV 12.i. b ,._J Pipe: 73 1 cc:-7 -::, 203 PL 8. 00 PF 1. -·. -,J..J. L... .::, 16.l• 28. 8 11. r.:..~ 16. -;-46. Lt-1 "A' 1 120 FTG PE 0. ,~l ,._J ,.., ..., . 16~ 28. 8 11. C 17. 5 Lt-8. 1 Ill. 156 TL 8. 00 PV 1. ·-·· ,._J L.. Pipe: 7L► . --·212t3. 8 2.203 PL B. 0121 PF <::• 1.-. 1 165 28. 8 11 '. 5 17. a::· 48. 1 1 -, 2 120 FTG PE Q.1. 0 ,._J I • 166 28. 8 11. C" ..... 19.6 50. 9 0.257 TL 8. 00 PV ~::, tZt ,_J '--. Pipe: -1c:.: --254. -, 2. 203 PL 8. 00 PF 3. 1 '..J I 16G 28. 8 11. c~~ 1(). 6 5tZt. 9 21.. Lt-12121 FTG PE e,. 0 ,_J 167 28. 8 11. i:::· ,_J ·::,-::, L..L... 7 5Lt-. 8 Ill. 388 TL 8. 00 pt..,• -:;-..... . 1 Pipe: 76 ··-31£.i'). 1::~ 2. 2tZt3 PL 8. 1210 pi:=-'-•. ,:;.-,J 0 167 28. 8 11. ,:;:· ..J ·::,·::. L...L... 7 ,:· .l ,_J •• 8 26. 1 120 FTG PE it). ei 168 28. 8 11. L-::-27. 1 59 .. ':) 0. 5~57 TL 8. IZt0 pl.,} '+. 6 ,_J Pipe: 77 -·-369. LJ. · ... • '-. 20~~ PL 5. 5121 PF 12. e1 168 28. 8 11. 5 27. 1 59. ') 31. 1 12121 FTG T PE 1. ·::, L- 28 26. 0 0. ll.i L•0 • .. :;. 0. 0 ,~. 773 TL 1 C: 50 PV 6 • c::· ..., ..J. ,._I Pipe: 78 ·--66121,. 2 --~ .. ..., . 314 PL 25. 17 PF 1 7 . l 28 26. 0 ei. 0 Lt-Ill. 3 0. 0 21 •• 6 120 FTEi 2T ~•E Ill. Q) 29 26.0 tZI. tZt 57. 4 0. 0 0. 310 TL 55. 17 PV L• • 1 SPHIN~<LER SYSTEM HYDf<(-=lUL IC ANf4LYSIS Page 1 e, JOB TITLE: CARLSBAD RESEARCH CENTEH ···-LOT H48 C(.'.:)LC ~HA ROOF PIPE DATA (cont' d) PIPE TAG Q(GPM) DH.'.l<IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. lJEL<FPS) HW(C) <FT> SUM. NODES <FT> 00 <PSI) (GPM> F. L. /FT <PSI> Pipe: 79 7-4 . 8 2. 203 PL 56.50 PF -~ ..., . <) .-.c::-26. 0 0. 0 11-2. c::-0. 0 6. ~ 120 FTG L1-T PE 0. IL'l a::. ... , ...J 26 26.0 0.0 38.6 e,. IZt Qt. tL'l4IZ1 TL •=)6 . 50 PV 0. 3 Pipe: 80 117. 1 2. 2e,3 PL 11. 012.'l PF 1. 3 27 26.0 0. 0 17.tZl 0. 0 9. ':) 120 FTG L PE L ·::, L-. l '.5 1 28. 8 11. 5 111-. c:· ...J L.3. 8 0. 092 TL 14. 00 P\r' e,. 7 Pip~::: 81 ·7 .. ; . I '-' • . .._ ~ 2.203 PL 8. 121121 PF 0. ··;• .. ., 151 28. 8 11. c:· ...J 1 Lt. 5 I. ~--. .. ~ . 8 6. 2 120 FTG PE l,{_1. Q) 1 ,::.-.-, ..JC 28.8 11. i::.-l .£1-• 2 ,._J 43. 3 tZI. 039 TL a. e,0 PV tZI. 3 Pipe: a--. a::. 3!l'l. 0 ·-·' L.... 21213 PL 8. etll'l PF !l'l. 1 152 28.8 11. 5 14. 2 43. .. .,_ c~. t::· 12121 FTG PE 0. 0 ..., ..J 153 28.8 11. 5 14. 1 42;. 2 0. 007 TL 8. 00 PV e,. 0 Pipe: 8...,_ ~ .. -13. 2 -::, I-. 21L'l3 PL 8.00 PF tZt. IZt 153 28. 8 11. i::.-1 '-•. 1 l.1-3. ·::, 1. 1 12il'l FTG PE e,. 0 ...J L... 154 28.8 11. 5 14. 1 43. 2 0. 1L'l1ZI2 TL 8.00 PV 121. IZt Pipe: 84 --56. L1-2. 21Zt3 PL 8. 00 PF 0. 2 154 28. 8 11. a:::· .::J 14. 1 43. 2 Li-• 7 120 FTG PE 12,. e1 155 28. 8 11,. 5 1 L1 .• 3 .L .. 3. ,-~ .::J il'I • 021 .. TL 8. 0Q.i PV 0. 2 Pipe: 85 ···-':J'j . 9 2. 21213 PL 8. 00 PF 0. 6 155 28. 8 11. i:::-14. 3 i. -··· ...J ·~-i:::· ..J 8. .L .. 12fli FTG PE 0. lli 156 28.8 11. 1:-.:· 14. CJ 4-'I-• .. , 0. tZt6•=) TL 8. 00 PV 0. 5 ...J ..:!> Pipe: 86 -1'-IA . 3 ·=· 203 PL 8. 1t:i1Zl PF L 1 L.... 156 2B.B 11. 5 1 L1. • 9 lt.l .. • .::; 1 ·::, . I-. 1 120 FTG PE (L). Ill 1 i=-7 ...JI 28. B 11. 5 16. e, 45. <:) 0. 136 TL 8. 00 PV 1. 0 Pipe: 87 ···-1912•. 2 ·=· 2Q'.t3 PL 8. 0121 PF 1. 8 I..... 1 !:j7 28. 8 11. i:::· 16. ei L ,::· ':) :l 6. !Li 120 FTG PE 1t:i. 0 ...J ...... , . 158 28. 8 11. 5 17.8 -'t-8 . c:.-0. 226 TL 8. IL'ltZI pt,,' 1. 7 ,_J Pipe: 88 -238. 6 2 . 203 PL 8. IZllli PF. ·-·' I..... 8 158 2B. 8 11. c::-1 7. 8 1t8. i::· 2121. 1 120 FTG PE 0. tZ1 ...J ...J 159 28. 8 11. C"" ...) 21l'l. i:::-...J 52. 1 e,. 3 1t-4 TL 8. 0~~ ~•v ·=· L-. 7 Pipe: 8<) -·-2<)0. ·7 I c. 203 PL 1 .. 7 I • 50 PF 18 .. 6 159 28. B 11. i:::· ..J 20. c:-..J 52. 1 2-' ... ,:-· .::J 121.l'l FTG 2T PE 1. 2 28 26. ei 0. 0 '-t-0. ...... tZt . Q..i 0. 496 TL 37. 51L'l P'v' , .... ~j ~ Pipe: Cj l.l'l !Li. 0 ·-·' I..... 2121,3 PL 18. tLi0 PF !li. Q:1 i:::'.IZI 1 2B. 8 e1. tZt 5121. a 0. 0 ILi. e, 120 FTG PE ~:t. 121 202 28. 8 0. 0 ~50. 8 0. 0 e1. 1Li1L'l0 TL 18. 00 pl.) 0. IL'l Pipe: 91 --0. QI 2.203 PL 1 ~5. IZttZt PF tZt. 121 2e12 28. 8 0. 0 50. 8 l,li. e1 0. 0 121l'i FTG T PE 0. IL'l 30~~ 28. 8 0.0 50.8 0. 0 e1. QIQ)1Li TL ~~5. 0121 P\..' tZI .. 121 SPFH N~<LER SYSTEM HYDf<nULIC •=1N~lL YS IS Pc\ge 11 JOB TITLE: CAHLSBAD HESEAHCH CENTEH -LOT :J:):1+8 CALC # 1f4 ROOF PIPE DATA (cont,d) PIPE TAG G! ( GPM > DIA<IN> LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) Ht,.J ( C) (FT) SUM. NODES <FT> (K) <PSl) <GPM) F. L. /FT <PSI> Pipe: 92 0.0 2 . 2IzI3 PL 210.00 PF iz, .. IZt 3QtA 28.8 0. Qi 50.8 ei. e, Qt. QI 12Q'I FTG T PE 1.2 30 26.0 0.0 52. IL'l 0.tZt 0. t2t012t TL 220.00 PV 0. fZt Pipe: ')3 --121. 0 2. 21li3 PL 3.00 PF 0. QI 203 28.8 0.0 50.8 0. 0 0. 0 120 FTG T PE 12.'l. e1 3121(-) 28.8 0.0 50. 8 0.0 0. lt)0!l) TL 13.00 p~t 0. Q.'I Pipe: <) L► tZI. 121 2.203 PL H."'. i,~0 PF 121. tZI 21211+ 28.8 0.0 '+7. ') 0.0 e1. I{) 120 FTG PE ll,'I. e, 205 28.8 12.). 0 1.'t 7. •=) 0.0 0. ll.'100 TL 16.00 PV 0.0 Pipe: ')5 e,. e1 2.203 PL 16.00 PF ll,'I. Q'I 205 28.8 0.0 L~'7 • ') 0. e, IZt. tZ1 12e, FTG PE 1Z1. IZI 206 28.8 0.0 47.9 0.0 121. iL'100 TL 16. 00 PV 0. IL'I Pipe: 9G 0. t21 2.203 PL 1.00 pi:=· 0. e, 21216 28.8 0.0 '+7. <:j !li. 0 0. Q,i 12Q.'I FTG T PE il'I. 0 24A 28.8 0.0 4 7. ':) 0.0 e1. e,e1e1 TL 11. 12.'llL'I Pl) 0. QI Pipe: 97 0.0 2.203 PL 16. 1Li0 PF Q'I. 0 2fll7 28.8 0. 0 '-1-8 . 6 0.0 tZt. 12.i 120 FTG PE IZI. 121 21Zt8 28.8 0. e1 L~B. 6 Qi. 0 0.000 TL 16 .. ,ZIIZI PV 0. e1 Pipe: 98 ILi. IL• i::'.. 2tt.U PL 16. 1Z1t2t PF 0. IZI 21218 28.8 0.0 L►B. 6 !Li. 121 0. QI 12121 FTG PE ei. e, 209 28.8 0.0 .li,8. b 0. 1ZI 0. 12101,) TL 16. Q.'10 PV IZt. IL'I Pipe: 9g 0.0 2. 202; PL 1.00 PF fl). it:i 21Li'.) 28.8 0.0 48.6 0. 0 It.I. 0 120 FTG T PE llt. Qt 22A 28. 8 0.0 '+8. 6 Q.'I. 0 0. 12It21Q.i TL 11. lli0 PV 0. 0 Pipe: 1eI12I 57. 1 i+. Jl1Z1 PL '+. 51Zt PF e,. w I 1 26.0 121. 0 5 1+. 7 Q.•. e, 1. 3 1212.'I FTG PE Q'.i. !Lt L)-2G. e, ei. Qt 51)-. ·-, I tZ1. Qt 0. e,e11 TL Li,• ~~QI 1:::i v ILi. QI Pipe: 101 11G. Qi 1►• 31 Q'I PL 12. Q.'IQ.'I PF Qi. Q.'I L~ 26.0 0. IZI 54.7 0.0 2.6 120 FTG PE tZl. 11.) f., 2£,. 0 0. 0 54. 7 ll'.l. ll'I !li. 003 TL 12.00 PV e,. 121 Pipe:: 11212 175. 1 L)-. 310 PL 12. !Lilli pr:· 0 .. 1 6 26.0 il'I. 0 ,-.:·L ..J +. 7 0. 121 3.9 12Q.i FTG PE lli. (1 8 26.0 0. e, ~5L► • 6 e,. 12) !l). 0tZt7 TL 12. 0Il'l P'v' ILi • 1 Pipe: 11Li3 23.1'.J-.. ~;;, -'1-. 31 e, PL 1 .-. .::.. llitZI PF Q.i. 2 8 26.tZI 0. e1 5ii-. 6 fl). tZt 5.2 li::'.0 FTG PE 0. 11.,i 10 26. 0 0. 0 5.l~. L1-lli. t2i 121. Q.113 TL 12. IL'l0 Pl,,,I Q.'l. 2 Pipe: 11214 29~~-1ZI L1 ... 310 PL 7.92 PF e, .. ~~ 11.ZI 26.0 0.0 5L~ • L~ ei. e, 6. c::· 12Q.'l FTG PE 0. e1 ..J 12 26.0 0.0 54.3 0. tZt 0.1Ztl9 TL 7 .. 92 PV 0. :~ SPRINt\LEH SYSTEM HYDRAULIC f."-lN{".}L YS l S P~tge 1 .-. a::. JOB TITLE: CAHLSBAD F<ESE~'4RCH CENTEH ··-LOT ~t48 CALC ~u~~ 1100F PIPE DATA (cont' d) PIPE TAG Q(GPl'il) DH~<IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. tJEL (FPS) HvJ ( C) <FT) SUM. NODES <FT> ( K) <PSI) <GPM> F. L. /FT <PSI> Pipe: 1e,5 348. 2 .Y·. 310 PL 12.00 PF 1Zt. 3 12 26. 0 Q.i. 0 5'+. 3 it). 0 7. 7 120 FTG PE 0. 0 14 26.0 0. 0 53.C) 0. 0 12.'l. Q.'126 TL 12. @Zl PV 0. 4 Pipe: 106 399. 8 4. 31121 PL 7. 012.'I PF e,. 2 14 26.0 0. Qt ~~3. 9 0. e1 8. 8 120 FTG PE 0. e, 1 1.r-1 26. 0 121. Q.'i 52;. 7 0. Q.'I Q.i. ,213.14 TL 7. 00 PV e,. ,::-...., Pipe: 107 399 .. 8 L• • 3H.i PL 1:::-,_J. IZ\IZt PF 0. ;;:: 11 • .:~ 26. 0 0. Q.i 53. 7 '1). Q.i 8. 8 12e1 FTG PE t21. 121 16 26. 121 121. tZI 53. C"-' ei. !Li 12,. e,34 TL 5. 1210 PV 12). 5 ,_J Pipe: 108 .l~50. 6 4. 310 PL 1 .-. i::.. 00 PF Q.i. 5 16 26.0 0.0 53. ,:.-tZI. e, ':,. 9 120 FTG PE tZt. 0 ... J 18 26. 0 0. QI 53. Q.'i Q.i. 0 0. Q.11•2 TL 1 -::, L.,. Q.'10 PV 0. 7 Pipe: 109 501. 2 4. 31 e, PL 1 .·-, i::.. 00 PF. 0. 6 18 26. 0 '1). 0 53. 0 0. 0 11.. Q.'l 1212.i FTG PE 0. ll.'l 20 26.0 t2.i. 0 52. L.. e,. e, 12,. 1Z1~52 TL 12. ,210 pl,) IZ\ • 8 Pipe: 110 ' 357. 7 1, .. 311l.'I PL Cj. 5'+ PF e,. 3 2e1 26. tZI 121. IZI 52. 4 0. 0 7 . ·) 120 FTG PE 12,. 121 2f.:~ 26. 0 Q'I. 0 52. 1 0. 0 121. 028 TL 9. 5'+ PV Q.'I. i i, Pipe: 1 1 1 188. c::-Li-• 310 PL 16 .. IZIILi PF !Li .. 1 ,_J 2 2 26. 0 0. e, 52. 1 e,. 0 Li,• 1 12Q) FTG PE 0. It) 24 26. 0 0. 0 ~~2. 0 0. IZI e,. 0tZl8 TL lG. t211Z1 PV 0. 1 Pipe: 112 e,. 0 Lt-• 310 PL 9. Q.i0 PF 0. Q.i 2Lt 26.0 0. 0 52. 0 0. 1Z1 0. It) 120 FTG PE 121. ,~, 3 12) 26. 0 0. 0 52. 0 0. (!) ei. lt)IZ!JL'i TL 9. JLi0 PV Q.'i. 0 Pipe: 113 ·-.. 5 7 . IZI b. L1-1ZI3 P L 1 ·::, 1-. e1e1 PF 0 .. ,z, 3 26. 0 0. tZI t.d. 7 t21. 0 0. 6 121Li FTG PE 0. Q.i i:=-2G.0 0. 0 td. 7 e, .. IZl 0. tZIIZttZI TL 12. t21t21 P\.' e,. ILi ,_J Pipe: 11 l~ --116. 0 6. 1.,.03 PL 12. 00 PF ll'i. 0 1::.-26.0 0. 0 61. 7 0. 121 1. 2 120 FTG PE 0. e, ,_J 7 26. 0 0. 0 61. 7 e,. 0 Q.i. 001 TL i2. 00 PV Q.i. Q:t Pipe: 115 ..... 1 75 .. 1 G . L1,lLi3 PL 12. 00 Pr=-0. ,~1 7 26. 0 0. ei 61. 7 ll,i. tZt 1. ~7 121£1 FTG PE e1. Q. I ·=., 26. 121 121. 0 61. 7 tZt. !Li 0. ,~itZt 1 TL 12. 0121 PV (Li. ,:, , P ipe: 116 ---23'-t. 7 6. LJ,03 PL 12. tLit2.i PF Qi. 121 ':) 26.0 121. 0 Gl. '7 0. tZt ·=· ··~ 1 ~~ILi FTG PE 0. ~~I , 1-. -...> i 1 26. 0 0. Qi 61. 7 !Li. 0 e1. lt'ir2t2 TL 12. 01l'i pi..,1 121 .. Q'i P ipe: 117 .. -2 9 5. Ill G. 403 PL ~). ~::•) PF 1Z1. l 1 1 26. 0 0. 0 61. 7 0. 0 ,::, I,.... g 120 FTG T PE e,. ,Zt 3 1 26. 1£1 0. 0 61. 8 tZI. 0 0. Q)1Z13 TL 35. 29 pi..,1 0. 1 SPHIN~\LER SYSTEM HYDRt4ULIC hNALYSIS Page 13 JOB TITLE: CARLSBr~D RESE~7.\RCH CENTEF< ,._ LOT ~f48 CALC # 1(.) ROOF PIPE DATA (cont 1 d) PlPE TAG G! (GPM) DIA<IN> LEl·-.JGTH PREBS. END ELEV. NOZ. PT DISC. VEL<FPS> HW(C) <FT> SUM. NODES <FT) 00 <PSI> <GPM) F. L. /FT <PSI> Pipe: 118 ·--1 764. 1 6. 403 PL 22. 75 PF 2 .. i:::-..J 31 26. 0 0. 0 61. 8 fl). 0 17. 6 121L'I FTG L PE ll1. 2 TOR 25. 5 0.0 64. 5 0.0 0. 077 TL 31. 75 PV ·:::. '-. 1 Pipe: 119 --1764 .. 1 6. 403 PL 25. 1t.'10 PF~ 1. ':) TOR 25. a:::-121. 0 f."' Lt• r.:: 121. Ill 1 -7 b 120 FTG PE 10 .. a ..J ...J I • BOH 0. i:::· ..J H. C-· n. Tl. 3 100. 0 flt. ll177 TL . -,c· C...J • fll0 PV 2 • 1 Pipe: 12121 -·-186Lt. 1 B. 510 PL 10.00 PF. 0. Lt BOF< 0.5 H. s. 77. 3 101L'I. eJ 1 e,. c::· 140 FTG L PE 1. c::· -..J ..J U5 -3.0 121: 0 79. 1 e,. 0 0. ~)16 TL 21. CJ7 pi...,1 0. 7 Pipe: 121 --186-'t. 1 7. 987 PL 260. !l)0 PF 6. 8 U5 -·-3. 0 0.0 79. 1 0. 0 11. Cj 151Zt FTG 7L PE 2. 2 lJLt ·::, 0 0. Ill B-:;• 8 It). 121 !l). 1211 g TL --c.-i::..-20 p1...,1 1. IL'I '-. ...., . ~..J..J ■ Pipe: 122 FIXED PF<ESSURE LOSS DEVICE U3 ·::• '-. QI 0. 0 88. 8 IL't. e, ,::· ,.__,. e, psi, 186L~. 1 gpm LJLt ·::, L-. 0 0. IZI a··;-..., . 8 0. 0 Pipe: 123 --186Lt. 1 7. 987 PL 1 -::, I-. fl'\Q.'l PF 1. G U3 ,::,, 0 0.0 B8.8 tZ1 . 0 11.. f) 150 FTG Ti:::L PE . ::, 2 "-• '-. U2 -3.0 ll,1. Q.'l 92. 6 0. Q.'t 0. 019 TL 84. 53 P\r' 1. 0 Pipe: 124 ··-186 Lt . 1 7.987 PL i.0. 00 PF. 1. 1 U2 -3.0 0. e, 92. 6 Ill. 121 11. C) 150 FTG TG PE ll'l. ~) Ul ·-... u ■ 0 SRCE 94. 4 (N/A) ilt. '2119 TL 8':). 8 7 PV 1. tZI Pipe: 1 --,£::-i:;.._1 --661L'l . 2 6. Lt03 PL 1 ·::, ._. 1t.10 r:iF 0. 2 29 ~:'.6. 0 0.0 1::..-·-; .. J' • 4 0. tZI 6.6 121Zt FTG PE ti.l .. ,z, 23 26. 0 0. 0 57. 6 0. It) 0. 013 TL 1 ·::, '-. 0121 P\r' 0. ·-.;• ,.__, Pipe: 126 ···-''.)75 .. 4 6. 4tZt3 PL 9. 5-4. PF Ill. 2 23 26. e, ![). 0 ,::-·-, ..JI • 6 It). 121 ',). -7 I 12tt) FTG PE f). tZI 21 26. 0 QI,. QI 57.8 e,. e, il'I . 1Z126 TL 9 . 5.l► PV 1Z1. 6 Pipe: 127 --1262. l) 6. 1-.e,3 PL 1 .-, i::.. lllfll PF it). 5 21 26. 0 0. tZI 57. 8 It). QI 12. 6 120 FTC; PE ILi., 121 19 26 . 0 0. 0 58. --;-,.__, IL'l. QI ,z,. e,11.2 TL 1 -::, I-. ,ZIQI PV 1.. 1 Pipe: 1~::8 ·--1313. 1;::· 6. 4Q.U PL 12.121121 PF Q. 1:::· ....J . .... 1 fj 26. 0 Q.'1. 0 58. 3 121. Qi 13. 1 12Q.'I FTG PE 0. t21 17 26. 0 0. tZI 58. ~ 0. e1 It),. 0 L~ 5 TL 12.00 P'v' 1 -::, • L- Pipe: 129 -1361. •• 3 6. itl.213 PL 1 -::, '-. 00 PF Q'\. 6 17 26.0 0. e, ~3a. '] QI. QI 13. b 12tZI FTG PE 0. IZI 15 26. 0 Q't. QI 59. .L. 121. QI Q.i • 048 TL 1 ·::, '-. 00 PV 1. 2 Pipe: 130 ·--1415. 9 6. LttZl3 PL 12. 1Z11Z1 PF 0. 6 15 26 . 0 ei. 0 59. L• 0. 0 1 L• • 1 120 FTG PE 0. Ill 13 26.0 0. 0 60. 1 0. 121 tZl. 051 TL 1 •::, L-. 00 PV 1. .::, SPRINKLER SYSTEM HYDRAULIC ANALYSIS JOB TITLE: CARLSBAD RESEARCH CENTER -LOT #48 CALC #lA ROOF PIPE DATA (cont'd> PIPE Tt-➔G C!(GPM) DI(-l(IN> LENGTH PRESS. END ELEV. i'JOZ. PT DISC. VEL<FPS) Hl.--J < C) <FT> SUM. NODES <FT) ( K > (PSI) <GPM) F.L./FT (PBI) Pipe: 131 M•" 146 (). IL~ 6. l~IZl3 PL 2.62 Pr=-1. 8 13 26. 0 0. 0 60. 1 ll.1. 0 1 Lj, • 6 120 FTG T PE ft). 0 31 26.0 0.0 61.8 0. e, tZt. 1Zt55 TL 32.62 PV 1. 't NOTES: (1) Calculations were performed by the HASS 5.5.0 computer program under license no. 8926J521 granted by HRS Systems, Inc. 2193 Ranchwood Dr., N.E. Atlanta, GA 30345 (2) The system has been balanced to provide an average imbalance at each node of 0.001 gpm and a maximum imbalance at any node of 0.061 gpm. ( 3) Velocity not used any pipe pressures are printed for in balancing the system. is 31. 1 ft/sec. inf or .. ·mat ion on 1 y, c:.1nd ar .. ·e Maximum water velocity in (4) PIPE FITTINGS TABLE Pipe Table Nam~: STANDARD.PIP Pf.'.:lGE: F MATEF<InL: DYNAFL HWC: 121Z1 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B C 'J A Ell Tee LNGELL CHt<VLV BFYVLV GATVL\) ALMCHK 2 .203 5.00 1 tZ1. IZttZI 3. 01Zt 1 l. 0tZ1 6. 1Z11Z1 1 • 12.,e, 1 tZ1. e,e, 3.314 7.00 15. tL'l0 5.00 16. 0~) 1 e1. 1Z11L1 1. 01l) 13. 1210 4. 31tZ1 10.00 20.00 6. tZ1f) 22. euz, 12.00 '-~. 00 20. 1Z11Z1 6 • .1.~e,3 14. e,0 30. 1Z10 '). 0('1 32 .. IZIILI 10. eie, 3.00 28. '%) D DP'v'LV 10. 1Z11Z1 10. lt)0 1 ILi . Q)QI 19. 0121 SPHINgLEf< SYSTEM HYDF<.:1ULIC ANALYSIS Page 1~i JOB TITLE: CARLSBAD RESEARCH CENTER -LOT #48 CALC #lA ROOF WATER SUPPLY CURVE p R . E i'"""• .::> {.-· .:;> u R E p s I 121Zt*\ \ \ \\ l \\\\\ I I * (-115.0 psi@ 1530 gpm Flow Test Point 11 tZt+ I 1121121+ l 9,Zt+ l aei+ I I 70+ I 6e1+ 50+ 31Zt+ I tZt X I============================== 20+ LEGEND X -Required Water Supply 9 L~ .. 3 [.--. p s i @ 2 2 E.A. 1 g pm 10+ I 0 = Available Water Supply I 109.68 psi@ 2264. 1 gpm II II II 0 ·t-·1-··-·i--····· ···I -·-..... ···--·I · ... -··--·-..... ····· -i· ---· ·•• ... _ ···· ···• ··I·--······-····-.................... -1-··-..... ···• ·-.. ···--·---..... +· ........ ····· .............. ··-·-·· .... ·i--·-··-..... --· ··--·-... _ .................... I .. 8001200 1600 2000 2400 2800 3200 3600 4000 F'LOW <UPM) ACTION FIRE SYSTEMS. '~ 185 HAf~NESS ST. SPRING VALLEY, CA. 91977-3948 11 Ct-➔LCUL.=~--I DI H2 11 HYDHt4UL IC cr-1LCULhT IONS FOF< CHC LDT #-'+8 CAHLSBAD, U4 .. FILE NUMBER: 98-762 7 -··':, ·-9 8 OCCUPANCY CLASSIFICATIOt: l>El\fSI TY~ AREA OF APPLICATION: COVERAGE PER SPRINKLER: NUMBER OF SPRINKLERS CALCULATED: TOTAL SPRINKLER WATER FLOW REQUIRED: FUTURE T. I. AT MEZZANINE • 21t.1 gpm/ sq. ft. 1 ~:jQl0 sq. ft. 1B"X i8, MAXIMUM 9 sprinklers 662.5 gpm TOTAL WATER REQUIRED (including hose): 912.5 gpm FLOW AND PRESSURE (@ BOR): 912.5 gpm@ 73.7 psi SPRINKLER ORIFICE SIZE: 5/8 l·.Jhl"IE O :· CONTFh'.:.)CTOF<: CO ~NERSTDNE CONE:iTRUCT ION DESIGN/LAYOUT BY: BRIAN WEIT inch •4UTHOR I TY ~-AV I NG J"UR 13D l CT I ON: Cf~-lF<LE>b►4D Fl HE DEPT. COHTHACTOR CERTIFICHTION l\JUMBEf<: c .. -·16 3881GiZ1 CALCULATIONS BY HASS COMPUTER PROGRAM <LICENSE# 8926J521 HRS SYST~MS, INC. nTU)I\ITA, Gr.-1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 Date: 11/1211/i..)1 C:: \ 7t\2· .. ··2 JOB TITLE: CARLSBAD RESEARCH CENTER -LOT #48 CALC #2 ROOF WATER SUPPLY DATA SOURCE NODE TnG Ul SHHIC RES ID. FLOt,.J PRESS. PRESS. @ <PSI> <PSI> <GPM) 1~::0 .. tZI 115. IZI 153ii.,. 0 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE A"'A IL. TOTAL PF<ESS. t]I DEMAl,m <PSI) (GPM) 117.0 llC.2.5 412.~ REG!" D PHEBS. <PSI) <.1 ·::, ·:::, '-''--• .... ~\'l.-~ 1162.5 GPM TOTA L HOSE STREAM ALLOWANCE AT SOURCE OTHER HOSE STREAM ALLOWANCES ll:$0 400.~ GPM ltZIIZl.0 GPM 662.5 GPM TOT(.~L DI SCHAHGE Ff<OM ~)CT I VE SPRI Nl·{LERS NODE ANALYSIS DATA NODE TAG 11211 102 11213 1 t21.£~ 11215 106 107 108 11211·) 1 1121 1 1 1 112 1 i3 114 1 i5 llb 1i7 118 1 i Cj 12121 121 122 123 12L~ 125 126 127 128 .12•=) 130 131 132 133 13L~ ELEV..HION <FT> 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.B 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 28.8 NODE TYPE PF•!ESSUF~E <PSI) 57.7 57.8 58.0 58. 1 58.2 58. L1, 5B.5 ~58. 6 ~S8. 8 57.7 57.8 57.9 58. 1 57.5 57 .6 57.8 57 . () :_;s. 1 58.2 58 • .l~ 58.5 58.7 57.7 57.9 58. 121 58.2 58.5 58.6 DISCHARGE (GPM) SPRINt<LER SYSTEM HYDRt=lUL 1 C hN{.'.\LYSI S JOB TITLE: CARLSBAD RESEARCH CENTER -LOT #48 CALC #2 ROOF JDE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE 151 152 153 154 155 156 15",7 158 159 160 i6i 162 163 1 (...l1- 165 166 167 168 16C) 17121 171 172 173 17'-t- 175 176 1 ·17 178 171.) 181Zt 181 182 183 18Lt- i::~01 21212 2Iz,3 21ZlL)- 21L15 206 2e,7 208 2,z,9 1 2 3 4 i:: ..J 6 7 8 9 1121 1 1 <FT> <PSI) <GPM> 28. 8 28. 8 28. 8 28. 8 28. 8 28. 8 28. 8 28. 8 28. 8 28. 8 28. 8 28. 8 28. 8 28. a 28. 8 28. 8 28. 8 28. 8 28. 8 28. 8 28. 8 28. 8 28. 8 28. 8 28. 8 28. 8 28. B 28. 8 28. 8 28. 8 28. 8 28. 8 28. 8 28. 8 28. 8 28. 8 28. 8 28. 8 28. 8 28. 8 28. 8 28. B 28. 8 26. 0 26. 121 26. ei 26. ll'i 26. It) 26. 0 26. Qt 26. tZl 26. 0 26. ,ZI 26. IZl t<= 11. 5Q.'I 1-<;:;:;1 L 50 t.i:,= 11. 5e1 IJ~::::: 11. 50 t<= 11. 5121 I{= 11. 5121 t{::::: 11. 5121 I·(= 11. 5V..) t(=11. 5t2t 58.7 58.8 58.9 5<:). IL\ 59. 1 5 '). 2 59.3 ~:jl.). 4 59.5 58.7 5£1.9 59. e, 59. 1 59.2 ~59 • L► 59.5 59.6 59.8 ~36 . 7 57.0 57.2 57. :5 57.8 58. 1 ---- 58.4 58. 6 ---- 58.0 t.i8. 2 58. L1- 58. 6 58.8 59 .0 59.2 31.. 9 32.9 Li.Li-. 4 -'► 11, • LJ- -'l-5. 1 57.5 61.8 56. <:) Gl.8 Gl. 8 t.i6 . 8 65.C) 7G .6 Tl . 2 P➔• 3 76.7 Tl . 2 79 .3 6 1 • ') ..... ·--·-· Page 2 SPRHH<LEF< SYSTEM HYDRAULIC f--lNt'.".\LYSIS JOB TITLE: CAF<LSBAD HESEARCH CENTER ···· LOT 41A8 CALC *~2 ROOF ODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE 1 .-, C 13 11► 14t1 15 16 17 18 19 20 21 22 23 24 ,••-,i;::-C...J 26 27 28 29 30 31Zlf.:l 31 ·TOH BOR U5 U4 U3 U2 Ul <FT> <PSI) <GPM> 26.0 26. 12.~ 26.0 26.0 26.0 26.0 26.0 26.0 26.0 26.0 26. t2t 26.121 28.B 26. 121 26. ll~ 28.8 26 .0 26.0 26 . e, 26.0 26. Q.1 26.0 28.8 26.0 .-,r.:-,:.-C..J a ..J 0.5 --3. 0 2.0 2. t2l ·--3. ILi HOSE STREAM SOUF<CE 56.6 61.8 5("• L;. 61. 7 56. 1 61. 7 55.6 61.6 55. 1 61. 6 54.6 51.2 61.6 51.2 53.9 5-4 .• 8 t.i':). 8 61.2 61.6 !:A. 1 33.3 61.9 62.6 73.7 75.3 74.4 7c3 • i► 81.9 82.2 762.5 Page 3 SPHI Nt<LEF< SYSTEM HYDF<AUL 1 C r-1N{1LYSI S JOB TITLE: CARLSBAD RESEARCH CENTER -LOT #48 CALC #2 ROOF PlPE DhTA PIPE T.:lG END ELEV. NOZ. NODES <FT> (K) 1 2 2 101 Pipe: 1 26.0 26.0 Pipe: 2 26.0 28.8 Pipe: 3 112'1 28. 8 102 28.8 Pipe: 4 102 28.8 103 28.8 Pipe: 5 103 28.8 ltZt4 28.8 Pipe: 6 10-4 28. 8 105 28.8 Pipe: 7 11215 28. 8 106 28.8 Pipe: 8 10G 28.8 H:'17 28. 8 Pipe: 9 11Zt7 28. 8 1e1a 2a.a Pipe: 10 11218 28. 8 1 lll'J 28. 8 Pipe: 11 H'.19 28. 8 3 26.0 Lt 110 Pipe: 12 26. !Ll 28.8 Pipe: 13 11e, 28.8 111 28.8 e,. 121 0. 121 0. 121 0.0 1l1. Q) Q.'I. 0 QCGPM> DIACIN> LENGTH PRESS. PT DISC. VEL <FPS) Hli-J <C> <FT> SUM. (PSI) (PSI> (GPM) F .L./FT 56.9 57.5 57.5 57.7 57 .7 57.8 57.8 58. IZt 58. ll'I ~.38. 1 58.1 58.2 58.2 ~58. 4 58.4 58.5 58.6 58.6 58.8 58.8 61.8 56. ':) 57.5 57.5 57.7 i;:,. e, 121. e, --L•7. 2 -4-. 0 c. 21213 PL 121l.1 FTG t21. 017 TL 2.203 PL 120 FTG Q.i. 017 TL 20.33 T2L -..... ... ..., -, ~b ... !I~ 70.00 T 80.00 PF PE PV PF PE Pt...' -47.2 c.203 PL 8.00 PF 0.0 4.0 120 FTG PE 0. tZI tZI. 0 1 7 TL 8. Q11Z1 P V 0. 0 L•• QI e,. 0 --Lt 7 . 2 t;:'I. 0 J'.~. 0 e,. 0 0.0 4.QI 0.0 ··-47. 2 0. 0 L1,. Ill ei. e, ---LO . 2 0.0 Lt.lZI IL'I. QI -···47. 2 QI. QI L~. 0 0. lL.l 12.i. 0 Li-. e, t;:'I. QI -···'-• 7 . ~::: e1 . e, ~➔-. 1t.1 0. e, 8. IL'l0 PF 120 FTG PE 0.017 TL 8.00 PV 2.203 PL 8.00 PF 12e1 FTG PE 0. t211 7 TL 8. 00 PV 2.203 PL 8.00 PF 120 FTG PE 0.017 TL B.00 PV 2.203 PL 8.00 PF 120 FTG PE 0.017 TL 8.00 PV 2 .. 203 PL 8.00 PF 120 FTG PE 0.017 TL 8.00 PV ~.203 PL 8.00 PF 120 FTG ----PE 0.017 TL 8.00 PV 2.203 PL 8.00 PF 120 FTG PE 0.017 TL 8.00 PV 2.203 PL 87.00 PF 120 FTG 2T PE 0.017 TL 107.00 PV ---L~B . a 2. 203 PL ai;:1. e1e1 PF 4. 1 1C0 FTG 2T PE 0.018 TL 100.00 PV -48.8 2.203 PL 8.00 PF 0.0 4. 1 120 FTG PE 0.0 0.018 TL 8.00 PV IZt. 6 !L'I. 0 121. 1 1.-'► 1.2 Q). 1 0. 1 0. 121 0. 1 0. 1 0. Qt 0. 1 0. 1 Q'l. 121 0. 1 IZl. 1 Qt. IZt IL'I. 1 0. 1 Q.'I. 0 0. 1 ll'l. 1 0 .. ti.. 0. 1 Qt., 1 121. e1 121 .. 1 Q'I. 1 0. Ill 121. 1 LB 1.2 0 • .l 1.8 1Z1. 1 ll'I. Q'I 0. 1 SPRINKLER SYSTEM HYDR•=tULIC ANhLYSIS Pcige c::· ._I I JOB TITLE: CAF<LSBAD HESEAHCH CENTEH ·--LOT :):l:Lt-8 Cf.)LC *~2 1100F PIPE DATA <cont' d) PIPE T~lG Q(GPM> DIA<IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL<FPS) HW(C) (FT) SUM. NODES <FT) ( K) <PSI) <GPM) F. L. /FT <PSI) Pipe: 1.1.~ -·-48. 8 .::: . 21Zt3 PL 8. 121121 pr:-Q) • 1 1 1 1 28.8 0.121 57. 7 0. 0 4. 1 12121 FTG PE 121. e, 112 28. 8 0. Qt 57.8 tZ1. QI 0. tZt 18 TL 8. e11zi PV 0. 1 Pipe: 15 --Li-8. 8 .:::: . 21213 PL B. !lifl'\ PF 0. 1 112 28.8 0. 0 57. 8 e,. e, l1, • 1 120 FTG PE 0. IZI 1 i 3 28. 8 lli. Ill 57. Cj e,. e1 ll'i. ll'l18 TL 8. 00 pl.) e1. 1 Pipe: 16 --48. 8 · ... • L-. 203 PL 8.00 PF 0. l 113 28. 8 0. 0 57. 9 it). 0 .L~. 1 12e1 FTG PE '2.1. e, 114 28.8 0.0 58. 1 0. QI tZl.018 TL 8. 00 Pl..' 0. 1 Pipe: 17 --Li-8. 8 ·::, 203 PL 8. t;:)Q'i PF 0. 1 ...... 114 28.8 0.121 58. 1 0. 121. l~ • 1 120 FTG PE 0. tZl 115 28. 8 lli.'0 58. 2 t;:). 0 (.I\. ttH8 TL 8. 01li r:iv t21. 1 Pipe: 18 --L~B . 8 2.203 PL 8.00 PF 0. 1 115 28. 8 ll,. e, 58. 2 ll,i. !i.i Lr• i 12121 FTG PE !l'l. 0 116 28. 8 0. 0 58. 4 0. tZt tZt. Qll8 TL 8. lli0 PV tZI. l Pipe: 19 -·-48. 8 4 ... , ...... 21213 PL 8. IZl!i.'l PF 0. 1 116 28.8 ei. 12) 58. 4 Q1. IZl 4. 1 120 FTG PE t21. 1Z1 i17 28. 8 t2.'l. 0 58. 5 Q). 0 0. '1.118 TL 8. tZl!t.i PV e,. 1 Pipe~ 20 -·-48. 8 2. 2tZt3 PL 8.00 PF ,~,. 1 117 28. 8 lli. ll1 58. c:· ..J ll1. 121 Lt• 1 12Q) FTG PE 0. 121 118 28. 8 e,. e, 58. 7 e,. e1 e1. e11a TL 8.00 PV 0. 1 Pipe: 21 --Lt-8 . 8 ·::, L-. 203 PL 87. IL'lll'l PF ._, ..... . ll'I 118 28.8 0. tZI 58. 7 0. 0 4-. 1 120 FTG 2T PE 1. 2 5 26. e, IZI. 0 61. B ll'I. 0 ll,1. Q'I18 TL 11217. eie1 PV '2.i. 1 - Pipe: 22 ·--48. 9 2. 2Q)3 PL 80. euzi PF 1. B 6 26. 0 0. QI 56. 9 ei. 0 4. 1 121li FTG 2T PE 1. 2 119 28. 8 e,. tZl 57. 1::-0. IZt 0.Q118 TL 100. tZ11Z1 PV 0. :l ._J Pipe:: 23 -•-1•8. ':) 2. i.:~1213 PL 8. lli0 PF 0. 1 119 28.8 0. 0 57. 1::: e,. Q1 4. 1 120 FTG PE 0. tZ1 ..J 12tt) 28. 8 0. ,ZI t:,i7. 6 QI. e1 li.'l. IZl 18 TL 8. 1Li0 PV e,. 1 Pipe: 24 --Lt8. -=:; · .... • I-. 2e,3 PL 8.00 PF e,. 1 12121 28. 8 QI. Q.1 57. 6 Ii). e, 1.t. 1 12Q'i FTG PE !i.i. IZi 121 28.8 0. 0 57. 8 e,. e, 0. 018 TL 8.00 Pl.,I 12). 1 Pipe: .···,c:· --L►B. Cj ·=· 203 PL 8. IZIIZI PF Ill. 1 C...J ...... 121 28.8 0. 0 1:::--7 ._JI• 8 0. Qt Lt• 1 1 i::'.ll.1 FTG PE 0. IZt 122 28. 8 0. 0 57. 9 tZt. 0 li.'l. 018 TL 8. 00 P'J 0. 1 Pipe: 26 ···-L1-8. ') 2. 2tlt~3 PL 8. Q,e1 Pr=-e,. l 122 28. 8 0. Q.'l ,::-1 ...JI • Cj !i.1. 0 .L1-. 1 121l1 FTG PE ~) . 0 1 ·:.:. -;;. 1--..> 28. 8 0. tZI 58. 1 tZI. IL'I e,.e11B TL 8. IZttZI PV Q1. l SPi·<I Nt<LER SYSTEM HYDH{~ULIC ANf:lLYSIS Page 6 JOB TITLE: CAHLSBAD RESEARCH CENTEF< -··· LOT ~f48 Ci:'.:\LC :l=f2 ROOF PIPE DATA (cont,, d) PIPE TAG G! <GPM) DIA<IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL<FPS) Hl--J < C > (FT) SUM. NODES <FT> <K> <PSI> <GPM> F .. -. L. /FT <PSI) Pipe: 27 -48. ~ -::, .._. 21213 PL a. 00 PF 0 • 1 123 28. 8 ~.i. Ill 58. 1 Q.i. e1 Lt• 1 120 FTG PE 0. ll.1 124 28. B 0.,e, 58. ,::, .._ 0. IL'. IL,. 12118 TL 8. 0121 PV e,. l Pipe: 28 -·1t8. I.) ·::, ...... 21213 PL 8. 00 1:)F 0. 1 124 28. 8 0. 0 58. .-. 0. Ii) 4. 1 121ZI FTG PE 0. IZI ..::. 125 28. 8 0. ll'l 58. it ei. e, 0. 018 TL 8. 00 PV 0. 1 Pipe: 2'=) ·--48. •=) .-, 2iz13 PL 8. 0121 PF Ill. 1 ..::. . 125 28. 8 Q.'l. 0 58. Lt 0. e, L1, • 1 12~) FTG PE 0. e1 126 28. 8 0. 0 58. i:::-..J 0. tZI 0. 018 TL 8. tZIIZI PV 0. 1 Pipe: 30 --48. (j .. ::, i.::'.'213 PL 8. 0e, PF 0 • 1 I.-. 126 28. 8 0. e, t58. 1::.-..J 0. 0 '+ • 1 l 21L) FTG PE 0. 0 127 28. 8 0. e, 58. 7 0. ,ZI 0. lt.118 TL 8. Q.'10 PV 0. 1 Pipe: 31 .... 4a. (':) 2. 203 PL 87. 00 PF 2. 1Z1 127 28. B e,. tZI 58. 7 0. 0 Ji .• 1 12121 FTG 2T PE 1. 2 7 26. 0 tZI. 0 61. 8 e1. 0 0. 12118 TL l tZ17. 00 PV ,:1. 1 Pipe: 32 --LtC) • 3 2. 203 PL 96. 01£1 PF ·::, ...... 2 8 26.0 e,. 121 :-;6. 8 0. 121 4. 2 12121 1-'fG 2T PE 1. 2 128 28. 8 0. 0 57. 7 "). e, e,. 12119 TL 116. 00 PV e1. 1 Pipe: _ ... _ ....... ···-4'). h" 2. 203 PL 8. tZIIZI PF 0. l ~~ , ~ 128 28. 8 e,. 0 C;:--; 7 ill. 121 Lt• -:::• 12Q.i FTG PE 0. f.'l ...JI • I- 129 28. B 0. e, 57. 9 e,. 0 IL1. IZt 19 TL B. e,121 pl.,' 121. 1 Pipe: 34 ---49. 3 -:;., ...... 2'23 PL 8. Q.'10 PF 0. 1 i29 28. 8 0. 0 i:::··..., ..JI• -=) e,. 121 Lt• 2 L:::0 FTG PE !Ll. tZt 13121 28. 8 lli. 0 58. e, 121. flt IL•. Qi19 TL 8. Q.10 p I Q.1 . 1 Pipe: 3~S .... 4 (:). 3 i::. 2IL13 PL 8. Q1Q1 PF 0. i 1312'.I 28. 8 0. e, 58. e, 0. 0 L; • 2 121l) FTG PE 12. 0 131 2B. 8 ei. 121 58. 2 12,. Qt 121 • QI 1 (j TL (). 01l) PV e,. 1 Pipe: 36 -L;<) • 3 i:.:.:. 21212; PL 8. Q),ZI PF e. 1 131 28. 8 0. 0 58. 2 0. 0 4. 2 121Zt FTG PE 0. ,~1 132 28. 8 Ill. 0 58. 3 e,. 0 12.'l. ('119 TL 8. 00 i:::i v 0. 1 Pi pe: 37 ··•-i.;Cj. .· -... , 203 PL 8. 0f'l PF-h 0. 1 ,.., 1-.. 132 28. 8 Qi. 0 58. 3 0 . 0 1.;. 2 121L'l FTG PE il'i. 0 133 28. 8 0. 0 58. 1:::-... J 121. IL,1 IL\. 12.i 1 'j TL 8. IZIIZI PV Ill. 1 Pipe: 38 ·-A9. 3 -::, 2iz13 PL 8. 0e, PF t21 . 1 I.-. 133 28. 8 0. 121 58. i::· e,. 0 4 • 2 120 FTG PE 0 .. 1Z1 ..J 13J'.; 28. 8 0. lli 58. 6 Q.'I. e,, 0. tt.i19 TL 8. e,ei P\J Qi. 1 , Pipe: 3'3 ·-.. 1.,.9 . 3 2. 203 PL 87. 00 PF ·::• I-. Ill 131+ 28. B e,. 0 58. 6 0. 12.'I L; • 2 12e, FTG 2T PE 1. 2 Cj 26. e, e,. e, (.-d . 9 121. 0 ei. ei 19 TL 107. 1210 pl,) e,. 1 SPRINKLEF< SYSTEM HYDR(~\UL 1 C ~lNALYSIS Page -7 I JOB TITLE: CAHLSBAD HESE~~f<CH CENTEH ·--LOT #48 CALC #i:.~ HOOF PIPE DATA (cont' d) PIPE TAG G! <GPM) Dih(lN) LEl"\lGTH PRESS. END ELEV. NOZ. PT DISC. 'VEL <FPS) Hli-J (C) <FT) SUM. NODES <FT) 00 (PSI) <GPM> F. L. /F·r (PSI) Pipe: .£1-0 ···-50 • QI ·::, I-.. 203 PL 231. 0121 PF ,:::-,_J. 2 1 IZI 26. 0 0. y:, 56. 7 0. 0 4. 2 120 FTG L► T PE 12.'l. 0 11 26.0 0. 0 61. 9 0. 0 e,. Q11 <-) TL 271. 00 PV 0. 1 Pipe: Ld --50. Q) -::, I-.. 212.13 PL 231. 00 PF i:::-,_J. 2 12 26. t21 0. 0 56. 6 0. 0 Lt,• 2 12e, FTG '+ T PE 0. e, i3 26. 0 0. 0 61. B 0. e, 0. 12.'119 TL 271. 0Q.'l PV 0. 1 Pipe: 42 ·--50. 9 2. 203 PL 231. 00 PF i:::-,_J. '+ 14 26. flt 0. Qt i::;-r ...Jt.\. 4 0. 0 -'I-. 3 1212.i FTG 4T PE flt. 12.1 15 26. 0 0. 0 61. 7 t21. 1Z1 e1. Qt20 TL 271. 121121 PV tZt. .l Pipe: L•3 -·-52. 3 ·::, 203 PL 231. '1.10 PF i:::· 6 L-. ,_I• 16 26. 12' 0. t21 56. 1 0. 0 4. 4 120 FTG L1-T PE 0. 0 17 26. 0 12.i. 0 61. 7 flt. 0 0. e121 TL 271. Q.'l0 ~: V e,. 1 Pipe: 44 ·--54. 2 ,::, L-. 203 PL 231. 1210 PF €.,. QI 18 26. 0 It). 0 55. 6 0. 0 L~ • 6 120 FTG L1-T PE 0. e1 1 ':) 26. 0 0. 0 61. 6 0. 0 0. e,22 TL 271. 00 P\.' IZt. Pipe: 45 -·-56. i:::· ,_J · ..... , L-. 203 PL 152. --. ~ ~.;:, PF L~ • 1 20 26. ILl Qt. tZI i:::-i::.· 1 ei. 121 4. 8 120 FTG 2T PE 1. 2 ,.J,.J. i78 28. B 0. 0 58. 12.'I fl). t21 e,. Q.'12L► TL 172. 33 PV 0. 2 Pipe: L~6 ··-56. t::· ~~. 21213 PL 8. tZttZt PF IZl. i::'. ,..> 178 28. 8 0. 0 58. e1 e1. IL'l 4. 8 12121 FTG PE 0. 0 179 28. 8 0. 0 58. 2 0. 0 12.i. 0~::4 TL 8. e,e, PV e,. 2 Pipe: 47 --56. i:·" .-, 203 PL 8. e,ei PF 0. 2 .::.i C.. 17,:-J 28. 8 0. e1 58. 2 tZI. Q) 4. 8 12e, FTG PE 0. e, i81ZI 28. 8 0. 0 58. 1► 0. 12.i e1. 12124 TL 8. 12112.'l P\.' 12.'l. 2 Pipe: '+8 .. --t5G. 5 -:-:, 2,2.u PL 8. 00 PF" ea • 2 1.-a 18121 28. B e1. 0 58. Lj, 0. fl) J.'. . 8 120 FTG PE 12.'i. Qi 1 fi 1 28. 8 ei. e, 58. 6 QI. e, tZt. ll.'124 TL 8. 01Z1 PV 0. 2 Pipe:: 11-9 --56. i:::· ·::, 203 PL 8. 12)0 PF' e,. 2 ,.J a..... 181 28. 8 ei. 0 58. 6 tZt. e1 .l,. • 8 1212l FTG PE 0. li.'.t 182 28. 8 Q.'l. 0 58. 8 Ii). ea 12.i. 12121. TL a. 121121 p, .. 1 0 . 2 Pipe: 50 ..... ,. 5 2 . 21Zt3 PL 8. e1,z, PF ei. ·::, ... -;::, t_'\ .. ·-182 28. 8 12.1. Q.1 58. 8 IL•. e, 4. 8 12121 FTG PE It). Q'.l 182' 28. B ei. tZI 5":). QI 0. 0 0. 024 TL 8. 00 Pl) tZt. 2 Pipe: 51 C" r -._jt:,. 5 ·::• I-.. f:Q13 PL 8. 12.itZl PF e,. 2 183 28. a tZl.tZI 5'). 0 tZt. 0. 4. 8 120 FTG PE e1. 121 18J'.j, 28. B 0. '121 59. 2 0. tZI fli. 1212-'• TL 8. 00 PV 121. 2 Pipe: 52 --56. ,::..-·.,_t 2e,3 PL 3tZt. 67 PF 1. ~::: ,_J I-.. 184 28. 8 0. 0 59. 2 0. 0 4. 8 12121 FTG 2T PE 1. 2 21 26. 0 12.i. 0 61. 6 tZI. Q) Ill. 024 TL 50. 67 PV 0. ·::, I-. SPRI N~<LEH SYSTEM HYDF<AUL IC •=lNf°4L YSl S JOB TITLE: CARLSBAD RESEARCH CENTER -LOT #48 CALC #2 ROOF PIPE DATA (cont'd) PIPE TAG END ELEV. NOZ. NODES <FT) CK) Pipe: 53 22 26.0 22A 28.8 pipe: 5lt 22,'.:\ 2a. a 169 28.8 Pipe: 55 169 28.8 170 28.8 Pipe: 56 17'tl.. 2H. 8 1 7 1 28.8 Pipe: 57 171 28.8 172 28.8 Pipe: 58 172 28.8 173 28.8 Pipe: 59 173 28.8 174 28.8 Pipe: 60 174 28.8 175 28.8 Pipe: f:\1 17 5 28.8 17 6 28.8 i76 177 177 23 24 21.,::i 24A 25 Pipe: b2 28.8 28.8 Pipe: G3 28.8 26.0 Pipe:: 61• 26.0 28.8 Pipe: 65 28.8 26.0 0.0 0.0 QCGPM> DIA<IN> LENGTH PRESS. PT DISC. VEL <FPS> Ht.,.J <C) (FT) SUM. <PSI> <PSI) (GPM) r:·. L. /FT 54.6 51.2 51.2 ~;6. Lt- 56.7 56.7 57. QI 57. QI ~-S7. 2 57.2 57.5 57.5 57.8 ~l.B ~58. l 58. 1 58.4 58.4 58.b 58.6 61.6 51.2 51. 2 ~:~3. ':) 164.0 2.203 PL i::::.83 PF 0.0 13.B 120 FTG T PE 0.0 0.172 TL 12.83 PV -69.2 ~.203 PL 139. 17 PF 0.0, 5.8 120 FTG T PE 0.0 0.035 TL 149. 17 PV --69. 2 i::::. 203 PL 8. 1Z10 PF 0.0 5.8 120 FTG PE 0.0 0.035 TL 8.00 PV -69.2 2.203 PL 8.00 PF 0.0 5.8 120 FTG PE 0.0 0.035 TL 8.00 PV -69.2 ~.203 PL 8.00 PF 0.0 5.8 120 FTG PE 0.035 TL -69.2 ~.203 PL 8.00 PF 0.0 5.8 120 FTG PE 0.0 0.035 TL 8.00 PV -E9.2 ~.203 PL 8.00 PF 0.0 5.8 120 FTG PE 0.0 0.035 TL 8.00 PV -69.2 2.203 PL 8.00 PF 0.0 5.8 120 FTG PE 0.0 e.035 TL 8.00 PV ···-G '). 2 i:::'.. 21213 PL 8. t210 PF 0.0 5.8 120 FTG PE 0.0 0.035 TL 8.00 PV -···6 (). 2 121. 0 5. 8 e. e1 ---6 ·:1. 2 0. QI 5. 8 0.0 1 L~ 7 • C) ~).Ii) 12.5 It). 121 --·85. i::~ 12'.l. e, 7. 2 0. 121· 2. ~~IZ(~ PL 121Zt FTG 0.035 TL. 2. 2tZl3 PL 12ii) f-~r G IL\. Q135 TL 12fL) FTG e1. 142 TL 2. 21213 PL 12('.) FTG 0. 1Z151 TL a. 121121 312). 6 7 2T 50.67 2.83 T 12.83 2121. Q\IZI T 31Zt. 00 PF PE PV PF PE P'v' 2.2 1 .-. • a:;. 1.3 5.2 0. 1Z1 1t.i. 2 tZt. 3 0. tL'I 0.2 0. tZt Ill. 2 12). 3 0. 0 0.2 0. 3 0. 121 Ill. 0 0.2 0.3 0.3 121. 0 0. i:::'. 121. 2,; 0. IL'.t Ill. 2 1.8 1.2 0.2 1.8 1. 2 1.0 1.5 1.2 121 • ..::, SPRINt<LEF< SYSTEM HYDF<f.'.tUL 1 C ~:1Nt'.=lL YB IS Page 9 , JOB TITLE: U~HLSBf.:m HESEf4RCH CENTEl1 ..... LOT ~t48 C(.:".\LC ~*2 HOOF PI ·:.E Df4T(4 (cont, d) PIPE TAG G! (GPM> DIA<IN> LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL<FPS) HW<C> <FT> SUM. NODES <FT> ( K) (PSI) (GPM> F~ L. /FT <PSI) Pipe: 66 ·-··51. '+ ~ ... • '-. 21Zt3 PL 2Lt-. 50 PF 121. <3 25 26. QI 0. Q1 53. Cj 0. 0 Lt-• 3 121l'l FTG 2T PE e,. Q.'l 26 26. 0 e,. Ill 54.8 e,. 121 e,. 020 TL 44. 50 PV 0. 1 Pipe: 67 -·-85. ·-·' ·::a 21213 PL 87. fl1e, PF ~= e, ..... L-• ...J. 26 26. 0 0. 0 54. B Qt. 0 7 . ~·-, 120 FTG T PE It). Qt .:::. 27 2(,. ll'l 0. 0 59. B 0. 0 0. Q.'l:=,i 1 TL 97. 00 PV ei. 3 Pipe: 68 ···-Lt-5 . i;~~ 2. 203 PL 7. 00 PF 0. 2 ,_J 27 26. 0 0. 0 59. B 0. 0 3. 8 121L'l FTG L PE 1. ·::, ..... 1612) 28. 8 0. e, 58. 7 e,. 0 0. 01G TL 10. e,e, PV 1Z1. l Pipe:: 69 -Lt-5. 5 ·::, ...... 203 PL 8. 0/l'l PF Q.'l. 1 1&0 28. 8 0. 0 58. 7 e,. e1 --.. 8 120 FTG PE e,. Ill ..., . l(·d 28. 8 ~.'l. Q1 58. 9 0. 0 tl.'l. e,1£. TL 8. 0121 PV 0. 1 , Pipe: 70 --lt-5,. i:::· -::, 203 PL 8. e,121 PF e,. :l ,_J ...... 161 28. 8 0. IL'l 58. 9 0. it) 3. 8 12e1 FTG PE e,. QI 162 28. B e,. Q.'l 59. 0 e,. Qi 0. 12116 TL 8. e112t PV 0. i Pipe: 71 -i.t-~5 . 5 ·::, ...... 203 PL 8. tt.'HZI PF e,. 1 62 28. 8 0. e, 5'3. 0 e,. it.l -;--..J. B 12Q'I FTG PE 0. 1Z1 163 28. 8 0. tL1 59. 1 0. e, 0. e116 TL 8. Q.'10 P\.-1 0. 1 Pipe: 72 --Li-5. i:~· ·::, 21213 FL B. eiei PF. e,. .l ...J ,_. i63 28. B IL'\. tL1 59 . 1 IZla 121 -:.;, ....,., b 12~) FTG PE e,. 0 164 28. 8 0. 0 59. 2 e,. e, e,. tZt 16 TL 8. 12)0 PV Ill. 1 Pipe: 73 --45 • i::.-..J ·::, ._. 2!ll3 PL B. 1t.11Zt PF It). 1 l 6L1-28. 8 e,. 0 5<:). 2 e,. ILl 3. 8 120 FTG PE e1. 121 165 28. 8 0. 0 59 . L► e,. ll,i Q.i. e116 TL 8. IZl!t.i PV tt.'l. 1 Pipe: 7Li-·-··1t5. 1:::-2 . 2,z,3 PL 8. 1t.'11Zt PF ~~-1 ._J 165 28. 8 0. IZt ti'-). L► It). e, ·-;• ._,. 8 12QI FTG PE !l'l. 12.'l 1G6 28 .. 8 e,. e, 5<). 1:::-e,. IZI e,. e, 16 TL 8. 00 PV e,. 1 ._J Pipe: ~-,i:-.:· Ir,••• r::-·-· 21213 PL 8. e10 PF. 12.'l. 1 I ...J -.l+:::J. ...) a..... 166 28. 8 0~ 121 59. L-::-0. e1 -, 8 120 FTG PE 0. tl1 ,_J -..J11 167 28. 8 0. 0 59 . 6 0. it,'t Q. e116 TL 8. e1e1 PV 0. 1 Pipe: 76 --45. i:::-·::. 21i)3 PL 8. 1LitZl PF It). 1 ,_J ...... 167 28. 8 ll.'l. 0 59. 6 ii). 0 2:;. 8 12/l'I FTG PE Q,i. e1 168 28. 8 e, .. 0 59. 8 e,. ~~I tZt. 016 TL 8. tZ1Qt PV e,. 1 Pipe: _'/_., .... 1.._5 _ 5 a:;:. 21213 PL i:::-5'1.'l PF Q). ·=· I I ...J. ..... 168 28. 8 tZl. 0 59. 8 e,. ~) ·-~-8 1 i::'.IZI FTG T PE 1.. ~~ -..Ja 28 26. 0 e, .. "-' f.1. 2 it.'l. tZI e,. e116 TL 15. 50 PV 0 . 1 Pipe: 78 -·-85. -· 3. 31 .{.~ PL 25. 17 pi::--IZt. 1.~ i::: 28 26. e, 1[.'l. 0 61. 2 0. e, ~:.;--..J. 2 12ii) FTG 2T PE Q,'l. 0 29 26 . fl' 0. QI 61. 6 ei. IZI ea. e,,z17 TL i:::-,::.~ ...J,.J. 17 Pl.) 0. l SPHH.H{LEF< SYSTDt! HYDf<t=lULI C t4N?~LYSI S JOB TITLE : U1RLSBAD HESEARCH CENTEH -·-LOT #48 C1~LC #2 ROOF PIPE DATA <cont 1 d) PIPE T•:lG Er-m NODES ELEV. <FT> 25 26 27 151 151 152 152 i53 153 154 1 ~54 155 Pipe: 7CJ 26.0 26.tZt Pipe: 8121 26. tZt 28.8 Pipe: 81 28.8 28.8 Pipe: 82 28.8 28.8 Pipe: 28.8 28.8 Pipe: 84 28.8 28.8 Pipe: 85 155 28.8 156 28.8 156 157 157 158 158 159 159 28 201 21212 202 30A Pipe: 86 28.8 28.8 Pipe: Pipe: Pipe: 87 28.8 28.8 88 28.8 28.8 89 28.8 26. e, 28.8 28.8 Pipe: 91 28.8 28.8 NOZ. 00 0. Q) e,. e, l[.i. l[.i Qt. tZ1 11.5 11. 5 11. 5 0. tZt Q(GPM) DIACIN> LENGTH Pf<ESS. PT DISC. VELCFPS> HW(C) <FT> SUM. (PSI) (PSI> <GPM) F.L./FT 53.9 5-'~. 8 t)9. 8 58.7 58.7 58.8 58.8 t38 . 9 58.C) 59 . tZt 5 <). 0 59 . 1 59 . 1 59.2 5 ':). 2 59 .3 59.3 59.4 5 ':). 4 59.5 59.5 61.2 32.2 0. e, e,. 0. ILi. tZI e,. 121 121. It) e1. e, 0. Ill t21. 0 -3':>.7 -39.7 -,, .... ,. ..., . ..., --3'). 7 -39.7 2. 21Zt3 PL 12Q.i FTG 0. lt.'llZI') TL 2.203 PL 12121 f-TG '21.012 TL 2.203 PL 120 FTG 0. 1Z112 TL 2.203 PL 120 FTG ,Z1. il:112 TL i:::. 21Zt3 PL i 2il'I FTG 1Z1. 012 TL 2 .. 2e13 PL 1 ~~IZt FTG tt.'I. 012 TL 56.50 -'~T 96.50 11.00 L 1 1►• 00 8.00 8.00 PF PE PV PF PE PV PF PE PV PF PE pt.,1 PF PE PV -39.7 ~.203 PL 8.00 PF 0.0 3.3 120 FTG PE 0.0 0.012 TL 8.00 PV tZt. 121 e,. 0 0 .. 121 ILi ,. It) 121. 0 ll.l . e, 65.2 65.2 -·39. 7 ·····3'). 7 ····39. 7 ·-65. QI ...,. 6 2. 21t.13 PL 120 FTG 1t.i. IL'ti 2 TL 2. 21213 PL 12Q'.I FTG IZt .1Z11 2 TL 2.203 PL 120 FTG e1. Q.112 TL 2. 21213 PL 12Q) FTG L 012 TL 2. -/03 PL 120 FTG e1. ell 1 TL 2. 703 i=1L 121li F .. ~G 121. 12)41 TL 8. 1210 8.00 1 7 . 51Zt 2T 37. 5121 18. IZl!li 15. IZtlZI T 2 7 . IZtlt.l PF PE pt_.1 PF PE PV PF PE PV PF PE PV PF PE PV PF PE P'vl 1Z1. 9 0. t2l 0. 1 121. 1 ~_'l. ,ZI tZt. 1 0 . 1 !Li . iz1 0. 1 0. 1 e1. e, 0 .. 1 0 .. i e1. 1z1 ll'I. 1 0. 1 0.0 tZt. 1 121. 1 t21. 12) e1. 1 IL'I • .l e1. e, 0 •. l Q'i. i 121. IZt 0. 1 0.5 1.2 Ill . 1 1..1 e1. e1 0 • .t'.1- SPFHNhLEf< SYSTEM HYDHt=1ULlC ANALYSIS JOB TITLE: CARLSBAD RESEARCH CENTER -LOT #48 CALC #2 ROOF PIPE DATA <cont'd) PIPE TAG END ELEV . NOZ. ' NODES (FT> CK) Pipe: ':12 31ZtA 28. 8 26. e, 21213 30A 2Q1L• 21215 21Zt5 206 Pipe: Pipe: Pipe: 93 28.8 28.8 94 28.8 28.8 95 28.8 28.8 Pipe: 96 11. 5 t21. Ill 11. 5 11. 5 11. ~) 11. 5 206 28.8 11.5 24A 28.8 0.0 Pipe: 97 207 28.8 11.5 208 28.8 11.5 Pipe: 98 208 28.8 11.5 209 28.8 11.5 Pipe= 99 20S 28.8 11.5 22A 28.8 0.0 6 a 8 H.'i 10 12 Pipe: 100 26 .0 2G.0 Pipe: 101 26. Qt 26.0 Pipe: H'.12 2&. e, 26. 0 Pipt:·: 11213 26.0 26. QI Pipe: H'.14 26.0 26.0 Q(GPM> DIA<IN> LENGTH PRESS. PT D I SC. VE L ( FPS ) H l.-J ( C ) ( FT ) SUM. <PSI) <PSI) <GPM> F.L./FT -...... ~. ···· . ..:,..:, . ..:, 32. ':i 41+ • L. it5. 1 '+5 . 1 L►7 . 5 L• 7 • 5 51.2 4L•• 4 1~5 . 1 45. 1 1+ 7 . G 47.G 51.2 56.9 56. '} 56.9 56.9 56.<) 56.8 56.8 56.7 56.7 56.6 --1 9 G • 1 2. 7 lL~ 3 PL 2 1 tZt. 1Zt0 PF 1 <). ·, 0.0 11.0 120 FTG T PE 1.2 0. Qt 65.9 121. 0 76.6 Tl . 2 Tl. 2 79 .3 -·-65. ',) --76. G 6.5 --153. 9 13.0 0.088 TL 222.00 PV 2. 2~'.13 PL 120 FTG 0. '2132 TL a:::. 203 PL 12Q.'I FTG IL•. 042 TL i::'.. 203 PL 120 FTG ll'I. 153 TL 3. !Lilli T 13. e,0 16.00 16.00 PF PE PV PF PE PV PF PE PV -233.2 i::'..203 PL 1.00 PF 79.3 19.6 120 FTG T PE 0.0 0.330 TL 11.00 PV -76 .7 2.203 PL 16.00 PF 76.7 b .5 120 FTG PE 7 7.2 0.042 TL 16.00 PV -153.9 2.203 PL 16.00 PF 77.2 13.0 120 FTG PE 79.3 0. 153 TL 16.00 PV -233.2 2.203 PL 1.00 PF 79.3 19.b 120 FTG T PE 0.0 0.330 TL 11.00 PV 47.2 4.310 PL 4.50 PF 0.0 1.0 120 FTG PE 1Z1. Ill tZt. 01211 TL 4. 51Zt P\.1 96.0 4.310 PL 12.00 JF 0.0 2.1 120 FTG PE 0 .0 0 .002 TL 12.00 PV 144.9 4.310 PL 12.00 PF 0.0, 3 .2 120 FTG PE 0 .005 TL 12.00 PV 194.2 4.310 PL 12.00 PF 0.0 4.3 120 FTG PE e1. Qi Ii). IZllli r:) TL 12. 00 ~-'V ll) .. ILi 121 .. 0 7 .92 PF 5 .4 120 FTG PE 0.014 TL 7 .92 PV QI. L~ 0. 1Z1 121. 2 .::;. 6 121. i;:) 2 . (, !Li. 7 121. e, 0.3 0. (ZI 1.1 i.::'.. 6 Qt., It) 0. e, tli. tZI ill. 12t 0. e, !l). 121 tZ1. l fi. Ill tZt. e,. 1 tt.i . 0 0. 1 It.\. 1 lli . ,ZI 0. i;;~ SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 JOB TITLE: CARLSBAD RESEARCH CENTER -LOT #48 CALC #2 ROOF PIPE DATA (cont 1 d) PIPE T(4G END ELEV. NOZ. NODES <FT> <K> 12 14 14(-) 16 16 18 18 20 2121 22 22 24 3121 3 7 ':) ·) 1 i 1 1 31 Pipe: Pipe: Pipe: Pipe: 105 26. 0 26.0 106 26.0 26.0 107 26.0 26.0 H.18 26.0 26.0 Pipe : 1121·~ 26.0 2G.0 Pipe: 1H.i 26.0 26. e1 Pipe: 111 26.0 26 . IZI Pipe: 112 26.0 26. e1 Pipe: 113 26.0 26. IL'l Pipe: 114 26. 121 26. Q) Pipe: 115 26.0 26. IZt Pipe: 116 2G.0 26. e, Pi pe: 117 26.0 26.0 0. 0 0.0 0.0 0.0 IZI. 121 0.0 e1. e, e,. e, Q(GPM) DIA<IN) LENGTH PRESS. PT DISC. VEL<FPS> ~W<C> <FT> SUM. <PSI> <PSI> <GPM> F.L./FT 56.6 56.4 56.4 56.2 56.2 5G. 1 56. 1 55.6 55.1 54.6 54.2 5Lt-. 2 54. 1 61.8 Gl.8 Gl. 8 61. 8 61. 8 61. ·:) 61. ·:) 61. C) 61.9 61.9 e,. e, 1Z1. 0 121. e, t21. Q) lli. t21 IZt. 0 345. 1 -7 r I. b 3Lt-5. 1 7.6 397 • Lt- L ... 31 IL'I PL i2Q.1 FTG 1Z1. 019 TL Lt. 3H) PL 120 FTG 0. t212f., TL Lt. 3ltL.1 PL 121li FTG 121. 026 TL -'►• 3H.i PL 120 FTG 12.00 12. 0121 5. IZIIZt 5. tZl0 PF. PE PV PF PE p1...,1 PF PE PV PF PE 0.034 TL 12.00 PV 4~1.G 4.31~ PL 12.00 PF ti.1. ,Z1 • 9 • 9 1 2 0 FT G PE 0.0 0.043 TL 12.00 PV 508. 1 4.310 PL 9.54 PF 0.0 11.2 120 FTG PE 0.0 0.~5~ TL 9.54 PV 344. 1 4.310 PL 16.00 PF 0.0 7 .6 120 FTG PE 0.0 0.02G TL lG.00 PV 121. 0 ei. e, 1 C) 6 • 1 L,-. 31 0 PL 9. eei PF 4.3 120 FTG PE 0.009 TL 9.00 PV -47.2 6.403 PL 12.00 PF 0.0 0.5 12Q FTG PE 0.0 0.000 TL 12.00 PV -96.0 6.403 PL 12.00 PF 0.0 1.0 120 FTG PE 0.0 0.000 TL 12.00 PV -1 L,-L .. • ') ei. e, 1. "t-e,. ,z, 6.403 PL 12.00 PF 120 FTG PE ~.001 TL 12.00 PV ····191,. 2 b • .t.1-1Zl2:; PL 12. 00 PF 0.0 1.9 120 FTG PE 0.0 0.001 TL 12.00 PV -244. ~:: Qi. 0 2. 1,. !Li. li.'l 6 • .l .. 1213 PL 5. 2C) 12121 r:·TG T IZt. IL'IQ)2 Tl-35. 29 PF PE pt.,1 e,. 2 121. Q't 0.3 0.2 0. 12) Q1. L; tZt. 1 0. 121 0. l1. 0 . .L~ Ill. IZI 121. 5 0. 5 It). Ill tZI. 7 li_'i. 5 0. IZt li_i. 8 0. 1 0. e, ll • 1 tZI. QI e,. ei 0. ,Z1 e,. e, tZI. tZI e1. Ql 0. Qt Q,. ,Zi 0. ,z, e. 0 0. 1/..1 e,. ei e,. 1 0.0 tZt. Ill SPf<INKLEf< SYSTEM HYDF<f4ULIC ?1Nf4LYSIS JOB TITLE: CARLSBAD RESEARCH CENTER -LOT #48 CALC #2 ROOF PIPE DATA <cont'd) PIPE TAG END ELEV. NOZ. NODES <FT) 00 Pipe: 118 31 26.0 0.,121 0.0 TOH 25.5 Pipe: 119 TOR 25.5 0.0 BOR 0.5 H.S. Pipe: 120 BOR 0.5 H.S. U5 -3.0 0.0 Pipe: 121 U5 -3.0 0.0 U4 2.0 0.0 U3 U4 U3 U2 Ul 23 23 21 19 17 17 15 15 13 Pipe: 122 2.0 2.0 Pipe: 123 i::'..0 0.0 --.::,. e, 0. 121 Pipe: 12"• -3. 0 0. 121 --3. 0 SRCE Pipe: 125 2€:l ■ Q) 0. Qt 26. 0 !li. QI Pipe: 126 26. 0 121. e, 26. 0 0. e, Pipe: 127 26.0 26.0 Pipe: Pipe: pi pt?: 128 26.0 26.0 129 26.0 26.0 130 26.0 26.0 Q(GPM> DIA<IN> LENGTH Pf~ESS. PT DISC. VEL (FPS) H~J (C) (FT) SUM. <PSI> <PSI) WPM> F. L. /FT 61.9 62.6 ·-662. 5 !li. ~)• 6. 6 0. IZt 6.403 PL 22.75 PF 120 FTG L PE 0.013 TL 31.75 PV ILi. L~ (). 2 0.3 -662.5 6.403 PL 25.00 PF 0.3 62.G 0.0 6.6 120 FTG PE 10.8 73.7 100.0 0.013 TL 25.00 PV 0.3 -762.5 8.510 PL 10.00 PF 0. 1 73.7 100.0 4.3 140 FTG L PE 1.5 75.3 0.0 0.003 TL 21.97 PV 0. 1 -762.5 7.987 PL 260.00 PF 1.3 75.3 0.0 4.9 150 FTG 7L PE 2.2 74.4 0.0 0.004 TL 355.20 PV 0.2 7'7J • .Lt, 74. Lt FIXED PRESSURE LOSS DEVICE 5.0 psi, --; ,. .·-. c::· , ba::. • ._, gpm -762.5 7.987 PL 12.00 PF 79.4 0.0 4.9 150 FTG T2L PE 81.9 0.0 0.004 TL 84.53 PV -762.5 7.987 PL 40.00 PF 81.9 0.0 4.~ 150 FTG TG PE 82.2 (N/A) 0.004 TL 89.87 PV -85.2 6.403 PL 12.00 PF 61.6 0.0 0.8 120 FTG PE 61.6 0.Q 0.000 TL 12.00 PV -154.4 6.403 PL 9.54 PF 61.6 0.0 1.5 120 FTG PE 61. & ll'I. 0 ,:). e,01 TL •:). 54 P'v1 61. b ['\ 1. 6 61.6 61. 7 61.7 61.7 61. 7 61.8 --211. e1 11.l.QI i:::'..1 it). Qi e1. 121 e,. e, ·-265. 1 2.6 ·····31 7. L~ Q1. IL\ t;:.'l. 0 121. e, e,. tt.1 -· 36B. 3 3.7 6. i~03 PL 12. ")QI 120 FTG 0. 1L'l1Z12 TL 12. ".11Li G • .i'.H;:.'13 PL 12ii) FTG 0. tZlii)2 TL 6. J.~03 PL 12tZI FTG e, • !i'.I 1213 TL 6. LHt.13 PL 120 FTG tZ1. 1Zt04 TL 12.00 12. tZ11l.'l 12. e,121 12.00 PF PE p,,i f.'F PE PV 0.3 · ... , ·=· I.-. I.- IZt. ~ 1£1. 0 e,. 2 0.0 ILi. ILi Q.i. Ill tZi. 11..i 0. Q) tZt. 121 e1. ei IL. tZ1 '21. Ill ILi. tZI QI. QI f'I. Qt 0.0 0 .. Qt (i. 1 IL'i . 1 0. QI 0. 1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS JOB TITLE: CARLSBAD RESEARCH CENTER -LO T #48 CALC #2 ROOF PIPE DATA (cont'd) PIPE TAG END ELEV . NODES (FT) Pipe: 131 13 26. 0 31 26. 0 l OTES: NOZ. <K> 0. I{) 0. 0 Q(GPM> DIA<IN) LENGTH PT D I SC. VE L ( FPS ) Hl,,J < C ) < FT) <PSI) <GPM> F.L./FT ··-LdB. 3 b. 403 PL 2. 62 61. 8 0. QI L~ • 2 12e1 FTG T 61. 9 121 . IZI 12,. 1L)IZ15 TL 32. 62 PHESS. SUM. <PSI> PF 121. PE 0. PV It). -:::, ,_ ll'l 1 (1) Calculati ons were performed by the HASS 5.5.0 computer program under license no. 8926J521 granted by HHS Systems , lnc. 2193 Ranchwood Dr., N.E. Atlanta, GA 30345 (2) The system has been balanced to p rovide an average imbalanc:·e at each node of 0. 01l.H ypm c::Hid c:1 mciximum imbalance at any node of 0.121 gpm. ( 3) Velocity pressures are printed for not used in balancing the system. any pipe is 19.6 ft/sec. i n f or m c.i t i on on l y , and c::i ·r-, e Maximum water velocity in (4) PIPE FITTINGS TABLE Pipe Table Name: STANDARD .PIP PAGE: F M(rrEHIAL: DYNAFL HvJC: 121i) Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G r:'.°.l El'l Tee LNGELL Cl-W,'v1L BFYVLV Grff vL t..1 ALMCHt< 2 . 2tZ13 5. 1Zt0 1 lZI. ti)l21 3 . 1210 11.tZllZI 6. 121121 1. 0Ql 10. 121121 2. 7Q:'l3 6. Q.ilZl 12. 0Q.i L~. 00 1.lt. ii.10 7.00 1.00 H'.I. 00 3 . 31.l► 7 . @:ll 15. 1210 5.@21 16.00 112.1. e,12, 1. ILllZt 13. 121121 4. 31 e1 10. 1£10 20. 0~'1 6 . QilZI -:::,-:, ,_ ...... fll~'i 12.00 -'t. tZlQ'i 2 lli • Ill It) 6. 41Zt3 14.00 30. 12uZt 9 • 12_iQ1 32. 1Z11Z1 H). 1Z1l21 3 .00 28. 121121 D DPVLV 112). tZIIZI 1 e,. ll,11i,1 10. 1Z1Q) 1 e1 . eie, 1 '}. 12)12) SPRINKLER SYSTEM HYDRAULIC ANALYSIS JOB TITLE: C(-H'<LSB~m t1ESEAF~CH CENTEH ···-LOT :*48 cnLC H2 t"<OOF W~TER SUPPLY CURVE j:) ·< L:. s s u Ii E p s I 12Q)·~ \ \ \ \ \ \ \ \ \ \ \ \ \ \ \ \ \. \ \\\\0\\\\\\\\\\\\\\\ 1 10+ I 11Z1Q1+ I ,;:.)QI+ I X 80+ I I 7 1Zt+ 60+ I 5121 + 3t2t+ I====================-========= 2 0 + LEGEND X -required Wate r Suppl y 82.24 psi@ 11f2.5 gp~ 1121 + I 0 = Available Water Supply llG.89 psi@ 1162.5 gpm II ·M· ( ·•• 1 1 5. QI p S i l]i 1 5 3 0 g p Ill Flow Test Point e1 ·1-·i· ---t-·--····· ·-1-----·-· ··· ·i· ·-·· --•·• ··-·--01 • ··-· ···-··-···-.. -···-.. , .. ··---· ..... ----· -·-·--···-+· ----·· ..... ···· ----·-..... --+· -·-........ ···-..... ---·-----·-1---··-... _ --·-··• ... _ .. -. --·--·-....... ··I .. 400 600 800 1000 1200 1400 1600 1800 2000 FLOW <GPM) ACTION FIRE SYSTEMS ':)185 HARNESS ST. SPF< I I\JG VALLEY, Ch. S> 1977-39.LtB HYDRAULIC CALCULATIONS CRC LOT ;lf.i'.•8 CAF<LSBhD, en. FILE NUMBER: 98-762 7---<-)--98 OCCUPANCY CLASSIFICATION: DENSITY: AREA OF APPLICATION: COVERAGE PER SPRINKLER: NUMBER OF SPRINKLERS CALCULATED: TOTAL SPRINKLER WATER FLOW REQUIRED: FUTURE T. I. UNDER MEZZ. • 2121 gpm/ sq. ft. 1 5 t21 IZt sq • ft • 1 3 !l'i sq • f t . sprinklers gpm TOT ►--iL ~J~ffER REQU I F<ED (including hose) : 65Q). "• g pm FLOW AND PRESSURE (@ BOR>: 410.4 gpm@ 75.2 psi SPRINKLER ORIFICE SIZE: 1/2 NAME OF CONTRACTOR: CORNERSTONE CONSTRUCTION DES IGN/L.:-iYOUT BY: BR I f41"J t,.JE IT inch AUTHOf< I TY HAVING JUR I SD I CT l ON: Ct-H<LSBhD FI BE DE~-'l CONTRACTOR CERT!FICATION NUMBER: C-lG 388160 Cf.:\LCULATIONS BY Ht=lSS ClJIYIPUTEF< PfWGf~AM <LlCEt"SE 4:~ 8926J521 HHS SYSTEMS, INC. hTL~lNTt=i, GA SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 Date:: 11/ll)l/91 C::\76~:::-3 JOB TITLE: CARLSBAD RESEARCH CENTER.-LOT #48 CALC #3 MEZZ FLR· #1 WATER SUPPLY DATA I SOUHCE NODE Tl=lG Lil STATIC HES ID. FLOW AVt4 IL. PF<ESS. PRESS. @ PHESS. <--PSI> <PSI> <GPM) <PSI) 12e,. 0 115. tZt 1 53121. I[_\ 118. 1 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE TOTAL HOSE STREAM ALLOWANCE AT SOURCE OTHER HOSE STREAM ALLOWANCES TOTAL DISCHARGE FROM ACTIVE SPRINKLERS NODE ANALYSIS DATA I\JODE TAG ELEVATION <FT> 28.8 NODE TYPE PRESSUHE <PSI> 61.2 t]I TOTAL RE:.Q, D DEMAND PHESS. (GPM> <PSI> 82.1 ~~ GPM 1 c:;0. • l GPM 100. 0 GPl'11 .L• 10 . .Lt GPM DISCHARGE <GPM> SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 JOB TITLE: CARLSBAD RESEARCH CENTER -LOT #48 CALC #3 MEZZ FLR #1 JDE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE 112•2 103 112•4 105 h'.16 112•7 11218 109 1 10 111 1 i2 113 1 i .lt 1 15 1 16 1 17 1 18 1 1 ':j 12ii) 121 122 123 124 125 126 127 128 12':i i30 131 12'2 i33 1 3J'.t 151 152 1!33 154 1~5 1 ~6 157 158 15':j 160 161 162 163 164 165 1Gb 167 168 169 17121 171 <FT> (PSI) <GPM) 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. 28. B 8 B 8 8 B B B 8 8 B 8 B B 8 B 8 B 8 B B 8 8 8 8 8 8 8 8 8 B B 8 6 8 8 8 8 8 B B 8 8 8 8 8 B 8 8 B 8. 8 B 8 I 61.2 61.3 61. 1t 61.4 61. 5 61.6 61.6 61. 7 61. 1 61.2 61.2 61. 3 61. it 61. 4 61. 5 61.6 61.6 61. 1 61. 1 6i.2 61. 3 61.4 61. 4 61.5 61. 6 61.6 61. 2 61.3 61. 3 61. "• 61.5 61.6 61. 6 62. 1 62. 1 62.2 62.2 62.2 62.2 62.3 62.3 62.3 62. 1 62. 1 62.2 62.2 62.3 62.3 62.3 62.4 61.5 61. 6 61.6 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 JOB TITLE: CARLSBAD RESEARCH CENTER.-LOT #48 CALC #3 MEZZ FLR #1 JDE TAG ELEVATION 'NODE TYPE PRESSURE DISCHARGE 172 173 171• 175 17& 177 178 179 1ae, 181 182 183 18.it 201 21Zt2 2tZa3 204 2e15 21Zlb 21Z1°7 21218 21Ll9 31Z11 3tZ•2 303 304 31215 306 ~07 3t2)8 31Z1'J 310 31 1 312 313 314 :-;0 51 5 2 c:-···, .J..!J 54 c:·t::-...J...J ~jb 57 1 2 ~ 4 ~ 6 7 8 <:j 1 ii) <FT> <PSI) <GPtrO 28. B 28. 8 28. B 28. 8 28. B 28. 8 28. B ·2a. 8 28. B 2B. 8 28. B 28. 8 28. B 28. B 28. B 28. B 28. B 28. B 28. B 28. 8 28.-8 28. 8 1 1. -::, ._ 11. 2 1 1. 2 11. 2 11. 2 11. 2 1 1. C: .J 11. i;;.-.J 1 1. c::· .J 1 1. 5 1 1. -, .,!, 11. 3 11. 2 1 1. 2 10. 6 1 t21. 6 1121. 6 UZI. 6 1'21. 6 10 • 6 1 '21. 6 1121. 6 26. 0 26. 0 26. It) 26. 121 26. ei 26. 0 26. tt.l 26. 0 26. 0 26. 0 ~\= 5. I-<= r-· ...J. K= ,::· ...J. K= i:::-...., . ~<= a:;;-...J. K= r.:.-...., . ~<= i:::· -....,. v-· ,-1::· ...., . ~<= c.::· .J. K:::: 1:::· ...., . K= 5. I-<= r-;:'J. K= i:::· .J. I-<= 5. --- 5tZI 51£1 50 51Zl 51l) 51£1 5tt.) 5t:L) 5121 50 5121 50 50 5121 -· 61.7 61.8 61.8 61.9 62.0 62. 1 61. 6 61. 7 61. 8 61.B 61.9 €., 2. 121 62. l 60. ll) 60. e, 6 ~). 1£\ 6121. 2 6tt.,. 2 6121 .. 2 6121. 1 60. 1 61Z1. 1 25.9 27.8 29.6 27.2 27.7 22.3 2i ... 8 26.5 28.2 30.6 31.4 33.2 33.9 32.B 33 .. 2 33. ,:_, 34.7 itB. 1 59.7 61. L~ 61.7 63.8 61. 4 63.B 61.4 63.B 61. Lt 63. a 61.3 28. ii) 2'-j. Ill 29.9 28.7 29.121 2'3. 9 26. Ill 27. '+ 28.3 2<-). 2 3121. 4 30.8 31.7 SPRIN~<LEf< SYSTEM HYDF<AULIC ANALYSIS Page 4 JOB TITLE: CARLSBAD RESEARCH CENTER -LOT #48 CALC #3 MEZZ FLR #1 ODE T~~G ELEVATION NODE TYPE Pf<ESSUHE DISCHAF<GE <FT> 11 26. 12 26. 1 -~-..., 26. 14 26. 14f4 26. 15 26. 16 26. 17 26. 18 26. 19 26. 212' 2b. 21 26. 22 26. 22A 28. 23 26. 24 26. 24t4 28. 25 26. c:6 26. 27 26. 28 26. 2'::.) 26. 31Zl 26. 30A 28. 31 26. TOH ·:..•= a......J. BUH 121. U5 ·--3. U4 2. U3 ,::, ...... U2 -3. U1 --3. 0 0 0 0 0 0 0 0 0 0 0 0 0 B 0 0 8 121 !l1 0 0 0 121 B 0 5 a::;--...s 0 0 0 0 fl) HOSE STF<El'.:\M SOW<CE (PSI) 63.8 61.3 63.8 61.2 61. 1 63.8 l" 1. 1 63.8 61. 2 63.8 61. 2 63.8 61.2 6121. 1 63.8 61.2 60.2 61.8 62. 121 63.7 63.8 61.2 6121. ill 63.Sl 64.2 75.2 76.8 75.2 aiz,. 2 82.5 82.7 (GPM) 100.0 SPRINKLER SYSTEM HYDRf:iUL IC ANALYSIS Pc,ge i:::-J JOB TITLE: CAf<LSBAD RESEARCH CENTEf< --LOT #48 CALC #3 MEZZ FLR *~ 1 PlPE DATA PIPE TAG G! <GPM> Dlh<IN) LENGTH Pf<ESS. END ELEV. NOZ. PT DISC. VEL<FPS) HW(C) <FT> SUM. NODES <FT> <K> <PSI) <GPM> F. L. /FT <PSI) Pipe: 1 -31. 9 2.203 PL 20. 33 PF 121. 3 i 26. 0 0. 0 61. 4 0. 0 2. 7 120 FTG T2L PE 0. e, 2 26. Qa 121. 0 61. 1 0. 0 121. 008 TL 36. --. ~ ..:, ..:, ·pv Q.). QI Pipe: 2 --31. '.) 2. 2Ql3 PL 70. Qt0 PF 121. 7 2 26.0 0.0 61. 7 0. IZt -::, '-. 7 120 FTG T PE 1. 2 HH 28. B 0.0 61. 2 e,. 0 IL). Q108 TL 80. 00 PV 0. fl) Pipe: 3 ·--31. ·=., 2.203 PL 8.00 PF 0. 1 H'.11 28. 8 0.'0 61. 2 0. 0 2. 7 12121 FTG PE ll,1. 0 102 28. B 0. 0 61. 2 121. tZ1 '21. 12108 TL 8.00 PV 0. 12) Pipe: 4 --31. '.) 2. 21213 PL 8. 00 PF e,. 1 H)2 28.8 0.0 61. 2 e,. 0 -:::. '-. 7 12ti) FTG PE 0. Ill 103 28. 8 12'1. 0 61. 3 0. 0 flt. '2108 TL 8. e,0 PV e1. 0 Pipe: 5 I ·-31. •:) 2.203 PL B. 00 PF tZt. 1 11.Zt3 28. 8 0.0 61. 3 0. 0 ·::• 7 120 FTG PE e,. 12) '-. 1 Q'.14 28.8 0. 0 61. 4 121. 121 0. Q108 TL a. 1L•t21 PV 0. 121 Pipe: 6 -31. <:) -::, 21213 PL B. Q.'1121 r-,F 1£1. i L.... . 1 ,Z14 28. B 0. 0 61. 4 tZt. Q.) 2. 7 120 FTG PE e, . 121 11l15 28. B 0. 0 l-d. Lt, 0. 0 Ill. 008 TL B. 1210 Pl) ei. 121 Pipe: 7 -31. '.) 2. 21213 PL B.00 PF 1Z1. 1 ill'.15 28. 8 0. ~) 61. i► 0. e1 2. 7 120 FTG PE 121. 0 lflt6 28. B 0.0 61. 5 0. 0 0. 1Z11Z18 TL 8.00 PV 0. IZt Pipe: B -31. 9 2. 21213 PL 8. 1£10 PF Qi. 1 106 28.8 tZl. tZl 61. i::· ""' 0. ILi 2. 7 120 FTG PE IZI. Ill 1 e,,7 28. 8 0. 0 61. 6 il'I. 1£1 0. e10a TL B. 00 PV 0 .. 1£1 Pipe: '.) --31. C.) 2.203 PL B. tZ11Z1 PF IL•. 1 1 t.b'l 28. B 121. ll,'l (·d. 6 1Zt. e, ·:::, L.... 7 121l'.I FTG PE 121. aZI 11Za8 28.8 Ill. t2l 61. G Ill. az, e,. 1Z11Z1B TL 8. Q11Z1 PV e,. e, Pipe: 1121 -·31. 9 ·-·· I-. 21Zt3 PL 8. 01l.l PF Qt. 1 108 28. B 0.0 61. 6 0. IZt 2. 1 1212, FTG PE 0. Q) 109 28. B 0. 0 61. 7 tt). QI, 0. 008 TL 8. 1£)0 PV 0. 0 I Pipe: 1 1 -·-31. <) 2. 212,3 PL 87.00 PF ILi. <) 1 lb':j 28. 8 0. lli 61. 7 0. 0 2. 7 12Q.l F~'TG 2T PE 1. 2 3 26.0 0. ,Zt 63. 8 e1. 0 Ill. e11z1H TL 107.IZ•tZI PV 0. Ill Pipe: 12 -.. 32. 9 -::, 203 PL 80. t2llll PF e,. 9 L.... L► 26. 0 iz1. 0 61. 4 e,. IL\ 2. 8 121Zt FTG 2T PE 1. 2 11121 28. B 0. 0 61. 1 e,. Q,1 0. 12109 TL 11£10. Q11l'l PV 0. 1 Pipe: 13 --32. ·:) 2. 2tZl3 PL B. ll'ltZI PF IL). 1 1112• 28. B 0. 0 61. 1 121. 121 · ... • '-. 8 .L2t21 FTG PE 0. e, 111 28.8 0. 0 61. 2 ii). IZt 121. 1Lit21~:) TL 8. Ii)!£\ PV 0. 1 SPHIM<LEF< SYSTEM HYDRnULIC ANALYSIS Page 6 JOB TITLE: CARLSBAD HESEARCH CEI\JTEH -LOT #48 CALC #3 MEZZ FLH #1 PIPE DATA (c-ont• d) PIPE TAG Q<GPM> DIA(IN> LENGTH PRESS. END ELEV. NOZ. PT DISC. Vf:::L <FPS> HW<C> <FT> SUM. NODES <FT) <K> , <PSI> <GPM) F. L. /FT <PSI> Pipe: 14 -32. '.) 2.203 PL 8.00 PF t21. 1 111 28. 8 0. 0 61. 2 0. 0 2. B 120 FTG PE 0. Ill 112 28. B 0.0 61. 2 lli. 12.i Ill. 00<:) TL 8.00 PV 0. 1 Pipe: 15 · -32. Cj · ... • L-. 203 PL 8. 12,0 PF tt.'l. 1 112 28. 8 0. 0 61. 2 ei. 0 2. 8 120 FTG PE 0. Ill 113 28. B 0. 0 61. 3 e,. 0 IZI. 01i)9 TL B. 12.10 PV 0. 1 Pipe: 16 --32. Cj 2.203 PL 8. 1Z10 PF 0. 1 113 2B. B 0.0 61. 3 ll.l. IZI C • 8 120 FTG PE 121. 0 114 28.B 0.0 61. 4 0. 12.i 0. 0121':) TL B. euz, PV 0. 1 Pipe: 17 -32. 9 2.203 PL 8. tt.10 PF Ill. 1 114 28. B 0. t21 61. 4 0. 0 2. B 120 F 'fG PE 0. iz, 1 i5 i:~8. 8 ii.l. Ill 61. 4 12,. 1£1 tZI. ,ZlfllCj TL B. e,0 t::-•v 12.'l. 1 Pipe: 18 --32. C) 2.203 PL 8. ~)0 PF IZI. 1 11 ~:j 28. B 0. e1 61. 4 0. 0 2. 8 120 FTG PE ll.l. Ill 116 28. B 0.0 61. a::-..J 0. 0 e,. 012.1<) TL B. e10 PV ti). 1 Pipe: 19 --32. C;J ·-· L-. 21Ll3 PL 8. 12.10 PF IZI. 1 116 28.8 0.0 61.5 0. 0 2.8 120 FTG PE 0. 12, 1i7 2B. B e,. 0 61. 6 IZI. 0 0. 1210'.) TL B. 00 PV !Li. 1 Pipe: 2e1 --32. 0:.) 2. 21213 . PL 8.00 PF 0. 1 117 28. 8 0. 1£1 61. 6 e1. Ill 2. 8 120 FTG PE 0. Ill 118 28.8 0.,0 61.6 1£1 • 121· 0. 1211z1 ~) TL B. 01£) PV It). 1 Pipe: 21 --32. 9 2. 21213 PL 87. !l)0 PF 0. Cj 118 28.8 0.0 61.6 0. 12, ·';;) a;..;.. 6 li::'.IZI FTG 2T PE 1. 2 5 26. 0 121. 0 63. 8 (LI. IZI It). tt.10 9 TL 1 tt.17. 0!l) r.:iv ~). 1 Pipe: 22 ··~ . ....,_ --,.!,~. e, 2. 21Zt3 PL 8121. 00 pi:;:-IZI. <) b 26. l2t 0. e, 61. .l. 0. I,() 2. 8 12121 FTG 2T PE 1. 2 11 ,3 28. 8 0. lt.i 61. 1 ii). tZI t21. 01l.~9 TL 1 iZ•IZI. 01L) PV tZI. 1 Pipe: 23 -33. Ill i.~. 21213 PL a. e1e1 PF 1Z1. 1 1 F; 28.8 0. 121 61. 1 12.). 121 2. 8 1 i='.ll) FTG PE Q.1. 121 12!l) 28. B 1£). 0 61. 1 e,. e, e,. t21iz19 TL 8. ")Q\ PV 121. 1 Pipe: 24 -'5'5. 0 2. 21213 PL B. 1Z1QI ~'F e1. 1 1212, 28. 8 0. 121 61. 1 e,. ll1 2. B 120 FTG PE 121. 121 121 28. B 0. JL' 61. 2 0. 12,' Ill. IZtlL)~) TL 8.00 PV Q). 1 Pipe: 25 -33. e, i.:::. 212,3 PL 8. '211li PF e,. 1 121 28. B 121. e, 61. 2 ,21. !Li 2. 8 120 FTG PE 0. 121 12~=:: 28.8 121. 121 61. 3 0. e, I,(). ~)09 TL 8. 1£1,ZI PV Ill. 1 Pipe: 26 ..... 33_ ,21 2. 21213 PL 8. 00 PF 1Za. 1 , 122 28. B 121. 0 61. -, ~ 1£). e, 2 .. B 12QI FTG PE e,. e, 123 28.8 0. 0 61. 4 0. 0 121. l2.)1Z1<:) TL 8.00 PV ill. 1 SPFHN•<LER SYSTEM HYDf<►4UL IC ANt=tLYSl S Page 7 JOB TITLE: crrnLSBAD 't<ESE~➔f<CH CENTEH --LOT #48 CALC U3 MEZZ FLR #1 PIPE DATA (cont' d) PIPE TAG Q(GPM) DH=t<IN> LENGTH PF<ESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) <FT> SUM. NODES <FT> ( K) <PSI> <GPM> F. L. /FT (PSI) Pipe: 27 .. " .. '"' -.:,.:,. Ii.~ 2. 2e,3 PL 8. 00 PF 12). 1 123 28. 8 0. 0 61. i► 0. 0 i:::. 8 120 FTG PE fl). Ill 124 28. B 0. 0 61. 4 0. 0 0. 1Z1Q1(;) TL 8. 00 PV 0. 1 Pipe: 28 -33. tZI ,::, '-. 2Q)3 PL 8. 00 PF 0. 1 124 28. B 0. 0 61. 4 0. 0 2. B 120 FTG PE 0. 0 i25 28. 8 . 0. 0 61. i:::· -..J 0. 0 Q'l. Q.11219 TL a.·00 PV Ill. 1 Pipe: 29 .. "" ··-. --.:,~. t21 .:::. 21213 PL B. 00 PF 0. 1 125 28. B 0. J2l 61. 5 0. 0· 2. B 12.;:,1 FTG PE 0. 0 126 28. B 0. 0 61. 6 0. t21 0. 01219 TL 8. t211Z1 PV 0. 1 Pipe: 30 -33. Ill 2. 21£)3 PL B. 00 PF 0. 1 126 28. B 0. 0 61. 6 e,. 0 2. B 12e, FTG PE 0. Q'I 12'/ 28. B 0. 0 61. 6 1£1. fl_'l • 0. 0~)9 TL 8. 1210 PV Q.1. 1 Pipe: 31 .. "'""' --.:,.:,. I{) 2. 203 PL 87. 00 PF 0. ') 127 28. B 0. 0 61. 6 0. QI 2. B 12Q.'l FTG 2T PE 1. 2 7 26. 0 0. 0 63. 8 e,. 0 Q). 12109 TL 107. tt)0 PV 121. 1 Pipe: 32 --·33. 3 2. 203 PL 'j6. 00 PF 1. 0 8 26. 0 e,. 0 61. 4 121. e1 2. 8 120 FTG 2T PE 1. 2 128 28. 8 0. ll'l 61. 2 0. 0 It). 0,ZlCj TL 116. Q.'l0 PV IL'l. 1 Pipe: 33 --~~-3 i:::. 203 PL 8. e,0 p1::-1Z1. 1 128 28. 8 0. 0 61. 2 ~). 121 2. B 12e1 FTG PE Ill. 0 12q 28. B Ill. IZt 61. ..... ~ e, • 12,1 Ill. 1Z11Z1<) TL 8. IZIIZI PV 12,\. 1 Pipe: 34 -33. 3 i::::. 203 PL 8. Q.'I ll_) PF 0. 1 12q 28. 8 0. 0 61. 3 0. 0 2. 8 120 FTG PE 0. li..'t 13Q1 28. 8 0. 0 61. . .. , 0. 0 121. 009 TL 8. 0121 PV 0. 1 .:, --Pipe: 35 ---~~. 3 2. 212,3 1:::iL 8. ~~0 pi::-Ill. l 13Qa 28. 8 0. 0 61. 3 1£1. 121 i:::. 8 12Q'l FTG PE e1. 121 131 28. 8 0. 0 61. 4 !Ll • 0 121. 1t)IL19 TL 8. IZIIZl PV IJ. 1 Pipe: 36 --.. _;.··:.·· ....,...., . 3 -=~ .._ . 21£13 PL B. e,ei PF e1 • 1 131 28. B Q1.,Q1 61. 4 Ill. 0 ·:::. .._. a 120 F .. TG PE 0. ILi 132 28. 8 0. 0 61. c· -...J 121. 121 1£1. e,09 TL 8. 1210 PV 0. 1 Pipe: 37 ... ,. ..... 3 2. 21l)3 PL B. It) tZI PF 1Z1. 1 ,.J...>. 132 28. 8 0. 121 61. i:::-..J 0. Ill 2. 8 12121 FTG Pt:. 1£). ill 133 28. 8 Ill. 121 61. 6 Ill. 121 0. t211Z1<-) TL 8. 1Z1Q'l PV e1. l Pipe: 36 --33. 3 ·-·' 2121:::; PL 8. e,0 PF e1. 1 .._. 133 28. 8 0. Q1 61. 6 e,. 0 •::, ._. 8 li:~0 t=-TG PE tZt. !l) 134 28. 8 0. lli 6i. 6 121. Q.i ei. 1Z1t21<:J TL B. Q.10 PV ~). 1 Pipe: 3<) ·--·•;;,, ··~, ...., ,..>. 3 2. f~Q13 PL 87. 1Z1Q1 PF. 1. QI 134 28. B 0. 0 61. 6 ill. aZI 2. 8 12121 FTG 2T PE 1. 2 9 26. 0 0. IZt 63. 8 121. iz, 0. 001.) TL 107. 1210 PV ll.l. 1 SPH I N~<LEf< SYSTEM HYDf<,:1uL IC ANt~LYSIS Page 8 JOB TITLE: CARLSBAD HESEAHCH CENTEH -LOT #L•B cr~Lc #~3 MEZZ FLR #1 PIPE DATA (c-ont, d) PIPE TAG Q (Gl=)M) DH4 < IN> LENGTH Vi<ESS. END ELEV. NOZ. PT DISC. VEL<FPS> Hl.-J < C) <FT> SUM. NODES <FT> 00 (PSI> , <GPIYI> F. L. /f:.T <PSI> Pipe: 4121 ... "" .... , 7 2. 21z13 PL 231. !Lhll PF ·::, i::.-.. -~~-...... ..., 1 Ill 26. 121 121. Qt 61. 3 Ill. Ill 2. 8 120 FTG i•T PE !Li. 0 11 26.0 0.,Qt 63. 8 0.0 0. 0121·~ TL 271. '211l.i PV 0. 1 Pipe: 41 --33. s, ·=• 212t3 PL 231. 0121 PF 2~ 5 ...... 12 26.0 0. 0 61. 3 0. 0 i:::. B 1212, FTG 4T PE 0. IZI 13 26. 121 0. 1£) 63. 8 0. 0 e,. ,z1,z1g TL 271. 00 PV 121. 1 Pipe: 42 -·-34. 1;:.• 2. 21213 PL 231. 00 PF ·::, 6 ..., ...... 14 26. ea 0. 0 61. 2 fl). 121 ·=· Cj 12121 FTG .l• T PE 121. 0 ...... 15 26.0 0. 0 63. 8 tZI. 0 0.01121 TL 271.00 1=:av ,zi. 1 Pipe: .l•3 -3-'•· 8 ·=· ...... 203 PL 231. ll.1'21 f-1F 2. 6 16 26.0 0.0 61. 1 e1. 0 a::.:. ~ 120 FTG 4T PE •Zt. ILi 17 26. 0 0. Ill 63. 8 0. 0 ,Z1. ,Zt 1121 TL 271. 1210 PV 1£1. 1 Pipe: 44 --~;4. -, 2. 203 PL 231. ,Z1,Z1 PF ·::. 6 .:, '-. 18 26. ea 0.0 61. 2 12). 0 2. s, 120 FTG .l• T PE 0. Ill 1 ':) 26. t21 t21. 0 63. B 0. 0 It)• tZt 10 TL 271. t210 P'-.,' ll.l. 1 Pipe: -'•5 --3.L~. Ill 2. 2~)3 PL 152. ..:, ..:, PF 1. 6 2121 26.0 0: 0 61.2 tZI. Q) 2. t) 12tlt FTG 2T PE 1 ·:::, . '- 178 28. 8 0. 1£1 61. 6 ~). 0 ~). 009 TL 172. .... , ..... ..:,..:, PV tZl. 1 Pipe: 46 --3.£•. 121 ·=-..... 21213 PL 8.00 PF 0. l 1 .i'8 28. 8 1£1. 121 61. 6 fl'I. 0 2. 9 121li FTG PE Q,. 0 1 7':) 28.8 0. 0 61. 7 0. Ill 0. 1Z11Zl'J TL 8.00 PV 121. 1 Pipe: 1.. 7 --2A. 0 2. 203 PL B. 00 PF e,. 1 17'-) 28. 8 0.0 61. 7 0. 0 2. ·:) 12121 FTG PE 12). 121 i80 28. 8 e,. 0 61. 8 It). 0 e,. 12,,z,g TL 8. 1t.ill:1 PV 0. 1 Pipe: 48 -3.l~. tZI 2. 21213 PL 8. QHZI PF Q). 1 18121 28. 8 0. e, 61. 8 Qt. tZI ·::, g 12~'.l FTG PE Q'i. ,Z1 ._. 181 28. 8 IL,. 0 61. 8 0. ea IL\. ll)t2t9 TL B .. Q)Qt PV IL\. 1 Pipe: 49 -3.1+. e, 2. 21213 PL 8. 00 pr,:· Ii). 1 181 28. 8 0. 0 bl. B 0. tZI 2,. \:} 121ll FfG PE tZt. 1£1 182 28. 8 0. Ill 61. Cj e,. 0 0. 009 TL 8. ,Zt0 PV e,. 1 Pipe: 5121 --3L~ • Ill 2. 2iz13 PL 8.00 PF 0. 1 182 28. 8 121. fl) 61. Cj 0. 121 ·-·' ...... 9 120 FTG PE e,. 0 183 28.8 0. t21 62. Ill 121. ½i 0.00') TL 8. tZt0 PV 0. 1 Pipe: 51 --34. ll1 i.~. 2Q)3 PL B. 0121 PF 12(. 1 183 28. 8 0.0 62. 121 e1. 121 -::, ..... ') 12Q'i FTG PE IL),, Ill 18.l• 28. 8 0.,0 62. i 0. ,ZI' ~). 1210') TL B. (>i0 PV Qi. 1 Pipe: 52 ·-3.l►• ILl 2. 21213 PL 3121. 6 7 Pr=-Q). a;~· ..J 184 28. 8 0. e, 62. 1 ,ZI. ,Zl 2. t) 120 FTG 2T PE 1. 2 21 26. 0 0. 0 63.8 IZt. 0 0. tL'i09 TL 50.67 PV Ill. :L SPHIN~<LEH SYSTEM HYDHAULIC {4NALYSIS Page <:) JOB TITLE: C~".\RLSBAD RESEAF<CH CENTEf< -LOT ~t48 CALC #3 MEZZ FLH #1 PIPE DATA (cont' d) PlPE TAG G!(GPM) DIA<IN) LENGTH Pf<ESS. END ELEV. NOZ. PT DISC. VEL<FPS) Hl--! ( C) <FT) SUM. NODES <FT> < K) <PSI) <GPM) F. L. /FT <PSI) Pipe: a;:--, ··•·. -"' 1:::· 2. 2,213 PL i:::. 83 PF 121. 1 -..., .:, --.:, ..:, . ..J 22 26. t2I 0. t2I 61. 2 0. 0 ·-·· I-. 8 120 FTG T PE 1. 2 22A 28. 8 0. 0 60. 1 0. ~) 0. 01Zt9 TL 12.83 PV 121. 1 Pipe: 51• -·33. i::;· ,_J ·-:., ...... 21213 PL 139. 17 PF 1. L• 22A 28. 8 IZI. t2l 60. 1 tZI. 0 2. a 120 FTG T PE 0. 121 16'.) 28. 8 0. 0 61. c:· ,_J 0. Ill ,ZI., 009 TL 1L~9. 17 PV Ill. 1 Pipe: 1:::·a:::--.:;.:;. ..... -:::., 2tt.\3 PL B. 00 PF tZI. 1 ..J..J ;:; i;.:;.. 16<:) 28. 8 0. 0 61. 5 0. ei 2. 8 12~) FTG PE 0. 0 170 28. 8 0. Qi 61. 6 ea. 0 e,. 12109 TL a. 00 PV ea. 1 Pipe: t:;"I' ..Jb -.. 33_ 5 2 . 203 PL 8. 00 PF 0. l 170 28. 8 0. 0 61. 6 121. 0 2. 8 120 FTG PE Ill. IZI 1 ·/ 1 28. B 0. 0 61. 6 0. 0 0. it.lll'l S> TL B. 00 PV 0. 1 Pipe: 57 .... ~ ...... i::: -· 2Q)3 PL 8. t21t21 Pr=-12). 1 --.:, ..:, . ..J ...... 171 28. 8 0. 0 61. 6 Ill. e1 ~::, I-. 8 121i'.I FTG PE e,. ll'l 172 28. 8 Ill. 0 61. 7 Q.). 0 ea. 1Z10') TL 8. 121121 PV Ill. 1 Pipe: 58 -33. ,::· ..J ·=· L-. 203 PL 8. 1210 PF t21. 1 1 /2 28. B 121. 121 61. 7 0. IZt 2. B 1 i:::'.IZI FTG PE e1. Ill 173 28. B 0. I{) 61. B 121. 0 0. it.'llll S> TL 8. 01t.'l PV 0. 1 Pipe: 5'➔ --33. 1;;.~ 2. 21213 PL 8. 00 PF e,. 1 ..J 173 28. 8 0. 0 61. 8 0. lt.1 ·=· ...... 8 12Ql FTG PE Ill. Q.1 174 28. 8 0. 0 61. 8 0. 0 t21. 01219 TL a. 0121 PV ILi. 1 Pi"pe: (,0 ... -.. ---. --.:, .:, . i:::· ,_J 2. 21213 PL 8. l{:10 PF t2l. i 174 28. 8 0. IZI 61. 8 0. IZI -::, L-. B 120 FTG PE 0. Ill 11t:i i:~8. B !l1. e, 61. Cj 0. 0 ei. 01219 TL 8. ill ill PV 121. 1 Pipe: 61 _-·~ ··:.· ,;;;· 2. ~~tZ13 PL B. (lllt_l PF 0. 1 ...,,.., . ..J 1 "/5 28. 8 0. 0 61. Cj 0. e, ·::, I.... 8 12121 FTG PE 0. 0 176 28. 8 0.,0 62. i;i) 0. 121 12,. e,121·:> TL 8. ll)tZI PV 0. 1 Pipe: 62 --33. 5 -::, L-. 203 PL B. ,Z1Q.1 PF Q). 1 176 28. B 0. 0 62. 121 ILi. e1 ··-· L. •• a 121l) FTG PE 0. (Ll 17 .. / 28. 8 tZt. 0 62. 1 12,. Q.1 e1. t21t2JCj TL 8. ll•'2l PV Ill. 1 Pipe: 63 --··;-·-~ ... 1;.;· 2. 21213 PL 31t). 67 PF e,. 5 ""''-'. ..J i ·,1 28. 8 0. 0 62. 1 tZt. e1 .. • 8 12i21 FTG 2T r.:iE 1. .•. I..... a::'. 2~ 26. 0 iz,. IL\ 63. fi ll'l. e, e1. !Lltll':, TL 5121. 67 PV 0. 1 Pipe: bl► --.c~i21. 6 -::, ~~03 PL · .... • 83 PF Ill. · ... • L.... L-. L- 24 26. 0 0. 0 61. 2 0. e, ·-~ .. ...., . 4 1212) FTG T PE 1. i:~ 21►,4 28. 8 0. 121 60. 2 !l'l. 0 ll.1. 1Zll3 TL 12. 83 PV 121. i Pipe: 65 -4ll'I. b 2. 21Zt3 PL 2121. 1Ztl2'.I PF ILi. lt 24i4 28. 8 0. 0 60. 2 e1. ei 2;. 1,. 12e1 FTG T PE 1. 2 25 26. 0 0. 0 61.. 8 tZI. Ill 121. ll-'13 TL ~31t). 121121 PV Ill. 1 . SPfUNKLEf< SYSTEM HYDf<AULlC ANt4LYSI S Pclge 10 JUB TITLE: CAHLSBAD RESEARCH CENTEH --LOT ~=t:48 CALC #3 MEZZ FLH #1 PIPE DATA (cont' d) PIPE TAG Q(GPM> DIA< IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL<FPS) Hli-J < C) <FT> SUM. NODES (FT> 00 <PSI) <GPM> F. L. /FT <PSI> Pipe: 66 --24. 5 2. 203 PL 24. 5'21 PF 0 .. 2 25 26. 0 0.,0 61. B 121. 0· 2 .. 1 12121 FTG 2T PE tZI. Ill 26 26. 121 0. 0 62. 0 0. Ill 0. 005 TL 44. ~:;iz, PV ILi. It) Pipe: 67 --4121. 6 2. 203 PL 87. ll.10 PF 1. "";i· ..... 26 26. 0 0. 0 62. e, 1Z1. e, .s. L► 120 FTG T PE IL\. Ill 27 26. 0 0. 0 63. 3 0. 0 ll'l. 013 TL ':17. 00 PV ll'l. 1 Pipe: 68 -·-21. 7 •::i .._. 21Z•3 PL 7. 1210 PF 0. !Ll 27 26. 121 0. 0 63. 3 0. e, 1. 8 12ll'l FTG L PE 1. 2 1 bill 28.8 0. 0 62. 1 0. 1£) 0. 12,iz,4 TL 10. IZlll\ PV ILl. iLl Pipe: 6'j --21. 7 ·=· ..... . 203 PL a. ~)QI PF e,. e, 160 28. B 0. 121 62. 1 1£\. 0 1. 8 12tli FTG PE ILi. 12, 161 28. B 0. 0 62. 1 t.21. 0 0. llllZlL• TL a. ll'l0 PV ,ZI. 0 Pipe: 7(i.) --21. 7 ·=· .._. 203 PL 8. tlt0 pi:=· 0. 1Z1 161 28. 8 0. e, 62. 1 0. 0 1. 8 12ll'l FTG PE 121. Ill 162 28. B 0. 0 62. 2 ii). 0 0. IZtlZIL• TL 8. ii.HJ PV It)• 121 Pipe: 71 -·21. 7 2. 21213 PL 8. 00 PF Qi. 0 162 28. B 0.,0 &•::, a;;;.. 2 0. 0, 1. B 120 FTG PE Ill. 0 163 28. 8 0. 0 62. 2 ll.l. fl) ll.1. !l10I¼ TL B. e,12, r.,v ('..1~ ll1 Pipe: 72 -21. 7 -::, I..... 212,3 PL B. li.llZt PF Ill. IZI 163 28. 8 Qi. 0 62. 2 ll.l. QI 1. 8 121l1 FTG p~ Qi. IL1 164 28. B 0. 0 62. 2 0. 0 ii). 1i.\1Z14 TL 8. 0121 PV 0. Qt Pipe: 73 ·-21. 7 2. 2'213 PL 8. 0121 PF 121. Q.'l 164 28. B IZl. 0 62. 2 e,. 0 1. 8 120 FTG PE e,. It) 165 28. B 0. 0 62. 3 e,. e, Q.i. 00-'t TL 8. 1,()0 PV 0. Ill Pipe: 74 -·-21 • . i, 2. 21t)3 PL 8. 0121 PF e,. ILi 165 28. B 0. 0 62. 3 ll.'l. ll1 1. 8 12121 FTG PE e,. e, 166 28. 8 0. Ill 62. 3 0. tZI 1Z1. ILIIL~4 TL 8. 121121 P\.I 0. e1 Pipe: 75 --21. 7 ·-·· L-. c:03 PL 8. IZlll.i PF QI. I[) 166 28. B 0. 0 6·=-~-3 ILl. 0 1. B 120 FTG PE ILl. Ill 167 28. 8 0. 0 62. 3 e,. ,ZI Q). 0!liL• TL 6. e10 PV 1Zt. 0 Pipe: 76 --21. 7 C:. 21213 PL 8. Q1Q) P1.::· 0 .. Ill 167 28. 8 121. 0 62. 3 ,ZI. IZI 1. 8 12e, FTG PE 121. 0 168 28.8 121. 121 62. 't e,. 0 1L1. e,1214 TL 8. 00 PV 121. ll't Pipe: T7 -21. 7 ·-·· 203 PL i::· 50 PF 0. 1 ...... ,.J,. 168 28. 8 0. Ill 62. 4 Ill. I 121-1. 8 12lll FTG T PE 1. 2 28 26. e, 0. 121 r -. b~. 7 Ill. 121 e,. 12101 .. TL 15. 50 PV Ill. 0 Pipe: 78 --'+121. 6 ··i '-'. 314 PL ,•:_.1:;;· L-..J. 17 PF e,. 1 28 26. 0 0. 0 63. 7 t;(). 0 1. ~) 1212, f·· ··1·G 2T PE 0. e, 2'-) 26. 0 IZI. 121 t\3. 8 0. 121 ll.1. 01212 TL L::•1~ ..J..J. 17 PV 0. 1Z1 SPFHN~<LER SYSTEM HYDF<i4ULIC ANf'.\LYSIS Page 11 JOB TITLE: CAF<LSBAD RESEfrnCH CENTEH -·-LOT #4G CALC #3 MEZZ FLH #1 PIPE DATA (cont' d) Pli)E T(~IG Q(GPM) DIA<IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL<FPS> Hl.-J (C) <FT> SUM. NODES <FT) HO <PSI> <GPM> F. L. /FT <PSI) Pipe: 79 -16. 1 2. 2tb3 PL i:·-:• ..)b • 51L'l PF t21. 2 25 26. 0 0. 121 61. B ei. tZI 1. i► 120 FTG i►T PE Q.1. IZl 26 26. 0 0. 1Z1 62. 0 0. ei I[.'\. 01l'l2 TL 96. 50 PV 121. Q1 Pipe: 8!i) --18. Cj ·=· L-. 203 PL 11. 01l1 PF 0. ll1 21 26. 0 0. 0 6 "? w• 7 w ei. 0 1. 6 121l'l FTG L PE 1. 2 151 28. 8 0. 0 62. 1 !l1. 0 0. IZlll'.13 TL 14. ll1fl'\ PV 0. e1 Pipe: 81 , --18. 9 2. 212,3 PL 8. QIQI PF 0. 121 151 28. B 0! 0 62. 1 !l1. 121 1. 6 12121 FTG PE 0. l[.l 152 28. 8 0.0 62. 1 0. 0 0. 12103 TL 8. 121121 PV 1Z1. Qt Pipe: 82 I -18. Cj ·::, L.■ 21l13 PL 8. QlQ.1 i::•F 0. 121 11:;;--·-. ..Ja::. 28. 8 0. 0 62. 1 tZI. Qt 1. 6 121l1 FTG PE 0. IZI 153 28. B 0. e, 62. 2 0. 121 !J). fl103 TL B. 00 PV 121. tZi Pipe: a··;---1 B • •:) ,:j 2Q)3 PL 8. IZIIL'l PF 0. Q1 .. ., L-. 153 28. B 0. 0 62. 2 1t1. 0 1. 6 120 FTG PE 0. 121 15.l► 28. 8 0. 0 62. 2 Q). 121 !l). 01213 TL B. flllZI PV !l). 121 Pipe: 84 --18. Cj i::'.. 2ll'.13 PL 8. 1210 PF e,. 0 15.lt 28. B 0. 0 62. -::, '-e,. 0 1. 6 l 21L\ FTG PE 0. Q'.I 1 ::s5 28. 8 0. Ii) 62. 2 Ill. 0 Ill. 012,3 TL 8. Q10 PV 121. 121 Pipe: 85 --18. c_, 2. 21z13 PL B. 1210 PF Q). IZI ·1~5 28. 8 0. 0 62. 2 0. Qt 1. 6 120 FTG 1=:iE 121. 121 156 28. B 0. 0 62. 2 121. 0 Ill. 01213 TL 8. 00 PV tZI. 121 Pipe: 86 -18. Cj ·=· L-. 21213 PL B. 1210 r•F e,. Ill 1 ~)6 28. 8 0. e1 62. 2 Ill. Ill 1. 6 120 FTG PE 0. Qt i57 28. B 0. 0 62. .., ~ 0. e, Ill. e,03 TL 8. 0e1 PV 0. e1 Pipe: B"l --18. ,:;j 2. 2,z,3 PL 8. e1121 PF ei .. Ill 1~·1 28. B 0. 0 62. ~ ei. 0 1. 6 120 FTG PE Q.1. e1 158 28. B 0. 121 62. 3 0. ' QI, e,. e11213 TL 8. 00 PV Q.'l. IL'l Pipe: 88 --18. (J ·::, L-. 21l13 PL 8. e10 PF Q). 0 158 28. 8 0. 0 62. >a:.· 1£\. 0 L 6 12tt) FTG PE 0. IZI ..., it,<) 28. B 0. 0 62. 3 et. 0 0. ,z,03 TL 8. 1210 PV Ill. tZI Pipe: 89 ···-1 B. (j :J '-. 21213 1::.L 17. 50 pi::;· Ill. 1 15'·j 28. 8 121. e1 62. 3 e,. 0 1. 6 12121 FTG 2T PE 1. 2 28 26. ILi 12.\. QI 63. 7 121. t21 121. tZllt'.13 TL ··_;-.·7 ...;J I • 51Z1 PV It). Ill Pipe: 90 e,. 0 2. 703 PL 18. 00 Pf e,. Ill 21Z11 28. B 0. Ill 61Zt. e1 e,. ll) 121. 0 l 21Ll FTG PE 0. ILi 202 28. 8 0. 0 6121. e, 0. e, iz,. ,Z1,Z1t2.1 TL 18. 1210 PV e1. ll) Pipe: 91 ··-ILi. ILi 2. 71Zt3 PL 15. 0121 PF Qt. 0 202 28. 8 0. 0 60. 0 0. 0 0. 0 1212.1 FTG T PE 121. 121 30A 28. B 121. 0 6121. fl\ 0. 0 0. IZlfL\IZI TL 27. 00 PV ei. 1£'\ ~ ~ SPRINKLEF< SYSTEM HYDRi=tUL l C nNi4LYSIS Pa£1e 12 JOB TITLE: CAF<LSBAD HESEARCH CENTEF< -LOT 4J48 CALC #3 MEZZ FLR #1 PIPE DATA (cont' d) PlPE TAG Q(GPM> DI~~<IN) LENGTH PRESS. END ELEV. NOZ, PT DISC. VEL<FPS> Hl.-J < C) <FT) SUM. NODES <FT> 00 <PSI) <GPM) F .. . L • /FT <PSI> Pipe: 'j2 0. Ill 2. 7Q.'3 PL 21121. 121121 PF 12, .. e, 3121'4 28. 8 0.'0 60. 0 0. 12• e,. tZ1 121£1 FTG T PE 1. 2 3121 26.0 0.0 61.2 IZl.0 0. 0121121 TL 222. 0tZI PV 0. 121 Pipe: 93 -~~). Q,1 ·-· ..._. 203 PL --:.· ..., . 01l.l PF 121. e1 21213 28.8 0.0 60. 0 ll\. 1£1 0. ILi 120 FTG T PE 0. 121 31L1f4 28.8 0. Ill 6!l1. 0 121. ll.1 0. e101l.1 TL 13. 1210 PV IL). IZl Pipe: 94 'L'. Q1 2.21213 PL 16.00 PF QI. 1Z1 2e,4 28. B 0. ll'I (-,.1£'1. 2 0. QI 121. ,Zt 121l'.I FTG PE 121. 1£1 205 28.8 0. 12, 6121. 2 12.'I. 0 IZI. 1Z11Z1QI TL 16. Q.'IIZa PV 0. fl.1 Pipe: 95 121. 0 2.203 PL 16. f10 PF 0. Ill 205 28. 8 0. 0 60. 2 il.l. 0 0. 121 1212.'I FTG PE Ql. ILi 21Zl6 28. 8 0. IZl 6121. 2 0. 0 Ill. ll.lll'I~) TL 16. 00 f)V Ill. 0 Pipe: <:}6 II.). Q1 2. 21Zt3 PL 1.00 PF IL\. 121 21216 28. 8 0. 0 6121. 2 121. 121 0. 1£1 1212, FTG T PE 0. ~) 24{-) 28. 8 0. 0 60. 2 0. Q.1 ei. 1Z11Z11ll TL 11. 0121 PV 0. Ill Pipe: en fl. Ill i:~. 21£13 PL 16. 00 1=:iF QI. 0 207 28.8 0.0 60. 1 0. Q.) 0.0 120 FTG PE IL\. e, 208 28. B 0. 0 60. 1 1£1. QI e,. ~)00 TL 16. 00 PV ~). 121 Pipe: 98 0. ILl 2.203 PL 16. Q10 PF. 0. e, dM3 28. B 0.0 6t2l. 1 0. 0 e,. e, 12Q'I FTG PE 0. !Lt 2121 1:} 28. 8 0. 0 60. 1 0. 121 e,. euz,e, TL 1 €.,. tZIQ.'l PV tZl. e, Pipe: 99 -0. It) 2. 203 PL 1. 00 PF ei. l[,'i 21lV·) 28.8 0. 0 61Zt. 1 0. Ill IL\. IZt 121£) FTG T PE 0. e, 22n 28. 8 0. 0 6121. 1 0. (1 0. 0flllZI TL 11. 0Ql PV f1. It) Pipe: 1~10 31.. ':) Lt• 310 PL -4. 5121 PF 0. ILi l 26. l,Zl e,. e, 61. Lt 0. 0 e, .. -1 12,ZI FTG PE e,. e, 4 26.0 0. Qt bl. 4 0. tZt '21 .. tZ11Z1Q1 TL 1 •• 50 PV IL) .. ILi Pipe: 101 6 1t. 8 Lt• 31 Ill PL 12. 00 PF t21. 0 4 26.0 Q). QI 61. 4 0. e, 1. 4 12Q.) FTG PE tZ1. ,Zt 6 26. t2I 0. 0 61. i. e,. 0 0. ll.101 TL 12. 0Qt PV Ill. 121 Pipe: 11212 91. 8 't. 31 Ill PL 12. 121121 i=•F Ill .. ILi 6 26. 0 0. Q.1 61. i. 0. tZJ 2. 1 12~1 FTG PE 121. 1L1 B 26. tZI QI~ 0 61. "• e,. 0 0. e,e,3 TL 1 .-, a::.. 00 PV !l). e, Pipe: 103 131. 1.(.1 .L►• 310 PL 12. 1210 PF e,. 1 B 26. 0 0., Ii) 61. 4 e,. 0· ·::, ..._. \j 120 F ·1-G PE e, .. ti.) !IL'.l 26. 0 0. 0 61. 3 0. 0 ":'. e,0 1+ TL 12. ti11Z1 PV 121. 1 Pipe: 11214 16"•· 7 .l •• 31 e, PL 7. ';)2 PF 1Z1 .. 1 1 e, 26. 0 0. e, 61. 3 0. 0 3. 6 121t) FTG PE 121. t2l 12 26.0 0. 0 61. 3 0. 0 0. 1Z11Z17 TL 7. 'j2 PV Ill. l ,# SPRIN~<LEH SYSTEM HYDHhULIC ANALYSIS Page 13 J·□B TITLE: CAHLSBAD RESEARCH CENTER ·--LOT ~f48 ChLC ~f3 MEZZ FLI~ #1 PIPE DATA (cont, d) PIPE Ti=tG Q<GPM> DH~<IN) Ll::.NGTH Pf<ESS. END ELEV. NOZ. PT DISC. VEL<FPS> Hl--J < C) <FT) SUM. NODES <FT> (K) <PSI> <GPM> F. L. /FT (PSI> Pipe: 11215 1 C)8. 6 4. 310 PL 12.00 PF !Lt. 1 12 26.0 0. 121 61. 3 e1. 0 4. i~ 120 FTG ~ f··'E 0. ll'l --·---- 14 26.0 0. 0 61. 2 0. t2I 0.00<) TL 12. !i)0 PV 0. 1 Pipe: 11216 233. 1 L~ • 310 PL 7. fl'\0 PF fl). 1 14 26.0 0. 0 61. ·=-..... 0. 0 i;;.-..J • 1 120 FTG PE tZI. 121 1 1►A 26. ll.l 0.0 61. 1 ei. e, e,. 013 TL 7. 01£'\ PV ll,l. 2 Pipe: 107 ·-1 Tl. 2 4. 310 PL 5.00 PF 0. Qt ' 14(4 26.0 0. 0 61. 1 0. e, ~:;. ...., . <=) 12({) FTG PE ll.'l. ll.l 16 26.0 0.0 61. 1 0. 0 1t.l. 12108 TL 5. e,12, PV 0. 1 Pipe: 108 ~-1 1►2. -'• -'•. 31121 PL 1 ·=· '-. 01ll PF Q'l. 1 16 26. 0 0. 0 61. 1 tZl. e, -·, 1 120 FTG PE e,. Ill w. 18 26. 0 0. 0 61. 2 0. e, 0. etlll5 TL 12. 00 t-::iv It). 1 Pipe: 1 e,q ·--108. 1 4. 310 PL 12.00 PF 0. Ill 18 26. 0 0. 0 61. 2 0. 0 2. .L. 12121 FTG PE 0. I{.'\ 2121 26. 0 0.0 61. 2 0. 0 121. ,z,03 TL 12.00 PV 0. 0 Pipe: 11 Ill -71t. 1 4. 31121 PL 9. 54 PF 121. Qt 2e, 26.0 0. tZl 61. 2 0. e, 1. 6 lf:0 FTG PE 0. 1Z1 22 26. 0 0.0 61. 2 0. e, 0. e112,2 TL 9. 54 PV ei. fl1 Pipe: 111 ·--40. 6 .( .. 310 PL 16.tZIIZt PF •Zt • IZI ...... -·, a::.a::. 26. 0 0. ") 61. 2 Ill. Ill 121. ') 121l.l FTG PE 0. e, 24 26.0 121. 121 61.2 0.0 0. 1Z1t21t21 TL 16. tZ1Q1 PV 0. ,✓.) Pipe: 112 e,. e, 4. 310 PL Cj. 01l) PF 121. Qt 2l~ 26.0 0. IZt 61.2 e,. ll'l Q.'i. Q1 121l) FTG PE 12,. Q) 3121 26. 0 0. 0 61. 2 0. e, e,. 00e1 TL Cj. fll0 PV Ill. ll,1 Pipe: 113 --31. 8 6. 41Zt3 PL 12. 1210 PF tZt. Ill 3 26. 0 0. 0 63. 8 Qi. lll 0. 3 12121 FTG F1E Ill. 121 1:~-26. 0 0.,0 63. 8 0. iz,· Qi. Q11Z11Z1 TL 12.00 PV !Li. tZ1 ..J Pipe: 114 --6"•· B 6. i.e,3 PL 12. ll_lQI PF e,. 0 i:;.-26. IZl 0. IZI 63.8 tZI. !Li lli. 6 120 FTG PE 0. ILi ..J 1 26. 0 0. Ill 63. 8 0. 0 Ill. e1e,e1 TL 12. lllt21 PV 1£1. ,z, Pipe: 115 --~<) 1. 8 b. 41,i3 PL 12. 121121 PF 0. Q) 7 26. 0 0.0 63. B Ill. 121 1. QI 121l) FTG PE IZt. ~) l:) 26. 0 0.0 6 .. ;-w. 8 e,. tZI iz,. eie,e, TL 1 -::, I-. 00 PV Ill. ILi Pipe: 116 --131. e, 6. .t.e,3 PL 1 ·::, '-. lll!ll PF ~). IL• '-) 26.0 IZI. 0 f, :~. 8 e,. e, 1. '"" 12lli FTG ~IE e,. Ill 1 1 26. 0 0. 0 63. 8 ,~. 0 e,. eu,Zti TL 12. !li0 PV ,ZI. It) Pipe: 117 .. -164. 7 6. 41i'.13 PL 5.29 PF e,. 0 11 26. 0 0. 0 63. 8 ei. 0 1. 6 120 FTG T PE IZt. e, 31 26. Q) 121. 0 63. 9 0. 0 e,. it.lQtl TL 35. 29 PV 0. Q) i, ,, SPR I N~<LEF< SYSTEM HYDRAULIC ANt:'.\LYSI S Page 11~ JOB TITLE:: Cf~~<LSBAD RESEARCH CENTEH --LOT #48 CALC #3 MEZZ FLR #1 PIPE DATA (con_t'd) PIPE TAG Q(GPM> Dlt➔<IN> LENGTH PHESS. END ELEV. Naz,. PT DISC. VEL<FPS) Hl.-J ( C > (FT) SUM. NODES <FT> <K> <PSI> <GPM> F. L. /FT (PSI> Pipe:: 118 ··-41 QI. '+ 6. 402, PL 22. 75 PF e,. ~2 31 26. 0 0.~ 63. Cj 0. 0 ' 1 •• 1 120 FTG L PE e,. 2 TOH 25. 5 0. 0 64. 2 e,. 0 ll). 01215 TL 31. 75 PV 0. 1 Pipe: 119 -it H:). i. 6. itl2I3 PL 25. 00 PF eI. 1 TOH 25.5 0. 0 64.2 0. 0 4. 1 12121 FTG PE 10. 8 BOH 0.5 H. s. 75. 2 100. tZt e1. 005 · TL 25. IL'iZI PV 0. 1 Pipe: 120 ··-5H). 4 B.510 PL 10.00 ~•F 0. iz, BLlR 0.5 H. C.:· i:). 75. 2 100. 0 2. Cj 14QI FTG L Pl::. 1. a::· ..J U5 -3.0 0. 0 76.8 0. 0 0. IZlllH TL 21. 97 PV tZI. 1 Pipe: 121 -5H'.I. .Lt 7. 987 PL 260. 0121 PF e1. 6 U5 -3. 0 0.0 76.8 0. e, . .. ,. ..... 15121 FTG 7L PE ·=· 2 ..., . ~ a... • U4 2.0 0. 0 75. 2 it.1. 0 e,. e,02 TL 355. 20 r-•v 0. 1 Pipe: 122 FIXED P~"<ESSUHE LOSS DEVICE U3 2. 0 0. 121 80. 2 1.21. 0 ,::· ..J. QI psi, 51121. 4 gpm U4 2. 0 0. 0 75. 2 0. 0 Pipe: 123 -510. it 7.987 PL 12. 00 PF 0. 1 U3 2.0 0.0 80. 2 0. 0 ·7 ..., . 3 15121 FTG T2L PE i:.~. 2 u--, a::. -3.0 0. 0 82. a:;;· ..J Q). 0 0. Qlll)2 TL 84. 53 PV 0. 1 Pipe: 124 --511t). 4 1. i..)87 PL 4 IL) • it'l 121 PF "' · 2 U2 -3. 0 0. 0 a·=· L-. c:· ..J 0. e, ,_J. 3 151l.l FTG TG PE 121. Q1 Lil -3.0 SRCE a2. 7 (N/f~) Qt,. "2I1Zt2 TL EFL 87 PV 0. 1 Pipe: 1 ···,c:· i:::....J --40. 6 b. it03 PL 12. 0121 p~--.:-e,. 0 29 26.0 0. ll'l f.:: .. ~ "\ ...... 8 121. 0 IL\. -'t 12121 FTG PE lZI. QI 23 26. 121 0. e, ,. ~-~ t_-....!,. 8 t;:). QI ll.'l. Q1t211t.) TL 12. ll.10 PV ll.l. e, Pipe: 126 .... "l .l~. 1 b. .L~Qt3 PL 9. 54 PF 0. Ii.) 23 26. 121 0.0 ,. --·•. 8 e,. QI 121. "/ 12121 FTG PE tL1. e, t_"\ ~. 21 26.0 0. Qt 63. 8 Q\. IZt •Zi. IZIIZtlll TL <=.). 54 PV 0 .. lit Pipe: 127 -1 eia .. 1 6 .. .t'.tl213 PL 12. llll21 PF ll.1. 121 21 2G. 121 12,. 0 63. fi 1Z1. tZl l.. 1 12121 FTG PE Ill. ILi 1 '.) 26. IL'l 0. 121 63. B e,. e, Ill. !Llfl.11{.'l TL 12. 0e, PV Qi. Q'l Pipe: 128 ··-l '-1-2. Lt 6.403 PL 12. 00 i:::•F 0. Ill 19 26. 0 0 I 0 63. 8 ea. e, 1. .Lt 12~) FTG PE e, . 121 17 26.0 0. 121 63. 8 0. 121 tZI. IL•'H TL 12. IZH2t PV ILl. ILi Pipe: 129 --1 Tl. 2 6. it~.13 PL i 2. fllll'l PF 121. ~1 17 26. QI 0. 0 63.8 e,. e,. 1. 8 121L) FTG PE IL'l. ILi 15 26'. 0 0.' e, ,. •··. b ..!, • 8 Q.l. tZI 0. 12101 TL 12. Ql,Zl PV Ill. e, Pipe: 130 .... 211. 8 6. 4It)3 PL 12. 00 PF--121. If) 15 26. 0 0. 0 63. 8 Ii). 121 2. 1 12121 FTG PE e,. 121 13 26. 121 0. 121 63. 8 Q). 0 1Z1. 1Z1tZ12 TL 12.00 PV 0. Ill Page 15 JOB TITLE: CARLSBAD RESEARCH CENTER -LOT #48 CALC #3 MEZZ FLR #1 PIPE DATA (cont'd> PIPE TAG END NODES ELEV. <FT> 13 31 31211 3iL12 31213 5tZi 31214 31215 Pip~: Pipe: Pipe: Pipe: Pipe: 131 26. IZl 26.0 132 11.2 11. 2 133 11. 2 11. 2 134 11.2 10.6 135 11. 2 11. 2 Pipe: 136 31Lt5 11. 2 306 11.2 Pipe: 137 31Ztb 11. 2 51 1 IL\. 6 Pipe: 138 3(L.\7 11. 5 3tZaB 11. 5 Pipe: 139 3Q'.18 11. 5 11. 5 Pipe: 140 309 11.5 ::; 1 e, 11. 5 Pipe: l'tl 31 Ill 11 • 5 ~2 1e,.6 Pipe: 11t2 311 11. 3 ::,3 1121. 6 Pipe: 143 312 11. 3 54 10.6 NOZ. < K) 0. QI 0. 121 a::-t:-'-'. '-' 5.5 5.5 c.~ c:.~ ,_,. ,.J C.7 i::: '-' • ...J 5.5 5,5 5.5 5.5 c:.~ L-::-.._J • ..J ' r.:.~ i::.~ ..J ... J c:· c;· ..J • ..J 0. 0 •=-c::-...J. ,.J 5.5 t21. IZl Q(GPM> DIA<IN> LENGTH PHESS. PT DISC. VEL <FPS) Hl--J (C) <FT> SUM. <PSI> <PSI) <GPM> F.L./FT 63.8 63.9 25.9 27.8 27.B 29.6 29.6 32.8 27.2 27.7 27.7 29.6 22.3 2.1.t. 8 26.~ 28.2 28.2 33.2 33.9 31 • .Lt 34.7 28.0 29.0 29.0 2C). '-) 28.7 29.0 2. 1.~ --28. 121 t). it --86. 9 12.5 ·-28. 7 6.403 PL 12Q.1 FTG ,zi. l211Z12 TL 1. 10-''.t PL 120 FTG e1. 1ag TL 1. 452 PL 120 FTG QI. 1Bt5 TL 1.687 PL 121Z1 FTG t21. 195 TL 1. L~52 PL 12fl) FTG 2.62 T 32.62 10.00 10.00 3.00 ET 15.00 10. e,iz1 pi:= PE PV PF PE PV PF PE PV PF PE PV 0.052 TL 10.00 PV -57.7 1.452 PL 10.00 ~F 29.0 11.2 120 FTG PE 29.9 0. 189 TL 10.00 PV -87.G 1.687 PL 3.00 PF 2 9 • 9 1 2 • 6 1 2 ll.1 FT G ET PE 0.0 0. 1qa TL 15.00 PV -26.0 1. 104 PL 13.00 PF 26.~ 8.7 120 FTG E PE 27.4 0. 165 TL 15.00 PV -53.4 1.452 PL 10.00 PF 27.4 10.3 120 FTG PE --81 • l 28.3 11.7 29.2 --3~) .. i~ 312,. 4 1,z,. 2 0. 121 -•-3121. a 30. 8 H) • .:, e,. 0 Q). 164 TL ltZt. e,e, PV 1.687 PL 10.00 PF 120 FrG PE iiJ. 174 TL 1121. t21t21 PV 1.687 PL 3.00 PF 120 FTG El PE 0.306 TL 15.00 PV 1. 104 PL 3.25 PF 120 FTG 2T PE tZI. f:2 i TL 13. 25 j:•V 1. 104 PL 3.25 PF 120 FTG 2T PE 0.226 TL 13.25 PV QI. 1 ll1. IZt 0. Ill 1.9 0. Q) 0.6 1 • •.:.) 0. Ill lb. B c.9 12, • .::, 1. lli Q). 5 it). 0 0. i::'. 1. C.) 1Z1 .. IL) e,. B 1. 1 2.5 0. t21 e,. 5 1.6 ll.1. e1 Q\. ·1 1. '/ IL'-e, e,. <:J 4.b 1L1 • .S:t 1. 1 i.:~. 9 !Li. :~ e,. 7 3. IZI e1. 3 e,. 1 SPfHN~\LEH SYSTEM HYDf<hUL IC nNHL YS IS Page 16 JOB TITLE: CARLSBAD RESEARCH CENTER -LOT #48 CALC #3 MEZZ FLR #1 PIPE DATA (cont'd) PIPE TAG G! <GPM) DIA<IN) LENGTH END ELEV. NOZ. PT DISC. VEL<FPS) HW<C) <FT> NODES <FT) < K > <PSI) <GPM> r· . L • /FT Pipe: 144 -<:,l. 7 1. 4~32 PL 10. IZlfl.) 313 11. 2 5.6 33. 2 31. 7 6. 1 12121 FTG 31 La, 11. -:::, '-5. 5 33. i..) 32. lb 0. tZ•63 TL 10. 0121 Pipe: 145 r -··. ···, 1. 687 PL .. :;. flllZI --t, ~-I ..., . 314 11. 2 c.~ a:;-·-·\ --,. 9 32. Q) •:). 1 121L) FTG ET ..J. "J ...,..., . 55 1121. 6 0. 0 -,c: ~..J. 8 e,. 0 e,. 11121 TL 1c::-..;. 00 Pipe: 146 ·--BG. ,::., -~-...,. 314 PL 11. 512• 51ZI 10. 6 fl). 0 32. 8 !l'l. 1.21 ... ;;-..., . 2 12ii.'l FTG 51 10. 6 0. 121 32. ':) 0. 1£) fl.). IZtlZI} TL 11. 51L'l Pipe: 147 --17 4. ~--31.L► PL 11. 75 ,J ..., . 51 10. 6 0. 0 32. 9 e1. 0 6. i;;: 120 FTG ..J .:.::· .--. ..JC 1121. 6 0. 0 ---·-.. ~~-2 Ill. 0 121. 12126 TL 11. -··•c: I ..J Pipe: l 1t8 --285. 4 3. 314 PL 10. 50 i;;:·.···, ..JC 10. 6 0. 0 .... .._ --. ~~-2 121. 0 10. 6 120 FTG c· ......... .j.:, 10. 6 0.,0 H~\. •·~ ...,..., . ':) IZt. e1 · IZI. ~)66 TL 10. 5'21 Pipe: 1.l►':J -··315. 8 ~~. ...., . 314 PL 10. ll,e, c·· --.. .j~ 10. 6 ei. 0 ··-.-..,. ~~-9 Q'l. 0 11. 7 12ll' FTG· 54 10. 6 0. 0 3.Lt. 7 121. Ill 0. IL17Cj TL 1121. 0121 Pipe: 15121 --3Ltb • 6 ··.,:· ...., . 31 lt PL 11. 75 54 1 e,. 6 ei. Ill 3 1t. ·1 ei. e, 12. C) 120 FTG 5 5 10. 6 0. 0 35. 8 e,. QI e,. Qll.)Lt TL 11. 75 Pipe: 151 --.ld ~). 4 3. 311t PL B1t.l. 83 ~1...-..J..J H). 6 121. t21 35. 8 0. Ill 15. ... A'-,.., 120 FTG T 56 1 Ill. 6 0. e, L►B. 1 e,. QI 0. 128 TL 95. 83 Pipe : 152 ---ld e•. Lt ,.J. 31 Lj. PL 65. 67 ~b 1121. 6 0. QI 48. 1 QI. ,Zl 15. ..:> 12!li FTG T2L '5 1 1 Q). 6 0. Ill 59. 1 tZI. !Ll 1Z1. 128 TL ') 1Zt. 67 Pipe: 1 5 3 -.lt1e,. .i'.t .:, . 31 .Lt PL 32. 5121 5 7 10. 6 0. 0 5'}. 7 e1. e, 1 t:i. -;-,.., 120 1---TG 2T 14n 26. e, 0. QI 61. 1 QI. 0 e,. 128 TL 6i:::. 50 NOTES: ( 1) Calculations , performed by the ~-1~=,ss .:::· i:::· t2t computer were ..J • ..J. und e ·, ... license no. EF)26J521 granted by Hf<S Systems, Inc-. 21'33 f<anchwood Dr. ' N. E . /-)t 1 ant c.1, Gt4 3~1!};45 (2) The system has been balanced to provide an average i m b a 1 an c-e at e a c· h n o d e o f e1. Q1Qi 1 g pm c.i n d c·, mi::\>< i m um imbalance at any node of 0. 126 gpm. PRESS. SUM. <PSI) PF Q). PE 0. PV It). PF 1. PE 0. PV Ill. PF e,. PE Ill. PV 0. PF 0. PE 0. PV It). PF 12). ~:iE 121. PV 0 .. PF 121. PE Q). PV !Li. PF 1. PE tL1. PV 1. Pf-1 ·=· ...... PE ei. PV 1. PF. 1 1. PE 121. PV 1. PF 8. PE 6. p1.y1 1. program b e, 3 6 3 6 1 ll'l 1 3 QI 3 7 121 8 8 Ill Cj 1 0 1 3 IZt 6 6 e, 6 Ill ·1 6 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 17 JOB TITLE: CARLSBAD RESEARCH CENTER -LOT #48 CALC #3 MEZZ FLR #1 ( 3) Velocity pressures are printed for not used in balancing the system. any pipe is 15.9 ft/sec. information only, and are Maximum water velocity in (4) PIPE F ITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: F MATERIAL: DYNAF--L Hl--JC: 1 i.~lt) Diameter Equivalent Fitting Lengths in Feet (in) E r L C B G A Ell Tee LNGELL CH~<VLV BFYVLV Gt=lT VLV ALIYJCH~< 2. 21213 5. IZJIZI 1121. li)0 3. 00· 11. IZl!i) 6. e,e, 1.00 1121. 1L\aZ1 2.703 6.00 12.00 .l~. Q)ll.1 1 .L~. ~)0 7.00 1.00 10.00 3.314 7.00 15. 1Z11Z1 5.00 16. li)lll 10.0Q.l 1. ,210 13. 1210 4.310 10. 0121 212,. 0121 6.00 22. 0121 12. 0e, 4.00 20.00 6. 41Zt3 14.00 30. t2tlll <). lltlZI 32. 1Z10 10. 00..l 3.00 28. tZIIZl PAGE: G MATEf<lf4L: BLT Hl--JC: 12'21 Diameter Equivalent Fitting Lengths in Feet (in> E T L C B G A Ell Tee LNGELL CHI-\ VLV BFYVLV GATVLV ALMCHh 1. 104 2.00 5. 0~) 2. IZll21 5. ll'llZI 6.00 1. 0fl.l 1121. ")~) 1. 4 ~2 3. Q'.10 6. 01l) 2. tZ1Q1 7. tlllb 6. tZ11Zt 1. IZlii.l 10. tZllZI 1. 68-/ 4. 00 8. 0121 2 .00 ') • 1,Jl2l 6. 0!l) 1. ~10 1121. 0121 D DPVLV 10. \lllll 1 ~). Ql~l 10. l{)lLI 10. ~)0 1 ·:,. 12'.llll D DPVLV 1121. tZIIZl 1 tZI. IZtll) 1 fl.). ~11Zt , • SPHIN~<LEF< SYSTEM HYDH(lUL 1 C rlNi4L YSl S Paye 18 JOB TITLE: CARLSBAD RESEARCH CENTER -LOT #48 CALC #3 MEZZ FLR #1 WATER SUPPLY CURVE p l-< E - s s u f< E r· ·-,. .. .:> I 120*\\\\\\\\\\\\\\\\\\\ ' 0 \\\\\\\\\\\\\\\\\\\\ 1 llZt+ ' I 11Z1tZ1+ I <)tZt+ I 80+ I I 7 1ZI+ I I I bli'.1+ 5 !LI+ 3 1Lt+ I ' X I========·===================== 21Z1+ llZt+ LEGEND X -Required Water S upply 62.69 psi@ 910.4 gpm I I 0 = Available Water Supply 118.09 psi@ g10.4 gpm 11 II * <-115.0 psi@ 1530 gpm Flow Test Point Qt ·i--t--·-·-1--·-·---·t--··----·i--1 ----·-·----t-···--·· ·-·---·--·-·-1-···--·-···--·-..... ···• ---··· -1--·-····· ···--·-···-.... -·-···I·····--·--·---·----------· ·t-·--·--·-· --··--·-··---·--···-··-··-I·· 400 600 800 1000 1200 1400 1600 1800 2000 FLOl..J ( GPM) · HYDRAULIC DESIGN INFOAMATIQN SHEET NAME LOCATION CAt2--Lffl ~a~ ~ · DATE '-.::f lA...JE "2:. '2..,\'9q9 LQr~ 7 Ru1110'2..:fotz..D · t2D c~~-1½-D CA · · • 1 1 • YSTE ~ NO f2.oDf Sf't2:< .J(C..(J:;-a__s BUI LOI NO CONTRACTOR '.Cof<.b)al-$:@t.JtS 0!'>)5t01-U.c.uo·~ OONTRACT NO 44-8 3" CALCULATED BY----""':~---------------------DRA~INO NQ _______ _ '-A . ·. ~al-•• CONSTRUCTION: '/" ·coMBUSTIBLE l I NON-COMBUSTIBLE CEILING HEIGtlT __ :.J. ______ FT. OCCUPANCY ________________________________ M_~_)'_._-__ _ z C) vi w .a ~ UJ t; r l/J ) NFPA lJ: ) NF.PA :ZJ1 l ) LT. H~Z.~ . --~:( . ) NFPA :zj1c: ORD. HAZ. OP • .. I 1 I l , l 1_.3 f)(J EX. HAZ. FIGURE _______ _ CURV ______ _ ) OTHER (S~lfy) ______________ _;.._ ___________________ _ ) SPEC.IF IC Al)LINO -----------------MADE ev _______ £lA.TE _____ _ AREA OF SPR.INKLER OPERATION-----~~"1""'11:--r=, SYSTEM TYPE DENSITY . -· ... . AREA PER SPnlt-Hd.ER HOSE ALLOWANCE GPMi INSIDE HQ$1: ALLOWANCE GPM: OUTSIDE __ :zj_z::> ____ D ___ 6 __ ~_?'Y\ __ HACK SPRINt<'--ER ALLOWANCE ( X) WET ( J DAY ( · J DELUGE ( ) PRE-ACTION --~--;.....;.,_;......;.:·. _-SPRINKLER OR NOZZLE MAKE \/ l)$1 .J'2:·? 11 MODEL · l'-1 , !!:Lo • SIZE · · ?L8 K-FACTOR I [ .. 5 TEMPERATURE RATING . :2 f>b "F CALCULATION SUMMARY GPM · neaumeo ___ l_~-----~---Pst REau1Reo _-, __ ~_. _b __ AT 01-se oF RISER !;C" FACTOR USED: OVERHEAD' \ '2.o UNDEROROUND Is p :j 0... 0... :) V) C( w >-c( ~ w CJ c( a: 0 t;; ~ 0 0 :E ~ 0 u WATER Fl.OW TEST rUMP OATA ANK 0 DATE & 1'\~E MA'{ I. 1998 RATED CAPACITY -----CAPAC STATIC PSI \,ZQ :$ I, Res, DUAL PSI ____ \;....;l .... s-___,e_~s .... , __ GPM FLOWING __ l_$_3 __ o_~_N\. __ ELEVATION AT PSI ELEVATION PAOOFFLQW _______ GPM LOCA.;;·ON ___ ··-_-____ .,_~~Tid:6{l.fu~.:::;.;..·~· :;.:.ffi......aa::::::__..:...0_0_. ---------------- '"AF S ·c..V•AI o ./'~D SOURCE · OF l~FOAMATION ____ .,&. _ _,;;_i_.___==-.-, __,,;::~□~..:.lA.1...:.....-"-.--=~::::;;;._:......a_~-------------- COMMOOITY ____________ cL.Ass ________ LOCATION---~~---- STORAOE Hl;IOHT AREA AISLE WIDTH,~----------.. t .,t .. . . .... STORAGE METHOD: SOLID PILED " PALLETIZED ACK _______ % J SINGLE ROW J DOUBLE. ROW ) MUL TIPLI! ROW ) _CONVENTIONAL PALLET I SLAVE PALLET I -------TRANSVE~se __ _ ) SOLID SHELVING ) OPEN I ENCAPSULA.TED _ 1 . I NON·• 'l ENCAPSULATED Cl.eARANCe FROM TO~ Of STORAGE TO CEILINO ________ fT,---------IN. l~ONTAL BARRIERS PROVIDED ________________________ _ SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 , Da' e: 11/01/91 835ROOF JOB TITLE: CARLSBAD RESEARCH/ROOF CALC .45/3000 06/22/99 WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) 1 ... 108.0 'to3.5 1530.0 100.7 1993.6 91. 2 ~~eef ,~ to¼ ~ luStH~1- AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 1993.6 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 500.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 1493.6 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 -3.0 SOURCE 91. 2 1493.6 2 -3.0 89.5 --- 3 -3.0 ----88.9 --- 4 -3.0 78.9 --- 5 -3.0 ----75.4 --- 6 0.5 ----73.6 --- 7 26.5 60.2 --- 8 26.5 ----56.8 --- 9 26.5 56.8 --- 10 26.5 56.8 --- 11 26.5 ----56.6 --- 12 26.5 56.1 --- 13 26.5 ----55.7 --- 14 26.5 55.4 --- 15 26.5 ----55.0 --- 16 26.5 54.8 --- 17 26.5 54.7 --- 18 26.5 54.6 --- 19 26.5 54.6 --- 20 26.5 54.5 --- 21 26.5 ----45.2 --- 22 26.5 45.2 --- 23 26.5 ----45.0 --- 24 26.5 44.8 --- 25 26.5 44.5 --- 26 26.5 44.0 --- 27 26.5 ----42.2 --- 28 26.5 41. 8 --- 29 26.5 ----41. 6 --- 30 26.5 41. 6 --- 31 26.5 ----41. 7 --- 32 26.5 41. 8 --- 33 26.5 ----54.5 --- 34 28.0 41. 2 --- SPRINKLER SYSTEM HYDRAULIC ANALYSIS •t JOB TITLE: CARLSBAD RESEARCH/ROOF CALC .45/3000 06/22/99 ~ODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE 35 36 37 38 39 40 41 42 301 302 303 304 305 306 307 308 309 310 311 312 313 314 315 316 201 202 203 204 205 206 207 208 209 210 211 212 213 214 215 216 217 218 219 220 221 222 223 224 225 226 227 228 229 230 (FT) (PSI) (GPM) 28.0 28.0 11. 0 11. 0 11. 0 11. 0 11. 0 11. 0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 28.0 K=ll.50 K=ll.50 K=ll.50 K=ll.50 K=ll.50 K=ll.50 K=ll.50 K=ll.50 K=ll.50 K=ll.50 K=ll.50 K=ll.50 K=ll.50 K=ll. 50 K=ll.50 K=ll.50 K=ll.50 K=ll.50 K=ll.50 K=ll.50 K=ll.50 K=ll.50 K=ll.50 K=ll.50 K=ll.50 K=ll.50 K=ll.50 K=ll.50 K=ll.50 K=ll.50 41. 0 41. 0 48.4 48.4 48.4 48.4 48.4 48.4 46.1 45.8 45.5 45.2 44.9 44.6 46.4 46.0 45.7 45.3 45.0 44.6 45.8 45.5 45.2 44.8 16.2 15.0 14.4 14.1 14.1 14.1 14.4 15.0 16.1 16.2 15.0 14.4 14.2 14.1 14.1 14.4 15.0 16.1 16.2 15.1 14.5 14.2 . 14. 2 14.2 14.5 15.1 16.2 27.3 26.7 26.5 46.2 44.5 43.6 43.2 43.2 43.2 43.6 44.5 46.2 46.2 44.5 43.6 43.3 43.2 43.3 43.6 44.5 46.2 46.3 44.6 I 43 O 7 43.4 43.3 43.4 43.7 44.6 46.3 60.0 59.4 59.2 Page 2 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 . \. JOB TITLE: CARLSBAD RESEARCH/ROOF CALC .45/3000 06/22/99 mQE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 231 28.0 K=ll.50 26.5 59.2 232 28.0 K=ll.50 26.8 59.5 101 11. 0 ----48.4 --- 102 11. 0 48.4 --- 103 11. 0 ----48.4 --- 104 11. 0 ----48.4 --- 105 11. 0 ----48.4 --- 106 11.0 48.4 --- 107 11. 0 ----48.4 --- 108 11. 0 48.4 --- 109 11. 0 ----48.4 --- 110 11. 0 48.4 --- 111 11. 0 ----48.4 --- 112 11. 0 48.4 --- 113 11. 0 ----48.4 --- 114 11. 0 ----48.4 --- 115 11. 0 ----48.4 --- 116 11. 0 48.4 --- 117 11. 0 ----48.4 --- SfRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 •\. JOB TITLE: CARLSBAD RESEARCH/ROOF CALC .45/3000 06/22/99 PIPE DATA PIPE TAG Q(GPM) DIA( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) ( J() (PSI) (GPM) F.L./FT (PSI) Pipe: 1 1493.6 7.987 PL 80.00 PF 1. 7 1 -3.0 SRCE 91. 2 (N/A) 9.6 150 FTG 52.50 PE 0.0 2 -3.0 o.o 89.5 0.0 0.013 TL 132.50 PV 0.6 Pipe: 2 1493.6 7.987 PL 5.00 PF 0.6 2 -3.0 o.o 89.5 0.0 9.6 150 FTG 39.30 PE 0.0 3 -3.0 o.o 88.9 0.0 0.013 TL 44.30 PV 0.6 Pipe: 3 FIXED PRESSURE LOSS DEVICE 3 -3.0 o.o 88.9 0.0 10.0 psi, 1493.6 gpm 4 -3.0 o.o 78.9 0.0 Pipe: 4 1493.6 7.987 PL 233.00 PF 3.5 4 -3.0 0.0 78.9 0.0 9.6 150 FTG 39.30 PE 0.0 5 -3.0 o.o 75.4 0.0 0.013 TL 272.30 PV 0.6 Pipe: 5 1493.6 8.510 PL 8.00 PF 0.3 5 -3.0 o.o 75.4 0.0 8.4 140 FTG 17.30 PE 1. 5 6 0.5 o.o 73.6 0.0 0.011 TL 25.30 PV 0.5 Pipe-: 6 1493.6 6.403 PL 26.50 PF 2.1 6 0.5 o.o 73.6 0.0 14.9 120 FTG L PE 11. 3 7 26.5 o.o 60.2 0.0 0.057 TL 37.80 PV 1. 5 Pipe: 7 1493.6 6.403 PL 22.00 PF 3.4 7 26.5 o.o 60.2 0.0 14.9 120 FTG T PE 0.0 10 26.5 p.o 56.8 0.0 0.057 TL 59.70 PV 1. 5 Pipe: 8 -71.3 6.403 PL 12.00 PF 0.0 8 26.5 0.0 56.8 0.0 0.7 120 FTG PE 0.0 9 26.5 o.o 56.8 0.0 0.000 TL 12.00 PV 0.0 Pipe: 9 -142.8 6.403 PL 6.50 PF 0.0 9 26.5 0.0 56.8 0.0 1. 4 120 FTG T PE 0.0 10 26.5 0.0 56.8 0.0 0.001 TL 44.20 PV 0.0 Pipe: 10 1279.3 6.403 PL 5.50 PF 0.2 10 26.5 0.0 56.8 0.0 12.7 120 FTG PE 0.0 11 26.5 0.0 56.6 0.0 0.043 TL 5.50 PV 1.1 Pipe: 11 1208.2 6.403 PL 12.00 PF 0.5 11 26.5 o.o 56.6 0.0 12.0 120 FTG PE 0.0 12 26.5 0.0 56.1 0.0 0.038 TL 12.00 PV 1.0 Pipe: 12 1137.8 6.403 PL 12.00 PF 0.4 12 26.5 0.0 56.1 0.0 11. 3 120 FTG PE 0.0 13 26.5 o.o 55.7 0.0 0.034 TL 12.00 PV 0.9 Pipe: 13 1067.8 6.403 PL 12.00 PF 0.4 13 26.5 p.o 55.7 0.0 10.6 120 FTG PE 0.0 14 26.5 p.o 55.4 0.0 0.030 TL 12.00 PV 0.8 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 .\. JOB TITLE: CARLSBAD RESEARCH/ROOF CALC . 45/3000 06/22/99 . PIPE DATA (cont'd) PIPE TAG Q(GPM) DIA( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) Pipe: 14 997.5 6.403 PL 12.00 PF 0.3 14 26.5 0.0 55.4 0.0 9.9 120 FTG PE 0.0 15 26.5 0.0 55.0 0.0 0.027 TL 12.00 PV 0.7 Pipe: 15 830.4 6.403 PL 12.00 PF 0.2 15 26.5 0.0 55.0 0.0 8.3 120 FTG PE 0.0 16 26.5 0.0 54.8 0.0 0.019 TL 12.00 PV 0.5 Pipe: 16 630.3 6.403 PL 12.00 PF 0.1 16 26.5 0.0 54.8 0.0 6.3 120 FTG PE 0.0 17 26.5 0.0 54.7 0.0 0.011 TL 12.00 PV 0.3 Pipe: 17 430.4 6.403 PL 12.00 PF 0.1 17 26.5 0.0 54.7 0.0 4.3 120 FTG PE 0.0 18 26.5 0.0 54.6 0.0 0.006 TL 12.00 PV 0.1 Pipe: 18 230.6 6.403 PL 11. 25 PF 0.0 18 26.5 0.0 54.6 0.0 2.3 120 FTG PE 0.0 19 26.5 0.0 54.6 0.0 0.002 TL 11.25 PV 0.0 Pipe: 19 154.9 6.403 PL 36.00 PF 0.0 19 26.5 0.0 54.6 0.0 1. 5 120 FTG L PE 0.0 20 26.5 0.0 54.5 0.0 0.001 TL 47.30 PV 0.0 Pipe: 20 75.0 6.403 PL 12.00 PF 0.0 20 26.5 0.0 54.5 0.0 0.7 120 FTG PE 0.0 33 26.5 0.0 54.5 0.0 0.000 TL 12.00 PV 0.0 Pipe: 21 71. 3 4.328 PL 12.00 PF 0.0 21 26.5 0.0 45.2 0.0 1. 6 120 FTG PE 0.0 22 26.5 0.0 45.2 0.0 0.001 TL 12.00 PV 0.0 Pipe: 22 214.3 4.328 PL 12.00 PF 0.1 22 26.5 0.0 45.2 0.0 4.7 120 FTG PE 0.0 23 26.5 0.0 45.0 0.0 0.011 TL 12.00 PV 0.1 Pipe: 23 285.4 4.328 PL 12.00 PF 0.2 23 26.5 0.0 45.0 0.0 6.2 120 FTG PE 0.0 24 26.5 0.0 44.8 0.0 0.018 TL 12.00 PV 0.3 Pipe: 24 355.8 4.328 PL 12.00 PF 0.3 24 26.5 0.0 44.8 0.0 7.8 120 FTG PE 0.0 25 26.5 0.0 44.5 0.0 0.027 TL 12.00 PV 0.4 Pipe: 25 425.8 4.328 PL 12.00 PF 0.4 25 26.5 0.0 44.5 0.0 9.3 120 FTG PE 0.0 26 26.5 --0. 0 44.0 0.0 0.037 TL 12.00 PV 0.6 Pipe: 26 496.1 4.328 PL 20.50 PF 1. 9 26 26.5 0.0 44.0 0.0 10.8 120 FTG 2L PE 0.0 27 26.5 0.0 42.2 0.0 0.050 TL 37.50 PV 0.8 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 ~ JOB TITLE: CARLSBAD RESEARCH/ROOF CALC .45/3000 06/22/99 PIPE DATA (cont'd) PIPE TAG Q(GPM) DIA( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) Pipe: 27 365.7 4.328 PL 12.00 PF 0.3 27 26.5 0.0 42.2 0.0 8.0 120 FTG PE 0.0 28 26.5 0.0 41. 8 0.0 0.028 TL 12.00 PV 0.4 Pipe: 28 166.4 4.328 PL 1.00 PF 0.2 28 26.5 0.0 41. 8 0.0 3.6 120 FTG T PE 0.6 35 28.0 0.0 41. 0 0.0 0.007 TL 29.50 PV 0.1 Pipe: 29 166.4 4.328 PL 11.00 PF 0.1 35 28.0 0.0 41. 0 0.0 3.6 120 FTG PE 0.6 29 26.5 0.0 41. 6 0.0 0.007 TL 11.00 PV 0.1 Pipe: 30 -32.1 4.328 PL 12.00 PF 0.0 29 26.5 0.0 41. 6 0.0 0.7 120 FTG PE 0.0 30 26.5 0.0 41. 6 0.0 0.000 TL 12.00 PV 0.0 Pipe: 31 -230.6 4.328 PL 11.25 PF 0.1 30 26.5 0.0 41. 6 0.0 5.0 120 FTG PE 0.0 31 26.5 0.0 41. 7 0.0 0.012 TL 11. 25 PV 0.2 Pipe: 32 -154.9 4.328 PL 14.00 PF 0.1 31 26.5 0.0 41. 7 0.0 3.4 120 FTG PE 0.0 32 26.5 0.0 41. 8 0.0 0.006 TL 14.00 PV 0.1 Pipe: 33 -75.0 4.328 PL 12.00 PF 0.0 32 26.5 0.0 41. 8 0.0 1. 6 120 FTG PE 0.6 34 28.0 0.0 41. 2 0.0 0.002 TL 12.00 PV 0.0 Pipe: 34 75.0 2.227 PL 156.00 PF 7.8 33 26.5 0.0 54.5 0.0 6.2 120 FTG 2T4L PE 0.6 301 28.0 0.0 46.1 0.0 0.038 TL 202.00 PV 0.3 Pipe: 35 75.0 2.227 PL 8.00 PF 0.3 301 28.0 0.0 46.1 0.0 6.2 120 FTG PE 0.0 302 28.0 0.0 45.8 0.0 0.038 TL 8.00 PV 0.3 Pipe: 36 75.0 2.227 PL 8.00 PF 0.3 302 28.0 0.0 45.8 0.0 6.2 120 FTG PE 0.0 303 28.0 0.0 45.5 0.0 0.038 TL 8.00 PV 0.3 Pipe: 37 75.0 2.227 PL 8.00 PF 0.3 303 28.0 0.0 45.5 0.0 6.2 120 FTG PE 0.0 304 28.0 o.o 45.2 0.0 0.038 TL 8.00 PV 0.3 Pipe: 38 75.0 2.227 PL 8.00 PF 0.3 304 28.0 0.0 45.2 0.0 6.2 120 FTG PE 0.0 305 28.0 0.0 44.9 0.0 0.038 TL 8.00 PV 0.3 Pipe: 39 75.0 2.227 PL 8.00 PF 0.3 305 28.0 0.0 44.9 0.0 6.2 120 FTG PE 0.0 306 28.0 0.0 44.6 0.0 0.038 TL 8.00 PV 0.3 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 \.. JOB TITLE: CARLSBAD RESEARCH/ROOF CALC .45/3000 06/22/99 PIPE DATA (cont'd) PIPE TAG Q(GPM) DIA( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) Pipe: 40 75.0 2.227 PL 52.00 PF 3.4 306 28.0 o.o 44.6 0.0 6.2 120 FTG 2T2L PE 0.0 34 28.0 o.o 41. 2 0.0 0.038 TL 89.40 PV 0.3 Pipe: 41 79.9 2.227 PL 156.00 PF 7.5 20 26.5 0.0 54.5 0.0 6.6 120 FTG TL PE 0.6 307 28.0 Q.0 46.4 0.0 0.043 TL 174. 70 PV 0.3 Pipe: 42 79.9 2.227 PL 8.00 PF 0.3 307 28.0 0.0 46.4 0.0 6.6 120 FTG PE 0.0 308 28.0 0.0 46.0 0.0 0.043 TL 8.00 PV 0.3 Pipe: 43 79.9 2.227 PL 8.00 PF 0.3 308 28.0 Q.0 46.0 0.0 6.6 120 FTG PE 0.0 309 28.0 0.0 45.7 0.0 0.043 TL 8.00 PV 0.3 Pipe: 44 79.9 2.227 PL 8.00 PF 0.3 309 28.0 0.0 45.7 0.0 6.6 120 FTG PE 0.0 310 28.0 Q.0 45.3 0.0 0.043 TL 8.00 PV 0.3 Pipe: 45 79.9 2.227 PL 8.00 PF 0.3 310 28.0 0.0 45.3 0.0 6.6 120 FTG PE 0.0 311 28.0 0.0 45.0 0.0 0.043 TL 8.00 PV 0.3 Pipe: 46 79.9 2.227 PL 8.00 PF 0.3 311 28.0 0.0 45.0 0.0 6.6 120 FTG PE 0.0 312 28.0 0.0 44.6 0.0 0.043 TL 8.00 PV 0.3 Pipe: 47 79.9 2.227 PL 52.00 PF 3.5 312 28.0 0.0 44.6 0.0 6.6 120 FTG 2T PE 0.6 32 26.5 0.0 41. 8 0.0 0.043 TL 80.80 PV 0.3 Pipe: 48 75.7 2.227 PL 180.00 PF 8.1 19 26.5 0.0 54.6 0.0 6.2 120 FTG 2T PE 0.6 313 28.0 0.0 45.8 0.0 0.039 TL 208.80 PV 0.3 Pipe: 49 75.7 2.227 PL 8.00 PF 0.3 313 28.0 0.0 45.8 0.0 6.2 120 FTG PE 0.0 314 28.0 0.0 45.5 0.0 0.039 TL 8.00 PV 0.3 Pipe: 50 75.7 2.227 PL 8.00 PF 0.3 314 28.0 0.0 45.5 0.0 6.2 120 FTG PE 0.0 315 28.0 0.0 45.2 0.0 0.039 TL 8.00 PV 0.3 Pipe: 51 75.7 2.227 PL 8.00 PF 0.3 315 28.0 0.0 45.2 0.0 6.2 120 FTG PE 0.0 316 28.0 0.0 44.8 0.0 0.039 TL 8.00 PV 0.3 Pipe: 52 75.7 2.227 PL 68.00 PF 3.8 316 28.0 0.0 44.8 0.0 6.2 120 FTG 2T PE 0.6 31 26.5 0.0 41. 7 0.0 0.039 TL 96.80 PV 0.3 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 \. " JOB TITLE: CARLSBAD RESEARCH/ROOF CALC .45/3000 06/22/99 PIPE DATA (cont'd) PIPE TAG Q(GPM) DIA( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) Pipe: 53 199.8 2.227 PL 132.00 PF 37.8 18 26.5 0.0 54.6 0.0 16.5 120 FTG 2T PE 0.6 201 28.0 11. 5 16.2 46.2 0.235 TL 160.80 PV 1.8 Pipe: 54 153.6 2.227 PL 8.00 PF 1. 2 201 28.0 11. 5 16.2 46.2 12.6 120 FTG PE 0.0 202 28.0 11. 5 15.0 44.5 0.144 TL 8.00 PV 1.1 Pipe: 55 109.0 2.227 PL 8.00 PF 0.6 202 28.0 11. 5 15.0 44.5 9.0 120 FTG PE 0.0 203 28.0 11. 5 14.4 43.6 0.077 TL 8.00 PV 0.5 Pipe: 56 65.4 2.227 PL 8.00 PF 0.2 203 28.0 11. 5 14.4 43.6 5.4 120 FTG PE 0.0 204 28.0 11. 5 14.1 43.2 0.030 TL 8.00 PV 0.2 Pipe: 57 22.2 2.227 PL 8.00 PF 0.0 204 28.0 11. 5 14.1 43.2 1. 8 120 FTG PE 0.0 205 28.0 11. 5 14.1 43.2 0.004 TL 8.00 PV 0.0 Pipe: 58 -21.0 2.227 PL 8.00 PF 0.0 205 28.0 11. 5 14.1 43.2 1. 7 120 FTG PE 0.0 206 28.0 11. 5 14.1 43.2 0.004 TL 8.00 PV 0.0 Pipe: 59 -64.3 2.227 PL 8.00 PF 0.2 206 28.0 11. 5 14.1 43.2 5.3 120 FTG PE 0.0 207 28.0 11. 5 14.4 43.6 0.029 TL 8.00 PV 0.2 Pipe: 60 -107.9 2.227 PL 8.00 PF 0.6 207 28.0 11. 5 14.4 43.6 8.9 120 FTG PE 0.0 208 28.0 11. 5 15.0 44.5 0.075 TL 8.00 PV 0.5 Pipe: 61 -152.4 2.227 PL 8.00 PF 1.1 208 28.0 11. 5 15.0 44.5 12.6 120 FTG PE 0.0 209 28.0 11. 5 16.1 46.2 0.142 TL 8.00 PV 1.1 Pipe: 62 -198.5 2.227 PL 78.00 PF 24.8 209 28.0 11. 5 16.1 46.2 16.4 120 FTG 2T PE 0.6 30 26.5 0.0 41. 6 0.0 0.232 TL 106.80 PV 1.8 Pipe: 63 199.9 2.227 PL 132.00 PF 37.9 17 26.5 0.0 54.7 0.0 16.5 120 FTG 2T PE 0.6 210 28.0 11. 5 16.2 46.2 0.235 TL 160.80 PV 1.8 Pipe: 64 153.7 2.227 PL 8.00 PF 1. 2 210 28.0 11. 5 16.2 46.2 12.7 120 FTG PE 0.0 211 28.0 11. 5 15.0 44.5 0.145 TL 8.00 PV 1.1 Pipe: 65 109.2 2.227 PL 8.00 PF 0.6 211 28.0 11. 5 15.0 44.5 9.0 120 FTG PE 0.0 212 28.0 11. 5 14.4 43.6 0.077 TL 8.00 PV 0.5 SPRINKLER SYSTEM HYDRAULIC AN~YSIS Page 9 'I. 1 JOB TITLE: CARLSBAp RESEARCH/ROOF CALC .45/3000 06/22/99 PIPE DATA (cont'd) PIPE TAG Q(GPM) DIA( IN) LENGTH PRESS. END ELEV. Npz. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) Pipe: 66 65.5 2.227 PL 8.00 PF 0.2 212 28.0 11. 5 14.4 43.6 5.4 120 FTG PE 0.0 213 28.0 11. 5 14.2 43.3 0.030 TL 8.00 PV 0.2 Pipe: 67 22.3 2.227 PL 8.00 PF 0.0 213 28.0 11. 5 14.2 43.3 1.8 120 FTG PE 0.0 214 28.0 11. 5 14.1 43.2 0.004 TL 8.00 PV 0.0 Pipe: 68 -20.9 2.227 PL 8.00 PF 0.0 214 28.0 11. 5 14.1 43.2 1. 7 120 FTG PE 0.0 215 28.0 11. 5 14.1 43.3 0.004 TL 8.00 PV 0.0 Pipe: 69 -64.2 2.227 PL 8.00 PF 0.2 215 28.0 11. 5 14.1 43.3 5.3 120 FTG PE 0.0 216 28.0 11. 5 14.4 43.6 0.029 TL 8.00 PV 0.2 Pipe: 70 -107.8 2.227 PL 8.00 PF 0.6 216 28.0 11. 5 14.4 43.6 8.9 120 FTG PE 0.0 217 28.0 11. 5 15.0 44.5 0.075 TL 8.00 PV 0.5 Pipe: 71 -152.3 2.227 PL 8.00 PF 1. 1 217 28.0 11. 5 15.0 44.5 12.5 120 FTG PE 0.0 218 28.0 11. 5 16.1 46.2 0.142 TL 8.00 PV 1.1 Pipe: 72 -198.5 2.227 PL 78.00 PF 24.8 218 28.0 11. 5 16.1 46.2 16.3 120 FTG 2T PE 0.6 29 26.5 o.o 41. 6 0.0 0.232 TL 106.80 PV 1. 8 Pipe: 73 200.1 2.227 PL 132.00 PF 37.9 16 26.5 o.o 54.8 0.0 16.5 120 FTG 2T PE 0.6 219 28.0 11. 5 16.2 46.3 0.236 TL 160.80 PV 1.8 Pipe: 74 153.8 2.227 PL 8.00 PF 1. 2 219 28.0 11. 5 16.2 46.3 12.7 120 FTG PE 0.0 220 28.0 11. 5 15.1 44.6 0.145 TL 8.00 PV 1.1 Pipe: 75 109.1 2.227 PL 8.00 PF 0.6 220 28.0 11. 5 15.1 44.6 9.0 120 FTG PE 0.0 221 28.0 11. 5 14.5 43.7 0.077 TL 8.00 PV 0.5 Pipe: 76 65.4 2.227 PL 8.00 PF 0.2 221 28.0 11. 5 14.5 43.7 5.4 120 FTG PE 0.0 222 28.0 11. 5 14.2 43.4 0.030 TL 8.00 PV 0.2 Pipe: 77 22.1 2.227 PL 8.00 PF 0.0 222 28.0 11. 5 14.2 43.4 1.8 120 FTG PE 0.0 223 28.0 11. 5 14.2 43.3 0.004 TL 8.00 PV 0.0 Pipe: 78 -21.3 2.227 PL 8.00 PF 0.0 223 28.0 11. 5 14.2 43.3 1. 8 120 FTG PE 0.0 224 28.0 11. 5 14.2 43.4 0.004 TL 8.00 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 . ,._ JOB TITLE: CARLSBAD RESEARCH/ROOF CALC .45/3000 06/22/99 PIPE DATA (cont'q) PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) Pipe: 79 -64.6 2.227 PL 8.00 PF 0.2 224 28.0 11. 5 14.2 43.4 5.3 120 FTG PE 0.0 225 28.0 11. 5 14.5 43.7 0.029 TL 8.00 PV 0.2 Pipe: 80 -108.3 2.227 PL 8.00 PF 0.6 225 28.0 11. 5 14.5 43.7 8.9 120 FTG PE 0.0 226 28.0 11. 5 15.1 44.6 0.076 TL 8.00 PV 0.5 Pipe: 81 -153.0 2.227 PL 8.00 PF 1.1 226 28.0 11. 5 15.1 44.6 12.6 120 FTG PE 0.0 227 28.0 11. 5 16.2 46.3 0.143 TL 8.00 PV 1.1 Pipe: 82 -199.3 2.227 PL 78.00 PF 25.0 227 28.0 11. 5 16.2 46.3 16.4 120 FTG 2T PE 0.6 28 26.5 0.0 41. 8 0.0 0.234 TL 106.80 PV 1. 8 Pipe: 83 167.0 2.227 PL 132.00 PF 27.1 15 26.5 0.0 55.0 0.0 13.8 120 FTG 2T PE 0.6 228 28.0 11. 5 27.3 60.0 0.169 TL 160.80 PV 1. 3 Pipe: 84 107.0 2.227 PL 8.00 PF 0.6 228 28.0 11. 5 27.3 60.0 8.8 120 FTG PE 0.0 229 28.0 11. 5 26.7 59.4 0.074 TL 8.00 PV 0.5 Pipe: 85 47.6 2.227 PL 8.00 PF 0.1 229 28.0 11. 5 26.7 59.4 3.9 120 FTG PE 0.0 230 28.0 11. 5 26.5 59.2 0.017 TL 8.00 PV 0.1 Pipe: 86 -11.6 2.227 PL 8.00 PF 0.0 230 28.0 11. 5 26.5 59.2 1.0 120 FTG PE 0.0 231 28.0 11. 5 26.5 59.2 0.001 TL 8.00 PV 0.0 Pipe: 87 -70.9 2.227 PL 8.00 PF 0.3 231 28.0 11. 5 26.5 59.2 5.8 120 FTG PE 0.0 232 28.0 11. 5 26.8 59.5 0.035 TL 8.00 PV 0.2 Pipe: 88 -130.4 2.227 PL 109.00 PF 14.7 232 28.0 11. 5 26.8 59.5 10.7 120 FTG 2T PE 0.6 27 26.5 0.0 42.2 0.0 0.107 TL 137.80 PV 0.8 Pipe: 89 70.3 2.227 PL 274.50 PF 11. 3 14 26.5 0.0 55.4 0.0 5.8 120 FTG 4T PE 0.0 26 26.5 0.0 44.0 0.0 0.034 TL 332.10 PV 0.2 Pipe: 90 70.0 2.227 PL 274.50 PF 11. 2 13 26.5 0.0 55.7 0.0 5.8 120 FTG 4T PE 0.0 25 26.5 0.0 44.5 0.0 0.034 TL 332.10 PV 0.2 Pipe: 91 70.3 2.227 PL 274.50 PF 11. 3 12 26.5 0.0 56.1 0.0 5.8 120 FTG 4T PE 0.0 24 26.5 0.0 44.8 0.0 0.034 TL 332.10 PV 0.2 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 . ,._ JOB TITLE: CARLSBAD RESEARCH/ROOF CALC .45/3000 06/22/99 PIPE DATA (cont'd) PIPE TAG Q(GPM) DIA( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) Pipe: 92 71. 2 2.227 PL 274.50 PF 11. 6 11 26.5 0.0 56.6 0.0 5.9 120 FTG 4T PE 0.0 23 26.5 0.0 45.0 0.0 0.035 TL 332.10 PV 0.2 C9 Pipe: 93 71. 5 2.227 PL 274.50 PF 11. 7 26.5 0.0 56.8 0.0 5.9 120 FTG 4T PE 0.0 2 26.5 0.0 45.2 0.0 0.035 TL 332.10 PV 0.2 Pipe: 94 71. 4 2.227 PL 274.50 PF 11. 6 9 26.5 0.0 56.8 0.0 5.9 120 FTG 4T PE 0.0 22 26.5 0.0 45.2 0.0 0.035 TL 332.10 PV 0.2 Pipe: 95 71. 3 2.227 PL 274.50 PF 11. 6 8 26.5 0.0 56.8 0.0 5.9 120 FTG 4T PE 0.0 21 26.5 0.0 45.2 0.0 0.035 TL 332.10 PV 0.2 Pipe: 96 0.0 3.356 PL 5.00 PF 0.0 35 28.0 0.0 41. 0 0.0 0.0 120 FTG L PE 0.0 36 28.0 0.0 41. 0 0.0 0.000 TL 12.70 PV 0.0 Pipe: 97 -0.1 3.356 PL 14.50 PF 0.0 36 28.0 0.0 41. 0 0.0 0.0 120 FTG L PE 7.4 37 11. 0 0.0 48.4 0.0 0.000 TL 22.20 PV 0.0 Pipe: 98 0.0 3.356 PL 212.00 PF 0.0 37 11.0 0.0 48.4 0.0 0.0 120 FTG 3L PE 0.0 38 11.0 0.0 48.4 0.0 0.000 TL 235.10 PV 0.0 Pipe: 99 0.0 3.356 PL 14.00 PF 0.0 38 11.0 0.0 48.4 0.0 0.0 120 FTG PE 0.0 39 11.0 0.0 48.4 0.0 0.000 TL 14.00 PV 0.0 Pipe: 100 0.0 3.356 PL 12.00 PF 0.0 39 11. 0 0.0 48.4 0.0 0.0 120 FTG PE 0.0 40 11.0 0.0 48.4 0.0 0.000 TL 12.00 PV 0.0 Pipe: 101 0.0 3.356 PL 10.00 PF 0.0 40 11. 0 0.0 48.4 0.0 0.0 120 FTG PE 0.0 41 11. 0 0.0 48.4 0.0 0.000 TL 10.00 PV 0.0 Pipe: 102 0.0 3.356 PL 8.50 PF 0.0 41 11. 0 0.0 48.4 0.0 0.0 120 FTG PE 0.0 42 11. 0 0.0 48.4 0.0 0.000 TL 8.50 PV 0.0 Pipe: 103 0.0 1.104 PL 8.75 PF 0.0 102 11.0 0.0 48.4 0.0 0.0 120 FTG PE 0.0 101 11.0 0.0 48.4 0.0 0.000 TL 8.75 PV 0.0 Pipe: 104 0.0 1.452 PL 7.75 PF 0.0 42 11. 0 0.0 48.4 0.0 0.0 120 FTG PE 0.0 102 11. 0 0.0 48.4 0.0 0.000 TL 7.75 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 ~ JOB TITLE: CARLSBAD RESEARCH/ROOF CALC .45/3000 06/22/99 PIPE DATA (cont'd) PIPE TAG Q(GPM) DIA( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) Pipe: 105 0.0 1.104 PL 8.75 PF 0.0 103 11. 0 0.0 48.4 0.0 0.0 120 FTG PE 0.0 104 11. 0 0.0 48.4 0.0 0.000 TL 8.75 PV 0.0 Pipe: 106 0.0 1. 452 PL 1.00 PF 0.0 42 11. 0 0.0 48.4 0.0 0.0 120 FTG PE 0.0 103 11. 0 0.0 48.4 0.0 0.000 TL 1.00 PV 0.0 Pipe: 107 0.0 1.104 PL 8.75 PF 0.0 106 11. 0 0.0 48.4 0.0 0.0 120 FTG PE 0.0 105 11.0 0.0 48.4 0.0 0.000 TL 8.75 PV 0.0 Pipe: 108 0.0 1. 452 PL 7.75 PF 0.0 41 11.0 0.0 48.4 0.0 0.0 120 FTG PE 0.0 106 11. 0 0.0 48.4 0.0 0.000 TL 7.75 PV 0.0 Pipe: 109 0.0 1.104 PL 8.75 PF 0.0 107 11. 0 0.0 48.4 0.0 0.0 120 FTG PE 0.0 108 11. 0 0.0 48.4 0.0 0.000 TL 8.75 PV 0.0 Pipe: 110 0.0 1. 452 PL 1.00 PF 0.0 41 11.0 0.0 48.4 0.0 0.0 120 FTG PE 0.0 108 11. 0 0.0 48.4 0.0 0.000 TL 1.00 PV 0.0 Pipe: 111 0.0 1.104 PL 8.75 PF 0.0 110 11. 0 0.0 48.4 0.0 0.0 120 FTG PE 0.0 109 11. 0 0.0 48.4 0.0 0.000 TL 8.75 PV 0.0 Pipe: 112 0.0 1. 452 PL 7.75 PF 0.0 40 11. 0 0.0 48.4 0.0 0.0 120 FTG PE 0.0 110 11. 0 0.0 48.4 0.0 0.000 TL 7.75 PV 0.0 Pipe: 113 0.0 1.104 PL 8.75 PF 0.0 111 11. 0 0.0 48.4 0.0 0.0 120 FTG PE 0.0 112 11. 0 0.0 48.4 0.0 0.000 TL 8.75 PV 0.0 Pipe: 114 0.0 1.452 PL 1.00 PF 0.0 40 11.0 0.0 48.4 0.0 0.0 120 FTG PE 0.0 111 11.0 0.0 48.4 0.0 0.000 TL 1.00 PV 0.0 Pipe: 115 0.0 1.104 PL 8.75 PF 0.0 114 11. 0 0.0 48.4 0.0 0.0 120 FTG PE 0.0 113 11. 0 o.o 48.4 0.0 0.000 TL 8.75 PV 0.0 Pipe: 116 0.0 1.452 PL 7.75 PF 0.0 39 11.0 o.o 48.4 0.0 0.0 120 FTG PE 0.0 114 11. 0 0.0 48.4 0.0 0.000 TL 7.75 PV 0.0 Pipe: 117 0.0 1.104 PL 8.75 PF 0.0 115 11. 0 0.0 48.4 0.0 0.0 120 fTG PE 0.0 116 11. 0 o.o 48.4 0.0 0.000 TL 8.75 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 13 \. JOB TITLE: CARLSBAD RESEARCH/ROOF CALC .45/3000 06/22/99 PIPE DATA (cont'd) PIPE TAG Q(GPM) DIA( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) Pipe: 118 · 0.0 1. 452 PL 1.00 PF 0.0 39 11. 0 0.0 48.4 0.0 0.0 120 FTG PE 0.0 115 11.0 0.0 48.4 0.0 0.000 TL 1.00 PV 0.0 Pipe: 120 0.0 1.104 PL 5.00 PF 0.0 38 11. 0 0.0 48.4 0.0 0.0 120 FTG PE 0.0 117 11. 0 0.0 48.4 0.0 0.000 TL 5.00 PV 0.0 NOTES: (1) Calculations were performed by the HASS 5.5.0 computer program under license no. 8926J521 granted by HRS Systems, Inc. 2193 Ranchwood Dr., N.E. Atlanta, GA 30345 (2) The system has been balanced to provide an average imbalance at each node of 0.002 gpm and a maximum imbalance at any node of 0.102 gpm. (3) Velocity pressures are printed for information only, and are not used in balancing the system. Maximum water velocity in any pipe is 16.5 ft/sec. ( 4 ) a. System remote area HAS been proven or 'peaked'. b. Minimum pressure at any sprinkler: 14.112 psi c. Minimum pressure with remote area shifted one sprinkler space toward left cross main: 14.121 psi d. Minimum pressure with remote area shifted one sprinkler space toward right cross main: 14.128 psi SPRINKLER SYSTEM HYDRAULIC ANALYSIS JOB TITLE: CARLSBAD RESEARCH/ROOF CALC .45/3000 (5) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: F MATERIAL: DFLO HWC: 120 Diameter Equivalent Fitting Lengths in (in) E T L C B Page 14 06/22/99 Feet G A D Ell Tee LNGELL CHKVLV BFYVLV GATVLV ALMVLV DPVLV 2.227 7.20 14.40 4.30 15.80 8.60 1. 40 14.40 14.40 4.328 14.20 28.50 8.50 31.30 17.10 2.80 28.50 14.20 6.403 17.60 37.70 11.30 40.20 12.60 3.80 35.20 23.90 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 15 JOB TITLE: CARLSBAD RESEARCH/ROOF CALC .45/3000 06/22/99 WATER SUPPLY CURVE , 120+ 0.,._,, l ~~~ 110+ <=: *\\\\\\\\\\\ \ \ \ \ \ \ \ \ l ~ l \\\\\\\_ ~\~ \ \ \ \ \ \ \ ---..--.,;.~~•1~<-4-la0~3-5.5--I?.P~S~i@ 1530 gpm Flow Test 7'oirrt 0 I I 100+ I I I I I I 90+ I I I I I I p 80+ R I I E I I s I I s 70+ u I I R I I E I I 60+ ( l P l s l I 50+ ) l I I I I 40+ I I I I I I 30+ I I I I 1------------------------------,------------~----------------- 20+ LEGEND " I I I I I I 10+ X = Required Water Supply 91.16 psf@ 1993.6 gpm l O = Available Water Supply l 100.66 psi@ 1993.6 gpm I I " " " " " " " O++-+---+----+-----+------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) · HYDRAULIC DESIGN INFORMATIQN SHEET :~:.\-,o-N-=--=---=--"T"'kdc...._-___ --+c-=--=-~-=-4:~~:,:s:~:.:::=· =~:::~=======k=~~~.;...-~~--....z..l:~_ . ...:.._-._· -_-_-___ o_A_Te _____ ;-=-~-=--v\.:-_~-:.-E-~ __ -i-=-=._:-i._ .... _' __ l_q:9-:. __ 9~---= eu1Lo1Na ______________________________ vsTeM No __ pt ___ ~----~------•H_._E. __ CONTRACTOR _____ . Cv ______ g_..J_efl._':{_[b __ ~_6. __ f:o ........ ,.J_~-----_· _____ c_:{l __ ( __ o_~ _____ (X)NfRACT N0 __ 4....a....q ____ g ___ 1 __ ~--- CALCULA TED BY __ __.,~--------------------DRA~ING NO ________ _ CONSTRUCTION: fX) "COMBUSTIBLE l I NON -COMBUSTIBLE CEILING HEIGUT _ _;;?.fi~_L-t> ___ FT. OCCUPANCY----------------------------------~-~_)C._· __ _ l)(J NFPA lJ: l ..J LT. H~Z.~ I • I ORD. HAZ. GP. ( .. J 1 0(1 :Z , l 1 .. 3 ( JEX. HAZ. ( ) NF.PA 2J1 · .. ~:( . ) NFPA 2j1c: FIGURE________ CURV------- ~ l J OTHER (Sp.clfyJ _______________ ;...._. _________________ _ in w .a ~ w t; r V) ) srec·1FIC R\!LINO -----------------MADE ev _______ o-.11: _____ _ AREA OF Sf'R.INKLER OPERATION-.....a..~-----Pl!!~--e::.:r DENSITY . ~-... . AREA PER SPfllt,Hd.ER HOSE ALLOWANCE GPM: INSIDE HOS~ ALLOWANCE GPM: OUTSIDE ___ cz._gj __ GJ}_M __ RACK SPRINt<~ER ALLOWANCE SYSTEM TYPE WET J DAY ( ·) DELUGE ( ) PRE-ACTION SPRINKLER OR NOZZLE MAKE ✓l!~& MOOEL __ M _____ _ SIZE !?Zi""~' K•FAGJOR B. D .TEMPERATURE RATING --i-Sh 0 f CALCULATION SUMMARY GPM . rlECUIRED 3t2 .S. !;C" FACTOR USED: PSI REQUIRED '2_ ~ • ':3: AT 81-SE OF RISER l ~() OVERHEAD· ___ \'°2-0 ____ UNOEROROUNO ________ _ >-J 0.. 0.. ::) (/) a: w r <( ~ w C, <( a: 0 t; ~ Q 0 :E ~ 0 u . WATER Fl.OW TEST OATEIHl~E MA::( L'qq~ PUMP DATA ANK OR RATED CAPACITY -----CAPACITY __;.---:~,:;;._ _____ _ STATIC PSI ('"2 .. t,, fS \ RESIDUAL PSI __ , __ \_S-____ .... e_s_·_. -- GPM FLOWING __ \_5 ...... i .... o ___ G ...... e __ fV\ __ ELEVATION AT PSI ELEVATION ELEV PROOFFLQW _______ GPM LOCATIQN ___ ··---------L.(2g-.:::.::..1.TYt0Lfo..!.1.:::. ::!.. ~~{U)=----Jfl:o~..:..A(J...;.;:;;... ____________ _ souAce-oF 1t:4FoRMA noN _____ _:A~F~-S::_...., --=C:.:.M.....;_~w..;:..i::=:o~J-....;:c..==-·...:.~~'D~.=------------ COMMODITY------------ClAS$ ________ LOCATION-----,,~---- STOAAGE H~IOHT AREA -------- STORAGE METH~6:" SOLID PILED . ~ . PALLETIZED ____ ___,,..,. J SINGLE ROW J CONVENTIONAL PALLET J DOUBLE ROW ) SLAVE PALLET . J SOLID SHELVING ) MULTIPLE AOW I OPEN -------" ( ) ENCAPSULATED. 1 ) NON• 1 ENCAPSULATeo ' CLEARANCE FROM TO~ Of STOAAOE TO CE I LINO t ._-----TRANSVERSE ___ _ ________ fT. _________ IN, OAl~ONTAL BARRIERS PROVIDED _________________________ _ SPRINKLER SYSTEM HYDRAULIC ANALYSIS · Page 1 Da~e: 11/01/91 835MEZA JOB TITLE: CARLSBAD RESEARCH/MEZZANINE CALC .20/1500 06/22/99 WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) 1 * 108. 0 +-103. 5 1530.0 107.1 622.5 37.4 _..~ 1Zeo"4.c-e-o ric-, ' & % fwt. G,ct(fff N--.' AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 622.5 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 250.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 372.5 GPM NODE ANALYSIS DATA NODE TAG ELEVATlON NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 -3.0 SOURCE 37.4 372.5 2 -3.0 37.2 --- 3 -3.0 37.2 --- 4 -3.0 ----27.2 --- 5 -3.0 ----26.9 --- 6 0.5 ----25.4 --- 7 26.5 ----13.9 --- 8 26.5 ----13.7 --- 9 26.5 13.7 --- 10 26.5 13.7 --- 11 26.5 13.7 --- 12 26.5 ----13.6 --- 13 26.5 13.6 --- 14 26.5 13.6 --- 15 26.5 ----13.6 --- 16 26.5 ----13.5 --- 17 26.5 ----13.5 --- 18 26.5 13.5 --- 19 26.5 ----13.5 --- 20 26.5 13.5 --- 21 26.5 ----12.8 --- 22 26.5 ----12.8 --- 23 26.5 12.8 --- 24 26.5 12.8 --- 25 26.5 12.8 --- 26 26.5 12.7 --- 27 26.5 12.6 --- 28 26.5 ----12.5 --- 29 26.5 ----12.3 --- 30 26.5 12.2 --- 31 26.5 ----12.1 --- 32 26.5 12.0 --- 33 26.5 ----13.5 --- 34 28.0 11. 3 --- SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 -; JOB TITLE: CARLSBAD RESEARCH/MEZZANINE CALC .20/1500 06/22/99 NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 35 28.0 ----11. 7 --- 36 28.0 11. 7 --- 37 11. 0 ----19.1 --- 38 11. 0 19.1 --- 39 11. 0 19.1 --- 40 11. 0 19.1 --- 41 11. 0 ----19.1 --- 42 11. 0 19.1 --- 301 28.0 K= 8.10 7.7 22.5 302 28.0 K= 8.10 7.7 22.4 303 28.0 K= 8.10 7.6 22.4 304 28.0 K= 8.10 7.7 22.4 305 28.0 K= 8.10 7.7 22.5 306 28.0 K= 8.10 7.9 22.7 307 28.0 K= 8.10 8.1 23.0 308 28.0 K= 8.10 8.0 22.9 309 28.0 K= 8.10 8.0 22.9 310 28.0 K= 8.10 8.0 22.9 311 28.0 K= 8.10 8.0 23.0 312 28.0 K= 8.10 8.2 23.2 313 28.0 K= 8.10 9.5 24.9 314 28.0 K= 8.10 9.4 24.9 315 28.0 K= 8.10 9.4 24.9 316 28.0 K= 8.10 9.5 24.9 201 28.0 ----12.2 --- 202 28.0 12.2 --- 203 28.0 ----12.1 --- 204 28.0 12.1 --- 205 28.0 ----12.1 --- 206 28.0 12.1 --- 207 28.0 12.0 --- 208 28.0 ----12.0 --- 209 28.0 ----12.0 --- 210 28.0 ----12.3 --- 211 28.0 ----12.2 --- 212 28.0 ----12.2 --- 213 28.0 ----12.2 --- 214 28.0 ----12.1 --- 215 28.0 ----12.1 --- 216 28.0 12.1 --- 217 28.0 ----12.1 --- 218 28.0 ----12.0 --- 219 28.0 ----12.4 --- 220 28.0 ----12.4 --- 221 28.0 ----12.3 --- 222 28.0 12.3 --- 223 28.0 ----12.3 --- 224 28.0 ----12.3 --- 225 28.0 ----12.2 --- 226 28.0 12.2 --- 227 28.0 12.2 --- 228 28.0 12.4 --- 229 28.0 ----12.4 --- 230 28.0 12.4 --- SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 JOB TITLE: CARLSBAD RESEARCH/MEZZANINE CALC .20/1500 06/22/99 NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 231 28.0 ----12.4 --- 232 28.0 ----12.3 --- 101 11. 0 19.1 --- 102 11. 0 ----19.1 --- 103 11. 0 ----19.1 --- 104 11. 0 19.1 --- 105 11. 0 19.1 --- 106 11. 0 19.1 --- 107 11. 0 ----19.1 --- 108 11. 0 19.1 --- 109 11. 0 19.1 --- 110 11. 0 ----19.1 --- 111 11. 0 ----19.1 --- 112 11. 0 ----19.1 --- 113 11. 0 ----19.1 --- 114 11. 0 19.1 --- 115 11. 0 ----19.1 --- 116 11. 0 19.1 --- 117 11. 0 ----19.1 --- SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 JOB TITLE: CARLSBAD RESEARCH/MEZZANINE CALC .20/1500 06/22/99 PIPE DATA PIPE TAG Q(GPM) DIA( IN) LENGTH PRESS. END ELEV. ijOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) Pipe: 1 372.5 7.987 PL 80.00 PF 0.1 1 -3.0 SRCE 37.4 (N/A) 2.4 150 FTG 52.50 PE 0.0 2 -3.0 0.0 37.2 0.0 0.001 TL 132.50 PV 0.0 Pipe: 2 372.4 7.987 PL 5.00 PF 0.0 2 -3.0 0.0 37.2 0.0 2.4 150 FTG 39.30 PE 0.0 3 -3.0 0.0 37.2 0.0 0.001 TL 44.30 PV 0.0 Pipe: 3 FIXED PRESSURE LOSS DEVICE 3 -3.0 0.0 37.2 0.0 10.0 psi, 372.4 gpm 4 -3.0 0.0 27.2 0.0 Pipe: 4 372.4 7.987 PL 233.00 PF 0.3 4 -3.0 0.0 27.2 0.0 2.4 150 FTG 39.30 PE 0.0 5 -3.0 0.0 26.9 0.0 0.001 TL 272.30 PV 0.0 Pipe: 5 372.4 8.510 PL 8.00 PF 0.0 5 -3.0 0.0 26.9 0.0 2.1 140 FTG 17.30 PE 1. 5 6 0.5 0.0 25.4 0.0 0.001 TL 25.30 PV 0.0 Pipe: 6 372.4 6.403 PL 26.50 PF 0.2 6 0.5 0.0 25.4 0.0 3.7 120 FTG L PE 11. 3 7 26.5 0.0 13.9 0.0 0.004 TL 37.80 PV 0.1 Pipe: 7 372.4 6.403 PL 22.00 PF 0.3 7 26.5 0.0 13.9 0.0 3.7 120 FTG T PE 0.0 10 26.5 0.0 13.7 0.0 0.004 TL 59.70 PV 0.1 Pipe: 8 -17.7 6.403 PL 12.00 PF 0.0 8 26.5 0.0 13.7 0.0 0.2 120 FTG PE 0.0 9 26.5 0.0 13.7 0.0 0.000 TL 12.00 PV 0.0 Pipe: 9 -35.4 6.403 PL 6.50 PF 0.0 9 26.5 0.0 13.7 0.0 0.4 120 FTG T PE 0.0 10 26.5 0.0 13.7 0.0 0.000 TL 44.20 PV 0.0 Pipe: 10 319.4 6.403 PL 5.50 PF 0.0 10 26.5 0.0 13.7 0.0 3.2 120 FTG PE 0.0 11 26.5 0.0 13.7 0.0 0.003 TL 5.50 PV 0.1 Pipe: 11 301.8 6.403 PL 12.00 PF 0.0 11 26.5 0.0 13.7 0.0 3.0 120 FTG PE 0.0 12 26.5 0.0 13.6 0.0 0.003 TL 12.00 PV 0.1 Pipe: 12 284.3 6.403 PL 12.00 PF 0.0 12 26.5 0.0 13.6 0.0 2.8 120 FTG PE 0.0 13 26.5 0.0 13.6 0.0 0.003 TL 12.00 PV 0.1 Pipe: 13 267.0 6.403 PL 12.00 PF 0.0 13 26.5 0.0 13.6 0.0 2.7 120 FTG PE 0.0 14 26.5 0.0 13.6 0.0 0.002 TL 12.00 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 JOB TITLE: CARLSBAD RESEARCH/MEZZANINE CALC .20/1500 06/22/99 PIPE DATA (cont'd) PIPE TAG Q(GPM) DIA( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) Pipe: 14 249.6 6.403 PL 12.00 PF 0.0 14 26.5 0.0 13.6 0.0 2.5 120 FTG PE 0.0 15 26.5 0.0 13.6 0.0 0.002 TL 12.00 PV 0.0 Pipe: 15 230.9 6.403 PL 12.00 PF 0.0 15 26.5 0.0 13.6 0.0 2.3 120 FTG PE 0.0 16 26.5 0.0 13.5 0.0 0.002 TL 12.00 PV 0.0 Pipe: 16 211. 9 6.403 PL 12.00 PF 0.0 16 26.5 0.0 13.5 0.0 2.1 120 FTG PE · 0.0 17 26.5 0.0 13.5 0.0 0.002 TL 12.00 PV 0.0 Pipe: 17 190.6 6.403 PL 12.00 PF 0.0 17 26.5 0.0 13.5 0.0 1. 9 120 FTG PE 0.0 18 26.5 0.0 13.5 0.0 0.001 TL 12.00 PV 0.0 Pipe: 18 168.6 6.403 PL 11.25 PF 0.0 18 26.5 0.0 13.5 0.0 1. 7 120 FTG PE 0.0 19 26.5 0.0 13.5 · 0. 0 0.001 TL 11.25 PV 0.0 Pipe: 19 121.7 6.403 PL 36.00 PF 0.0 19 26.5 0.0 13.5 0.0 1. 2 120 FTG L PE 0.0 20 26.5 0.0 13.5 0.0 0.001 TL 47.30 PV 0.0 Pipe: 20 59.6 6.403 PL 12.00 PF 0.0 20 26.5 0.0 13.5 0.0 0.6 120 FTG PE 0.0 33 26.5 0.0 13.5 0.0 0.000 TL 12.00 PV 0.0 .-., Pipe: 21 17.7 4.328 PL 12.00 PF 0.0 21 26.5 0.0 12.8 0.0 0.4 120 FTG PE 0.0 22 26.5 0.0 12.8 0.0 0.000 TL 12.00 PV 0.0 Pipe: 22 53.1 4.328 PL 12.00 PF 0.0 22 26.5 0.0 12.8 0.0 1. 2 120 FTG PE 0.0 23 26.5 0.0 12.8 0.0 0.001 TL 12.00 PV 0.0 Pipe: 23 70.7 4.328 PL 12.00 PF 0.0 23 26.5 0.0 12.8 0.0 1. 5 120 FTG PE 0.0 24 26.5 0.0 12.8 0.0 0.001 TL 12.00 PV 0.0 Pipe: 24 88.1 4.328 PL 12.00 PF 0.0 24 26.5 0.0 12.8 0.0 1. 9 120 FTG PE 0.0 25 26.5 0.0 12.8 0.0 0.002 TL 12.00 PV 0.0 Pipe: 25 105.4 4.328 PL 12.00 PF 0.0 25 26.5 0.0 12.8 0.0 2.3 120 FTG PE 0.0 26 26.5 0.0 12.7 0.0 0.003 TL 12.00 PV 0.0 Pipe: 26 122.8 4.328 PL 20.50 PF 0.1 26 26.5 0.0 12.7 0.0 2.7 120 FTG 2L PE 0.0 27 26.5 0.0 12.6 0.0 0.004 TL 37.50 PV 0.0 ~PRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 JOB TITLE: CARLSBAD RESEARCH/MEZZANINE CALC .20/1500 06/22/99 PIPE DATA (cont'q) PIPE TAG Q(GPM) DIA( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) Pipe: 27 141.5 4.328 PL 12.00 PF 0.1 27 26.5 0.0 12.6 0.0 3.1 120 FTG PE 0.0 28 26.5 0.0 12.5 0.0 0.005 TL 12.00 PV 0.1 Pipe: 28 160.5 4.328 PL 1.00 PF 0.2 28 26.5 0.0 12.5 0.0 3.5 120 FTG T PE 0.6 35 28.0 0.0 11. 7 0.0 0.006 TL 29.50 PV 0.1 Pipe: 29 160.5 4.328 PL 11. 00 PF 0.1 35 28.0 0.0 11. 7 0.0 3.5 120 FTG PE 0.6 29 26.5 0.0 12.3 0.0 0.006 TL 11. 00 PV 0.1 Pipe: 30 181.8 4.328 PL 12.00 PF 0.1 29 26.5 0.0 12.3 0.0 4.0 120 FTG PE 0.0 30 26.5 0.0 12.2 0.0 0.008 TL 12.00 PV 0.1 Pipe: 31 203.8 4.328 PL 12.00 PF 0.1 30 26.5 0.0 12.2 0.0 4.4 120 FTG PE 0.0 31 26.5 0.0 12.1 0.0 0.010 TL 12.00 PV 0.1 Pipe: 32 151.1 4.328 PL 12.00 PF 0.1 31 26.5 0.0 12.1 0.0 3.3 120 FTG PE 0.0 32 26.5 0.0 12.0 0.0 0.006 TL 12.00 PV 0.1 Pipe: 33 75.4 4.328 PL 12.00 PF 0.0 32 26.5 0.0 12.0 0.0 1. 6 120 FTG PE 0.6 34 28.0 0.0 11. 3 0.0 0.002 TL 12.00 PV 0.0 Pipe: 34 59.6 2.227 PL 156.00 PF 5.1 33 26.5 0.0 13.5 0.0 4.9 120 FTG 2T4L PE 0.6 301 28.0 8.1 7.7 22.5 0.025 TL 202.00 PV 0.2 Pipe: 35 37.0 2.227 PL 8.00 PF 0.1 301 28.0 8.1 7.7 22.5 3.1 120 FTG PE 0.0 302 28.0 8.1 7.7 22.4 0.010 TL 8.00 PV 0.1 Pipe: 36 14.6 2.227 PL 8.00 PF 0.0 302 28.0 8.1 7.7 22.4 1. 2 120 FTG PE 0.0 303 28.0 8.1 7.6 22.4 0.002 TL 8.00 PV 0.0 Pipe: 37 -7.8 2.227 PL 8.00 PF 0.0 303 28.0 8.1 7.6 22.4 0.6 120 FTG PE 0.0 304 28.0 8.1 7.7 22.4 0.001 TL 8.00 PV 0.0 Pipe: 38 -30.2 2.227 PL 8.00 PF 0.1 304 28.0 8.1 7.7 22.4 2.5 120 FTG PE 0.0 305 28.0 8.1 7.7 22.5 0.007 TL 8.00 PV 0.0 Pipe: 39 -52.7 2.227 PL 8.00 PF 0.2 305 28.0 8.1 7.7 22.5 4.3 120 FTG PE 0.0 306 28.0 8.1 7.9 22.7 0.020 TL 8.00 PV 0.1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 ~ JOB TITLE: CARLSBAD RESEARCH/MEZZANINE CALC .20/1500 06/22/99 PIPE DATA (cont'd) PIPE TAG Q(GPM) DIA( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) Pipe: 40 -75.4 2.227 PL 52.00 PF 3.5 306 28.0 8.1 7.9 22.7 6.2 120 FTG 2T2L PE 0.0 34 28.0 0.0 11. 3 0.0 0.039 TL 89.40 PV 0.3 Pipe: 41 62.1 2.227 PL 156.00 PF 4.7 20 26.5 0.0 13.5 0.0 5.1 120 FTG TL PE 0.6 307 28.0 8.1 8.1 23.0 0.027 TL 174.70 PV 0.2 Pipe: 42 39.1 2.227 PL 8.00 PF 0.1 307 28.0 8.1 8.1 23.0 3.2 120 FTG PE 0.0 308 28.0 8.1 8.0 22.9 0.011 TL 8.00 PV 0.1 Pipe: 43 16.2 2.227 PL 8.00 PF 0.0 308 28.0 8.1 8.0 22.9 1. 3 120 FTG PE 0.0 309 28.0 8.1 8.0 22.9 0.002 TL 8.00 PV 0.0 Pipe: 44 -6.7 2.227 PL 8.00 PF 0.0 309 28.0 8.1 8.0 22.9 0.6 120 FTG PE 0.0 310 28.0 8.1 8.0 22.9 0.000 TL 8.00 PV 0.0 Pipe: 45 -29.6 2.227 PL 8.00 PF 0.1 310 28.0 8.1 8.0 22.9 2.4 120 FTG PE 0.0 311 28.0 8.1 8.0 23.0 0.007 TL 8.00 PV 0.0 Pipe: 46 -52.6 2.227 PL 8.00 PF 0.2 311 28.0 8.1 8.0 23.0 4.3 120 FTG PE 0.0 312 28.0 8.1 8.2 23.2 0.020 TL 8.00 PV 0.1 Pipe: 47 -75.7 2.227 PL 52.00 PF 3.2 312 28.0 8.1 8.2 23.2 6.2 120 FTG 2T PE 0.6 32 26.5 0.0 12.0 0.0 0.039 TL 80.80 PV 0.3 Pipe: 48 47.0 2.227 PL ·180.00 PF 3.4 19 26.5 0.0 13.5 0.0 3.9 120 FTG 2T PE 0.6 313 28.0 8.1 9.5 24.9 0.016 TL 208.80 PV 0.1 Pipe: 49 22.0 2.227 PL 8.00 PF 0.0 313 28.0 8.1 9.5 24.9 1.8 120 FTG PE 0.0 314 28.0 8.1 9.4 24.9 0.004 TL 8.00 PV 0.0 Pipe: 50 -2.8 2.227 PL 8.00 PF 0.0 314 28.0 8.1 9.4 24.9 0.2 120 FTG PE 0.0 315 28.0 8.1 9.4 24.9 0.000 TL 8.00 PV 0.0 Pipe: 51 -27.7 2.227 PL 8.00 PF 0.0 315 28.0 8.1 9.4 24.9 2.3 120 FTG PE 0.0 316 28.0 8.1 9.5 24.9 0.006 TL 8.00 PV 0.0 Pipe: 52 -52.7 2.227 PL 68.00 PF 1. 9 316 28.0 8.1 9.5 24.9 4.3 120 FTG 2T PE 0.6 31 26.5 0.0 12.1 0.0 0.020 TL 96.80 PV 0.1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 JOB TITLE: CARLSBAD RESEARCH/MEZZANINE CALC .20/1500 06/22/99 PIPE DATA (cont'd) PIPE TAG Q(GPM) DIA( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) Pipe: 53 22.0 2.227 PL 132.00 PF 0.6 18 26.5 0.0 13.5 0.0 1. 8 120 FTG 2T PE 0.6 201 28.0 0.0 12.2 0.0 0.004 TL 160.80 PV 0.0 Pipe: 54 22.0 2.227 PL 8.00 PF 0.0 201 28.0 0.0 12.2 0.0 1.8 120 FTG PE 0.0 202 28.0 0.0 12.2 0.0 0.004 TL 8.00 PV 0.0 Pipe: 55 22.0 2.227 PL 8.00 PF 0.0 202 28.0 0.0 12.2 0.0 1. 8 120 FTG PE 0.0 203 28.0 0.0 12.1 0.0 0.004 TL 8.00 PV 0.0 Pipe: 56 22.0 2.227 PL 8.00 PF 0.0 203 28.0 0.0 12.1 0.0 1.8 120 FTG PE 0.0 204 28.0 0.0 12.1 0.0 0.004 TL 8.00 PV 0.0 Pipe: 57 22.0 2.227 PL 8.00 PF 0.0 204 28.0 0.0 12.1 0.0 1. 8 120 FTG PE 0.0 205 28.0 0.0 12.1 0.0 0.004 TL 8.00 PV 0.0 Pipe: 58 22.0 2.227 PL 8.00 PF 0.0 205 28.0 0.0 12.1 0.0 1.8 120 FTG PE 0.0 206 28.0 0.0 12.1 0.0 0.004 TL 8.00 PV 0.0 Pipe: 59 22.0 2.227 PL 8.00 PF 0.0 206 28.0 0.0 12.1 0.0 1. 8 120 FTG PE 0.0 207 28.0 0.0 12.0 0.0 0.004 TL 8.00 PV 0.0 Pipe: 60 22.0 2.227 PL 8.00 PF 0.0 207 28.0 0.0 12.0 0.0 1.8 120 FTG PE 0.0 208 28.0 0.0 12.0 0.0 0.004 TL 8.00 PV 0.0 Pipe: 61 22.0 2.227 PL 8.00 PF 0.0 208 28.0 0.0 12.0 0.0 1. 8 120 FTG PE 0.0 209 28.0 0.0 12.0 0.0 0.004 TL 8.00 PV 0.0 Pipe: 62 22.0 2.227 PL 78.00 PF 0.4 209 28.0 0.0 12.0 0.0 1. 8 120 FTG 2T PE 0.6 30 26.5 0.0 12.2 0.0 0.004 TL 106.80 PV 0.0 Pipe: 63 21. 3 2.227 PL 132.00 PF 0.6 17 26.5 0.0 13.5 0.0 1. 8 120 FTG 2T PE 0.6 210 28.0 0.0 12.3 0.0 0.004 TL 160.80 PV 0.0 Pipe: 64 21. 3 2.227 PL 8.00 PF 0.0 210 28.0 0.0 12.3 0.0 1. 8 120 fTG PE 0.0 211 28.0 0.0 12.2 0.0 0.004 TL 8.00 PV 0.0 Pipe: 65 21. 3 2.227 PL 8.00 PF 0.0 211 28.0 0.0 12.2 0.0 1. 8 120 FTG PE 0.0 212 28.0 0.0 12.2 0.0 0.004 TL 8.00 PV 0.0 qPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 JOB TITLE: CARLSBJ\D RESEARCH/MEZZANINE CALC .20/1500 06/22/99 PIPE DATA (cont'q) PIPE TAG Q(GPM) DIA( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) Pipe: 66 21. 3 2.227 PL 8.00 PF 0.0 212 28.0 0.0 12.2 0.0 1. 8 120 FTG PE 0.0 213 28.0 0.0 12.2 0.0 0.004 TL 8.00 PV 0.0 Pipe: 67 21. 3 2.227 PL 8.00 PF 0.0 213 28.0 0.0 12.2 0.0 1.8 120 FTG PE 0.0 214 28.0 0.0 12.1 0.0 0.004 TL 8.00 PV 0.0 Pipe: 68 21. 3 2.227 PL 8.00 PF 0.0 214 28.0 0.0 12.1 0.0 1. 8 120 FTG PE 0.0 215 28.0 0.0 12.1 0.0 0.004 TL 8.00 PV 0.0 Pipe: 69 21. 3 2.227 PL 8.00 PF 0.0 215 28.0 0.0 12.1 0.0 1.8 120 FTG PE 0.0 216 28.0 0.0 12.1 0.0 0.004 TL 8.00 PV 0.0 Pipe: 70 21. 3 2.227 PL 8.00 PF 0.0 216 28.0 0.0 12.1 0.0 1. 8 120 FTG PE 0.0 217 28.0 0.0 12.1 0.0 0.004 TL 8.00 PV 0.0 Pipe: 71 21. 3 2.227 PL 8.00 PF 0.0 217 28.0 0.0 12.1 0.0 1.8 120 FTG PE 0.0 218 28.0 0.0 12.0 0.0 0.004 TL 8.00 PV 0.0 Pipe: 72 21. 3 2.227 PL 78.00 PF 0.4 218 28.0 0.0 12.0 0.0 1. 8 120 FTG 2T PE 0.6 29 26.5 0.0 12.3 0.0 0.004 TL 106.80 PV 0.0 Pipe: 73 19.0 2.227 PL 132.00 PF 0.5 16 26.5 0.0 13.5 0.0 1. 6 120 FTG 2T PE 0.6 219 28.0 0.0 12.4 0.0 0.003 TL 160.80 PV 0.0 Pipe: 74 19.0 2.227 PL 8.00 PF 0.0 219 28.0 0.0 12.4 0.0 1. 6 120 FTG PE 0.0 220 28.0 0.0 12 .4 0.0 0.003 TL 8.00 PV 0.0 Pipe: 75 19.0 2.227 PL 8.00 PF 0.0 220 28.0 0.0 12.4 0.0 1. 6 120 FTG PE 0.0 221 28.0 0.0 12.3 0.0 0.003 TL 8.00 PV 0.0 Pipe: 76 19.0 2.227 PL 8.00 PF 0.0 221 28.0 0.0 12.3 0.0 1. 6 120 fTG PE 0.0 222 28.0 0.0 12.3 0.0 0.003 TL 8.00 PV 0.0 Pipe: 77 19.0 2.227 PL 8.00 PF 0.0 222 28.0 0.0 12.3 0.0 1. 6 120 FTG PE 0.0 223 28.0 0.0 12.3 0.0 0.003 TL 8.00 PV 0.0 Pipe: 78 19.0 2.227 PL 8.00 PF 0.0 223 28.0 0.0 12.3 0.0 1. 6 120 FTG PE 0.0 224 28.0 0.0 12.3 0.0 0.003 TL 8.00 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 JOB TITLE: CARLSBAD RESEARCH/MEZZANINE CALC .20/1500 06/22/99 PIPE DATA (cont'q) PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) Pipe: 79 19.0 2.227 PL 8.00 PF 0.0 224 28.0 0.0 12.3 0.0 1. 6 120 FTG PE 0.0 225 28.0 0.0 12.2 0.0 0.003 TL 8.00 PV 0.0 Pipe: 80 19.0 2.227 PL 8.00 PF 0.0 225 28.0 0.0 12.2 0.0 1. 6 120 FTG PE 0.0 226 28.0 0.0 12.2 0.0 0.003 TL 8.00 PV 0.0 Pipe: 81 19.0 2.227 PL 8.00 PF 0.0 226 28.0 0.0 12.2 0.0 1. 6 120 FTG PE 0.0 227 28.0 0.0 12.2 0.0 0.003 TL 8.00 PV 0.0 Pipe: 82 19.0 2.227 PL 78.00 PF 0.3 227 28.0 0.0 12.2 0.0 1. 6 120 FTG 2T PE 0.6 28 26.5 0.0 12.5 0.0 0.003 TL 106.80 PV 0.0 Pipe: 83 18.7 2.227 PL 132.00 PF 0.5 15 26.5 0.0 13.6 0.0 1. 5 120 FTG 2T PE 0.6 228 28.0 0.0 12.4 0.0 0.003 TL 160.80 PV 0.0 Pipe: 84 18.7 2.227 PL 8.00 PF 0.0 228 28.0 0.0 12.4 0.0 1. 5 120 FTG PE 0.0 229 28.0 0.0 12.4 0.0 0.003 TL 8.00 PV 0.0 Pipe: 85 18.7 2.227 PL 8.00 PF 0.0 229 28.0 0.0 12.4 0.0 1. 5 120 FTG PE 0.0 230 28.0 0.0 12.4 0.0 0.003 TL 8.00 PV 0.0 Pipe: 86 18.7 2.227 PL 8.00 PF 0.0 230 28.0 0.0 12.4 0.0 1. 5 120 FTG PE 0.0 231 28.0 0.0 12.4 0.0 0.003 TL 8.00 PV 0.0 Pipe: 87 18.7 2.227 PL 8.00 PF 0.0 231 28.0 0.0 12.4 0.0 1. 5 120 FTG PE 0.0 232 28.0 0.0 12.3 0.0 0.003 TL 8.00 PV 0.0 Pipe: 88 18.7 2.227 PL 109.00 PF 0.4 232 28.0 0.0 12.3 0.0 1. 5 120 FTG 2T PE 0.6 27 26.5 0.0 12.6 0.0 0.003 TL 137.80 PV 0.0 Pipe: 89 17.4 2.227 PL 274.50 PF 0.9 14 26.5 0.0 13.6 0.0 1. 4 120 FTG 4T PE 0.0 26 26.5 0.0 12.7 0.0 0.003 TL 332.10 PV 0.0 Pipe: 90 17.3 2.227 PL 274.50 PF 0.8 13 26.5 0.0 13.6 0.0 1. 4 120 FTG 4T PE 0.0 25 26.5 0.0 12.8 0.0 0.003 TL 332.10 PV 0.0 Pipe: 91 17.4 2.227 PL 274.50 PF 0.9 12 26.5 0.0 13.6 0.0 1. 4 120 FTG 4T PE 0.0 24 26.5 0.0 12.8 0.0 0.003 TL 332.10 PV 0.0 ~PRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 JOB TITLE: CARLSBAD RESEARCH/MEZZANINE CALC .20/1500 06/22/99 PIPE DATA (cont'q) PIPE TAG Q(GPM) DIA( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) Pipe: 92 17.6 2.227 PL 274.50 PF 0.9 11 26.5 0.0 13.7 0.0 1. 5 120 FTG 4T PE 0.0 23 26.5 0.0 12.8 0.0 0.003 TL 332.10 PV 0.0 Pipe: 93 17.7 2.227 PL 274.50 PF 0.9 10 26.5 0.0 13.7 0.0 1. 5 120 FTG 4T PE 0.0 22 26.5 0.0 12.8 0.0 0.003 TL 332.10 PV 0.0 Pipe: 94 17.7 2.227 PL 274.50 PF 0.9 9 26.5 0.0 13.7 0.0 1. 5 120 FTG 4T PE 0.0 22 26.5 0.0 12.8 0.0 0.003 TL 332.10 PV 0.0 Pipe: 95 17.7 2.227 PL 274.50 PF 0.9 8 26.5 0.0 13.7 0.0 1. 5 120 FTG 4T PE 0.0 21 26.5 0.0 12.8 0.0 0.003 TL 332.10 PV 0.0 Pipe: 96 0.0 3.356 PL 5.00 PF 0.0 35 28.0 0.0 11. 7 0.0 0.0 120 FTG L PE 0.0 36 28.0 0.0 11. 7 0.0 0.000 TL 12.70 PV 0.0 Pipe: 97 0.1 3.356 PL 17.00 PF 0.0 36 28.0 0.0 11. 7 0.0 0.0 120 FTG L PE 7.4 37 11.0 0.0 19.1 0.0 0.000 TL 24.70 PV 0.0 Pipe: 98 0.0 3.356 PL 212.00 PF 0.0 37 11. 0 0.0 19.1 0.0 0.0 120 FTG 3L PE 0.0 38 11. 0 0.0 19.1 0.0 0.000 TL 235.10 PV 0.0 Pipe: 99 0.0 3.356 PL 14.00 PF 0.0 38 11.0 0.0 19.1 0.0 0.0 120 FTG PE 0.0 39 11. 0 0.0 19.1 0.0 0.000 TL 14.00 PV 0.0 Pipe: 100 0.0 3.356 PL 12.00 PF 0.0 39 11. 0 0.0 19.1 0.0 0.0 120 FTG PE 0.0 40 11.0 0.0 19.1 0.0 0.000 TL 12.00 PV 0.0 Pipe: 101 0.0 3.356 PL 10.00 PF 0.0 40 11.0 0.0 19.1 0.0 0.0 120 FTG PE 0.0 41 11. 0 0.0 19.1 0.0 0.000 TL 10.00 PV 0.0 Pipe: 102 0.0 3.356 PL 8.50 PF 0.0 41 11. 0 0.0 19.1 0.0 0.0 120 FTG PE 0.0 42 11. 0 0.0 19.1 0.0 0.000 TL 8.50 PV 0.0 Pipe: 103 0.0 1.104 PL 8.75 PF 0.0 102 11.0 0.0 19.1 0.0 0.0 120 FTG PE 0.0 101 11. 0 0.0 19.1 0.0 0.000 TL 8.75 PV 0.0 Pipe: 104 0.0 1. 452 PL 7.75 PF 0.0 42 11. 0 0.0 19.1 0.0 0.0 120 FTG PE 0.0 102 11.0 0.0 19.1 0.0 0.000 TL 7.75 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 JOB TITLE: CARLSB.l\D RESEARCH/MEZZANINE CALC .20/1500 06/22/99 PIPE DATA (cont'd) PIPE TAG Q(GPM) DIA( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) Pipe: 105 0.0 1.104 PL 8.75 PF 0.0 103 11. 0 0.0 19.1 0.0 0.0 120 FTG PE 0.0 104 11. 0 0.0 19.1 0.0 0.000 TL 8.75 PV 0.0 Pipe: 106 0.0 . 1. 452 PL 1.00 PF 0.0 42 11.0 0.0 19.1 0.0 0.0 120 FTG PE 0.0 103 11. 0 0.0 19.1 0.0 0.000 TL 1.00 PV 0.0 Pipe: 107 0.0 1.104 PL 8.75 PF 0.0 106 11. 0 0.0 19.1 0.0 0.0 120 FTG PE 0.0 105 11.0 0.0 19.1 0.0 0.000 TL 8.75 PV 0.0 Pipe: 108 0.0 1. 452 PL 7.75 PF o.o 41 11. 0 0.0 19.1 0.0 0.0 120 FTG PE 0.0 106 11. 0 0.0 19.1 0.0 0.000 TL 7.75 PV 0.0 Pipe: 109 0.0 1.104 PL 8.75 PF 0.0 107 11. 0 0.0 19.1 0.0 0.0 120 FTG PE 0.0 108 11.0 0.0 19.1 0.0 0.000 TL 8.75 PV 0.0 Pipe: 110 0.0 1. 452 PL 1.00 PF 0.0 41 11. 0 0.0 19.1 0.0 0.0 120 FTG PE 0.0 108 11. 0 0.0 19.1 0.0 0.000 TL 1.00 PV 0.0 Pipe: 111 0.0 1.104 PL 8.75 PF 0.0 110 11. 0 0.0 19.1 0.0 0.0 120 FTG PE 0.0 109 11. 0 0.0 19.1 0.0 0.000 TL 8.75 PV 0.0 Pipe: 112 0.0 1. 452 PL 7.75 PF 0.0 40 11.0 0.0 19.1 0.0 0.0 120 FTG PE 0.0 110 11. 0 0.0 19.1 0.0 0.000 TL 7.75 PV 0.0 Pipe: 113 0.0 1.104 PL 8.75 PF 0.0 111 11. 0 0.0 19.1 0.0 0.0 120 FTG PE 0.0 112 11. 0 0.0 19.1 0.0 0.000 TL 8.75 PV 0.0 Pipe: 114 0.0 1.452 PL 1.00 PF 0.0 40 11.0 0.0 19.1 0.0 0.0 120 FTG PE 0.0 111 11. 0 0.0 19.1 0.0 0.000 TL 1.00 PV 0.0 Pipe: 115 0.0 1.104 PL 8.75 PF 0.0 114 11. 0 0.0 19.1 0.0 0.0 120 FTG PE 0.0 113 11.0 0.0 19.1 0.0 0.000 TL 8.75 PV 0.0 Pipe: 116 0.0 1.452 PL 7.75 PF 0.0 39 11.0 0.0 19.1 0.0 0.0 120 FTG PE 0.0 114 11. 0 0.0 19.1 0.0 0.000 TL 7.75 PV 0.0 Pipe: 117 0.0 1.104 PL 8.75 PF 0.0 115 11. 0 0.0 19.1 0.0 0.0 120 FTG PE 0.0 116 11.0 0.0 19.1 0.0 0.000 TL 8.75 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 13 JOB TITLE: CARLSBAD RESEARCH/MEZZANINE CALC .20/1500 06/~2/99 PIPE DATA (cont'cJ) PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) Pipe: 118 0.0 1. 452 PL 1.00 PF 0.0 39 11. 0 0.0 19.1 0.0 0.0 120 FTG PE 0.0 115 11. 0 0.0 19.1 0.0 0.000 TL 1.00 PV 0.0 Pipe: 120 0.0 1.104 PL 5.00 PF 0.0 38 11. 0 0.0 19.1 0.0 0.0 120 FTG PE 0.0 117 11. 0 0.0 19.1 0.0 0.000 TL 5.00 PV 0.0 NOTES: (1) Calculations were performed by the HASS 5.5.0 computer program under license no. 8926J521 granted by HRS Systems, Inc. 2193 Ranchwood Dr., N.E. Atlanta, GA 30345 (2) The system hqs been balanced to provide an average imbalance at each node of 0.001 gpm and a maximum imbalance at any node of 0.121 gpm. (3) Velocity pre~sures are printed for information only, and are not used in q~lancing the system. Maximum water velocity in any pipe is 6.2 ft/sec. (4) PIPE FITTING$ TABLE Pipe Table Nqme: STANDARD.PIP PAGE: F MATERIAL: DFLO HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A Ell Tee LNGELL CHKVLV BFYVLV GATVLV ALMVLV 2.227 1.20 14.40 4.30 15.80 8.60 1. 40 14.40 4.328 11.20 28.50 8.50 31.30 17.10 2.80 28.50 6.403 11.60 37.70 11.30 40.20 12.60 3.80 35.20 D DPVLV 14.40 14.20 23.90 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 14 JOB TITLE: CARLSBAD RESEARCH/MEZZANINE CALC .20/1500 06/22/99 WATER SUPPLY CURVE p R E s s u R E ( p s I ) ~ 120i # 110+ I ~ -\\\\\\\0\\ \\\~\ ~ \ \ I \\\~\\\\\\\\\\ I I 100+ I I I I I I 90+ I I I I I I 80+ I I I I I I 70+ I I I I I I 60+ I I I I I I 50+ I I I I I I 40+ I I I I I I 30+ I I I I X I===========~================== 20+ LEGEND " I I I I I I 10+ X = Required Water Supply 37.36 psi@ 622.5 gpm I O = Available Water Supply I 107.15 psi@ 622.5 gpm I I " " " " " " " -_.., E 103 5 psi @ 1530 gpm Flow Test PulnL O++-+---+----~-----+------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) · HYDRAULIC DESIGN INFOAMATIQN SHEET NAME ___ -,--~C~A-<Lt _____ <;_BAf __ . .;....D_~.:,.....;;;;..~~----~\ ___,;;;~;;.._. ~.J,.,~,;;;;;;.· __ DATE-~ _(JJ_~_~_£, ___ 7..._«'2_., __ l __ °t ___ 9 ____ <j __ _ LOCATION ___ L4f ___ 4_1........,_ ____ fu ____ ~➔-----------'2-Q---_..._'(PO_/f0 ____________ ~--:------~ BUILOINQ _________ , _________________ _sysTEM NO \38.-0v-J M.€2..--i.A-,~s1~E CONTRACTO R------=OJ ___ e......._,-..l_az._ ____ --=~--r,v,._I _u ___ E. ____ C-0_..:)_$:tQu__...,· ._____C_:U .... 1 .... 0 __ ~-=-----00NTRACT NO 4q .,.. ~ ~~ CALCULATED BY---~~--~·-' ________________ ORA\'_IINO NO------------ CONSTRUCTION: ,}Q ·coMeu~i-,oLE l J NON•COMeusneLe ce,uNa He1011r __ l_?:>_'-_'=»_"_~FT. OCCUPANCY _________________________________ O_e:L_tc::::_--- z l:) (/) w .a ~ w t;; >-V) v(J NFPA lJ: l ) LT. H~Z~ ORD.HAZ.OP. l .. J 1 ()4 :Z, ( J_.l l I EX. HAZ. ( ) NF.PA 2J1 · .. ~:( . ) NFPA 2j1c: FIGURE _______ _ CURV.__ _____ _ I I OTHER (Specify) _________________________________ _ I SPEdFIC R\.!LINO -----------------MACE ev _______ oa.ra _____ _ AREA OF SPRINKLER OPERATION----'~----r-=~~.,. DENSITY . "· .... . AREA PER SPAtr·iKlER HOSE ALLOWANCE GPM: INSIDE HQ$t: ALLOWANCE GPM: OUTSIDE __ ?-...,..5]) __ {;,._(/ __ M __ HACK SPRINK~ER ALLOWANCE SYSTEM TYPE [')() WET ) DRY ( · ) DELUGE ( J PRE •ACTION SPRINKLER OR NOZZLE MAKE Yl~..J b M size Y2"1 --:::s:-._-s.:-.:-_-_-_-_-_ TEMPERATURE RATING CALCULATION SUMMARY GPM . hEOUIRED ~00 · ~ !;C,, FACTOR USED: PSI REQUIRED __ 5 ___ \ ._C) ___ AT B,}SE OF RISER OVERHEAD' · ('LO UNDEROAOUNo __ l...,:iS.___O ____ _ >-..J 0.. 0.. :J V) a: w t-. <( ~ w l:) c{ a: 0 t; t 0 0 ~ ~ 0 u . WATER FLOW TEST DATE & T\~E t'½::C ,, l°t4~ \~.\15>t STATIC PSI A ES I DUAL PS I __ \ ___ \ ~ ___ p_l:,_, __ l __ _ GPM FLaw1No __ 1_s_;_b ___ b_(l._M ____ _ rUMP DATA RATED CAPACITY AT PSI ELEVATION ELEVATION PROOF FLOW _______ GPM LocAr10N __ ·_·-_· _____ _.:.,.J2u~Dz\~·:.a.:e;.,.,f2.;::.ieQ~(ZOi..;..;;;. _ __...f2o__,_;.AD_.;;;.. _________ _ souRce-oF 1~FoRMAT1ON _____ ---'-A....;..;..r...:;s~,.,......;c..~M~w...;.....:D;..,;_• _c_.__;F.:-,:•._;,:o;...,&...-_________ _ COMMODITY ____________ CLASS ________ LOCATION-----~--- STOAAGE Hl;IOHT AREA --------.. i .. ~ " . . . • .. STORAGE METHOD: SOLIO PILED ,r. PALLETIZED--------------" ')('. u <( a: ) SINGLE ROW I DOUBLE ROW ) CONVENTIONAL PALLET J SLAVE PALLET ) SOLID SHELVING ( ) ENCAPSULATED t J NON·• ', . . ) MULTIPLE ROW ) OPEN ENCAPSULATED CLEARANCe FROM TO,,: OF STOAAOE TO CE I LINO I ,,_ ____ JRANSVEnse ___ _ ________ ff. _________ lN. ORl~ONTAL BARRIERS PROVIDED _________________________ _ SPRINKLER SYSTEM HYDRAULIC ANALYSIS , Date: 11/01/91 Page 1 , 835BELOW 06/22/99 JOB TITLE: CARLSBAD RESEARCH/BELOW MEZZ .20/1500 WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. NODE PRESS. PRESS. @ PRESS. @ TAG (PSI) (PSI) (GPM) (PSI) 1 ;, 108.0 .. 103.5 1530.0 107.2 TOTAL REQ'D DEMAND PRESS. (GPM) (PSI) 610.5 62.9 *~ ~c,EYJ 0'1 to¼ ~L Gu.C~M. I • AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE TOTAL HOSE STREAM ALLOWANCE AT SOURCE OTHER HOSE STREAM ALLOWANCES TOTAL DISCHARGE FROM ACTIVE SPRINKLERS NODE ANALYSIS DATA NODE TAG 1 2 3 4 5 6 7 8 9 10 11 12 13 14 . 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 ELEVATION (FT) -3.0 -3.0 -3.0 -3.0 -3.0 0.5 26.5 26.5 26.5 26.5 26.5 26.5 26.5 26.5 26.5 26.5 26.5 26.5 26.5 26.5 26.5 26.5 26.5 26.5 26.5 26.5 26.5 26.5 26.5 26.5 26.5 26.5 26.5 28.0 NODE TYPE PRESSURE (PSI) SOURCE 62.9 62.8 62.7 52.7 52.5 51. 0 39.5 39.3 39.3 39.3 39.3 39.2 39.2 39.2 39.2 39.2 39.2 39.2 39.2 39.1 37.8 37.8 37.8 37.7 37.7 37.6 37.4 37.3 37.0 37.1 37.1 37.1 39.1 36.5 610.5 GPM 250.0 GPM 0.0 GPM 360.5 GPM DISCHARGE (GPM) 360.5 --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 JOB TITLE:·CARLSBJ\D RESEARCH/BELOW MEZZ .20/1500 06/22/99 NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 35 28.0 ----36.3 --- 36 28.0 35.1 --- 37 11. 0 ----40.4 --- 38 11.0 18.0 --- 39 11. 0 ----16.9 --- 40 11.0 16.3 --- 41 11. 0 ----16.0 --- 42 11.0 16.0 --- 301 28.0 ----37.3 --- 302 28.0 -' ---37.2 --- 303 28.0 ----37.2 --- 304 28.0 ----37.1 --- 305 28.0 ----37.1 --- 306 28.0 ----37.0 --- 307 28.0 ----37.3 --- 308 28.0 ----37.2 --- 309 28.0 37.2 --- 310 28.0 37.1 --- 311 28.0 37.1 --- 312 28.0 ----37.0 --- 313 28.0 37.2 --- 314 28.0 ----37.2 --- 315 28.0 37.1 --- 316 28.0 ----37.1 --- 201 28.0 ----37.5 --- 202 28.0 ----37.4 --- 203 28.0 ----37.4 --- 204 28.0 ----37.3 --- 205 28.0 ----37.3 --- 206 28.0 37.2 --- 207 28.0 ----37.2 --- 208 28.0 ----37.1 --- 209 28.0 ----37.1 --- 210 28.0 37.5 --- 211 28.0 ----37.4 --- 212 28.0 ----37.4 --- 213 28.0 ----37.3 --- 214 28.0 ----37.3 --- 215 28.0 ----37.2 --- 216 28.0 ----37.2 --- 217 28.0 ----37.1 --- 218 28.0 ----37.1 --- 219 28.0 ----37.6 --- 220 28.0 ----37.6 --- 221 28.0 ----37.5 --- 222 28.0 ----37.5 --- 223 28.0 37.4 --- 224 28.0 37.4 --- 225 28.0 ----37.3 --- 226 28.0 37.3 --- 227 28.0 ----37.3 --- 228 28.0 37.7 --- 229 28.0 37.6 --- 230 28.0 37.6 --- SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 JOB TITLE: CARLSBAD RESEARCH/BELOW MEZZ .20/1500 06/22/99 NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 231 28.0 ----37.5 --- 232 28.0 ----37.5 --- 101 11. 0 K= 5.50 13.7 20.3 102 11. 0 K= 5.50 14.6 21. 0 103 11. 0 K= 5.50 15.2 21. 5 104 11. 0 K= 5.50 14.3 20.8 105 11. 0 K= 5.50 13.7 20.4 106 11. 0 K= 5.50 14.6 21. 0 107 11. 0 K= 5.50 14.3 20 ·. 8 108 11. 0 K= 5.50 15.3 21. 5 109 11. 0 K= 5.50 13.9 20.5 110 11.0 K= 5.50 14.8 21. 2 111 11. 0 K= 5.50 15.5 21. 7 112 11.0 K= 5.50 14.5 21. 0 113 11. 0 K= 5.50 14.4 20.9 114 11. 0 K= 5.50 15.4 21. 6 115 11. 0 K= 5.50 16.1 22.0 116 11. 0 K= 5.50 15.1 21. 4 117 11. 0 K= 5.50 17.4 22.9 ~PRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 JOB TITLE: CARLSBAD RESEARCH/BELOW MEZZ .20/1500 06/22/99 PIPE DATA PIPE TAG Q(GPM) DIA( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) Pipe: 1 360.5 7.987 PL 80.00 PF 0.1 1 -3.0 ~RCE 62.9 (N/A) 2.3 150 FTG 52.50 PE 0.0 2 -3.0 0.0 62.8 0.0 0.001 TL 132.50 PV 0.0 Pipe: 2 360.4 7.987 PL 5.00 PF 0.0 2 -3.0 0.0 62.8 0.0 2.3 150 FTG 39.30 PE o·. o 3 -3.0 0.0 62.7 0.0 0.001 TL 44.30 PV 0.0 Pipe: 3 FIXED PRESSURE LOSS DEVICE 3 -3.0 0.0 62.7 0.0 10.0 psi, 360.4 gpm 4 -3.0 0.0 52.7 0.0 Pipe: 4 360.4 7.987 PL 233.00 PF 0.3 4 -3.0 0.0 52.7 0.0 2.3 150 FTG 39.30 PE 0.0 5 -3.0 0.0 52.5 0.0 0.001 TL 272.30 PV 0.0 Pipe: 5 360.4 8.510 PL 8.00 PF 0.0 5 -3.0 0.0 52.5 0.0 2.0 140 FTG 17.30 PE 1. 5 6 0.5 0.0 51. 0 0.0 0.001 TL 25.30 PV 0.0 Pipe: 6 360.4 6.403 PL 26.50 PF 0.2 6 0.5 0.0 51. 0 0.0 3.6 120 FTG L PE 11. 3 7 26.5 0.0 39.5 0.0 0.004 TL 37.80 PV 0.1 Pipe: 7 360.4 6.403 PL 22.00 PF 0.2 7 26.5 0.0 39.5 0.0 3.6 120 FTG T PE 0.0 10 26.5 0.0 39.3 0.0 0.004 TL 59.70 PV 0.1 Pipe: 8 -23.5 6.403 PL 12.00 PF 0.0 8 26.5 0.0 39.3 0.0 0.2 120 FTG PE 0.0 9 26.5 0.0 39.3 0.0 0.000 TL 12.00 PV 0.0 Pipe: 9 -47.0 6.403 PL 6.50 PF 0.0 9 26.5 0.0 39.3 0.0 0.5 120 FTG T PE 0.0 10 26.5 0.0 39.3 0.0 0.000 TL 44.20 PV 0.0 Pipe: 10 289.9 6.403 PL 5.50 PF 0.0 10 26.5 0.0 39.3 0.0 2.9 120 FTG PE 0.0 11 26.5 0.0 39.3 0.0 0.003 TL 5.50 PV 0.1 Pipe: 11 266.3 6.403 PL 12.00 PF 0.0 11 26.5 0.0 39.3 0.0 2.7 120 FTG PE 0.0 12 26.5 0.0 39.2 0.0 0.002 TL 12.00 PV 0.0 Pipe: 12 242.7 6.403 PL 12.00 PF 0.0 12 26.5 0.0 39.2 0.0 2.4 120 FTG PE 0.0 13 26.5 0.0 39.2 0.0 0.002 TL 12.00 PV 0.0 Pipe: 13 219.0 6.403 PL 12.00 PF 0.0 13 26.5 0.0 39.2 0.0 2.2 120 FTG PE 0.0 14 26.5 0.0 39.2 0.0 0.002 TL 12.00 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 JOB TITLE: CARLSBJ\D RESEARCH/BELOW MEZZ .20/1500 06/22/99 PIPE DATA (cont'q) PIPE TAG Q(GPM) DIA( IN) LENGTH PRESS. END ELEV. ~oz. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) Pipe: 14 195.0 6.403 PL 12.00 PF 0.0 14 26.5 0.0 39.2 0.0 1. 9 120 FTG PE 0.0 15 26.5 0.0 39.2 0.0 0.001 TL 12.00 PV 0.0 Pipe: 15 169.0 6.403 PL 12.00 PF 0.0 15 26.5 0.0 39.2 0.0 1. 7 120 FTG PE 0.0 16 26.5 0.0 39.2 0.0 0.001 TL 12.00 PV 0.0 Pipe: 16 142.4 6.403 PL 12.00 PF 0.0 16 26.5 0.0 39.2 0.0 1. 4 120 FTG PE 0.0 17 26.5 0.0 39.2 0.0 0.001 TL 12.00 PV 0.0 Pipe: 17 113.9 6.403 PL 12.00 PF 0.0 17 26.5 0.0 39.2 0.0 1.1 120 FTG PE 0.0 18 26.5 0.0 39.2 0.0 0.000 TL 12.00 PV 0.0 Pipe: 18 85.6 6.403 PL 13.54 PF 0.0 18 26.5 0.0 39.2 0.0 0.9 120 FTG PE 0.0 19 26.5 0.0 39.2 0.0 0.000 TL 13.54 PV 0.0 Pipe: 19 57.5 6.403 PL 36.00 PF 0.0 19 26.5 0.0 39.2 0.0 0.6 120 FTG L PE 0.0 20 26.5 0.0 39.1 0.0 0.000 TL 47.30 PV 0.0 Pipe: 20 27.9 6.403 PL 13.00 PF 0.0 20 26.5 0.0 39.1 0.0 0.3 120 FTG L PE 0.0 33 26.5 0.0 39.1 0.0 0.000 TL 24.30 PV 0.0 Pipe: 21 23.5 4.328 PL 12.00 PF 0.0 21 26.5 0.0 37.8 0.0 0.5 120 FTG PE 0.0 22 26.5 0.0 37.8 0.0 0.000 TL 12.00 PV 0.0 Pipe: 22 70.6 4.328 PL 12.00 PF 0.0 22 26.5 0.0 37.8 0.0 1. 5 120 FTG PE 0.0 23 26.5 0.0 37.8 0.0 0.001 TL 12.00 PV 0.0 Pipe: 23 94.1 4.328 PL 12.00 PF 0.0 23 26.5 0.0 37.8 0.0 2.1 120 FTG PE 0.0 24 26.5 0.0 37.7 0.0 0.002 TL 12.00 PV 0.0 Pipe: 24 117.7 4.328 PL 12.00 PF 0.0 24 26.5 0.0 37.7 0.0 2.6 120 FTG PE 0.0 25 26.5 0.0 37.7 0.0 0.003 TL 12.00 PV 0.0 Pipe: 25 141. 4 4.328 PL 12.00 PF 0.1 25 26.5 0.0 37.7 0.0 3.1 120 FTG PE 0.0 26 26.5 0.0 37.6 0.0 0.005 TL 12.00 PV 0.1 Pipe: 26 165.5 4.328 PL 20.50 PF 0.2 26 26.5 0.0 37.6 0.0 3.6 120 FTG 2L PE 0.0 27 26.5 0.0 37.4 0.0 0.007 TL 37.50 PV 0.1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 JOB TITLE: CARLSBl\D RESEARCH/BELOW MEZZ .20/1500 06/22/99 PIPE DATA (cont'd) PIPE TAG Q(GPM) DIA( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) Pipe: 27 191.4 4.328 PL 12.00 PF 0.1 27 26.5 0.0 37.4 0.0 4.2 120 FTG PE 0.0 28 26.5 0.0 37.3 0.0 0.009 TL 12.00 PV 0.1 Pipe: 28 218.0 4.328 PL 1.00 PF 0.3 28 26.5 0.0 37.3 0.0 4.8 120 FTG T PE 0.6 35 28.0 0.0 36.3 0.0 0.011 TL 29.50 PV 0.2 Pipe: 29 -142.4 4.328 PL 11. 00 PF 0.1 35 28.0 0.0 36.3 0.0 3.1 120 FTG PE 0.6 29 26.5 0.0 37.0 0.0 0.005 TL 11.00 PV 0.1 Pipe: 30 -113.9 4.328 PL 12.00 PF 0.0 29 26.5 0.0 37.0 0.0 2.5 120 FTG PE 0.0 30 26.5 0.0 37.1 0.0 0.003 TL 12.00 PV 0.0 Pipe: 31 -85.6 4.328 PL 12.00 PF 0.0 30 26.5 0.0 37.1 0.0 1. 9 120 FTG PE 0.0 31 26.5 0.0 37.1 0.0 0.002 TL 12.00 PV 0.0 Pipe: 32 -57.5 4.328 PL 12.00 PF 0.0 31 26.5 0.0 37.1 0.0 1. 3 120 FTG PE 0.0 32 26.5 0.0 37.1 0.0 0.001 TL 12.00 PV 0.0 Pipe: 33 -27.9 4.328 PL 12.00 PF 0.0 32 26.5 0.0 37.1 0.0 0.6 120 FTG PE 0.6 34 28.0 0.0 36.5 0.0 0.000 TL 12.00 PV 0.0 Pipe: 34 27.9 2.227 PL 156.00 PF 1. 2 33 26.5 0.0 39.1 0.0 2.3 120 FTG 2T4L PE 0.6 301 28.0 0.0 37.3 0.0 0.006 TL 202.00 PV 0.0 Pipe: 35 27.9 2.227 PL 8.00 PF 0.0 301 28.0 0.0 37.3 0.0 2.3 120 FTG PE 0.0 302 28.0 0.0 37.2 0.0 0.006 TL 8.00 PV 0.0 Pipe: 36 27.9 2.227 PL 8.00 PF 0.0 302 28.0 0.0 37.2 0.0 2.3 120 FTG PE 0.0 303 28.0 0.0 37.2 0.0 0.006 TL 8.00 PV 0.0 Pipe: 37 27.9 2.227 PL 8.00 PF 0.0 303 28.0 0.0 37.2 0.0 2.3 120 FTG PE 0.0 304 28.0 0.0 37.1 0.0 0.006 TL 8.00 PV 0.0 Pipe: 38 27.9 2.227 PL 8.00 PF 0.0 304 28.0 0.0 37.1 0.0 2.3 120 FTG PE 0.0 305 28.0 0.0 37.1 0.0 0.006 TL 8.00 PV 0.0 Pipe: 39 27.9 2.227 PL 8.00 PF 0.0 305 28.0 0.0 37.1 0.0 2.3 120 FTG PE 0.0 306 28.0 0.0 37.0 0.0 0.006 TL 8.00 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 JOB TITLE: CARLSBAD RESEARCH/BELOW MEZZ .20/1500 06/22/99 PIPE DATA (cont'd) PIPE TAG Q(GPM) DIA( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) Pipe: 40 27.9 2.227 PL 52.00 PF 0.5 306 28.0 0.0 37.0 0.0 2.3 120 FTG 2T2L PE 0.0 34 28.0 0.0 36.5 0.0 0.006 TL 89.40 PV 0.0 Pipe: 41 29.7 2.227 PL 156.00 PF 1. 2 20 26.5 0.0 39.1 0.0 2.4 120 FTG TL PE 0.6 307 28.0 0.0 37.3 0.0 0.007 TL 174.70 PV 0.0 Pipe: 42 29.7 2.227 PL 8.00 PF 0.1 307 28.0 0.0 37.3 0.0 2.4 120 FTG PE 0.0 308 28.0 0.0 37.2 0.0 0.007 TL 8.00 PV 0.0 Pipe: 43 29.7 2.227 PL 8.00 PF 0.1 308 28.0 0.0 37.2 0.0 2.4 120 FTG PE 0.0 309 28.0 0.0 37.2 0.0 0.007 TL 8.00 PV 0.0 Pipe: 44 29.7 2.227 PL 8.00 PF 0.1 309 28.0 0.0 37.2 0.0 2.4 120 FTG PE 0.0 310 28.0 0.0 37.1 0.0 0.007 TL 8.00 PV 0.0 Pipe: 45 29.7 2.227 PL 8.00 PF 0.1 310 28.0 0.0 37.1 0.0 2.4 120 FTG PE 0.0 311 28.0 0.0 37.1 0.0 0.007 TL 8.00 PV 0.0 Pipe: 46 29.7 2.227 PL 8.00 PF 0.1 311 28.0 0.0 37.1 0.0 2.4 120 FTG PE 0.0 312 28.0 0.0 37.0 0.0 0.007 T~ 8.00 PV 0.0 Pipe: 47 29.7 2.227 PL 52.00 PF 0.6 312 28.0 0.0 37.0 0.0 2.4 120 FTG 2T PE 0.6 32 26.5 0.0 37.1 0.0 0.007 TL 80.80 PV 0.0 Pipe: 48 28.1 2.227 PL 180.00 PF 1. 3 19 26.5 0.0 39.2 0.0 2.3 120 FTG 2T PE 0.6 313 28.0 0.0 37.2 0.0 0.006 TL 208.80 PV 0.0 Pipe: 49 28.1 2.227 PL 8.00 PF 0.0 313 28.0 0.0 37.2 0.0 2.3 120 FTG PE 0.0 314 28.0 0.0 37.2 0.0 0.006 TL 8.00 PV 0.0 Pipe: 50 28.1 2.227 PL 8.00 PF 0.0 314 28.0 0.0 37.2 0.0 2.3 120 FTG PE 0.0 315 28.0 0.0 37.1 0.0 0.006 TL 8.00 PV 0.0 Pipe: 51 28.1 2.227 PL 8.00 PF 0.0 315 28.0 0.0 37.1 0.0 2.3 120 FTG PE 0.0 316 28.0 0.0 37.1 0.0 0.006 TL 8.00 PV 0.0 Pipe: 52 28.1 2.227 PL 68.00 PF 0.6 316 28.0 0.0 37.1 0.0 2.3 120 FTG 2T PE 0.6 31 26.5 0.0 37.1 0.0 0.006 TL 96.80 PV 0.0 I' I l "lt I "I I ti f l'l''I I 11 I '' I I 1'1 I I I• I If' 1·1 I ,,,,,, ... SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 JOB TITLE: CARLSBAD RESEARCH/BELOW MEZZ .20/1500 06/22/99 PIPE DATA (cont'q) PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) Pipe: 53 28.2 2.227 PL 132.00 PF 1.0 18 26.5 0.0 39.2 0.0 2.3 120 FTG 2T PE 0.6 201 28.0 0.0 37.5 0.0 0.006 TL 160.80 PV 0.0 Pipe: 54 28.2 2.227 PL 8.00 PF 0.1 201 28.0 0.0 37.5 0.0 2.3 120 FTG PE 0.0 202 28.0 0.0 37.4 0.0 0.006 TL 8.00 PV 0.0 Pipe: 55 28.2 2.227 BL 8.00 PF 0.1 202 28.0 0.0 37.4 0.0 2.3 120 FTG PE 0.0 203 28.0 0.0 37.4 0.0 0.006 TL 8.00 PV 0.0 Pipe: 56 28.2 2.227 PL 8.00 PF 0.1 203 28.0 0.0 37.4 0.0 2.3 120 FTG PE 0.0 204 28.0 0.0 37.3 0.0 0.006 TL 8.00 PV 0.0 Pipe: 57 28.2 2.227 PL 8.00 PF 0.1 204 28.0 0.0 37.3 0.0 2.3 120 FTG PE 0.0 205 28.0 0.0 37.3 0.0 0.006 TL 8.00 PV 0.0 Pipe: 58 28.2 2.227 PL 8.00 PF 0.1 205 28.0 0.0 37.3 0.0 2.3 120 FTG PE 0.0 206 28.0 0.0 37.2 0.0 0.006 TL 8.00 PV 0.0 Pipe: 59 28.2 2.227 PL 8.00 PF 0.1 206 28.0 0.0 37.2 0.0 2.3 120 FTG PE 0.0 207 28.0 0.0 37.2 0.0 0.006 TL 8.00 PV 0.0 Pipe: 60 28.2 2.227 PL 8.00 PF 0.1 207 28.0 0.0 37.2 0.0 2.3 120 FTG PE 0.0 208 28.0 0.0 37.1 0.0 0.006 TL 8.00 PV 0.0 Pipe: 61 28.2 2.227 PL 8.00 PF 0.1 208 28.0 0.0 37.1 0.0 2.3 120 FTG PE 0.0 209 28.0 0.0 37.1 0.0 0.006 TL 8.00 PV 0.0 Pipe: 62 28.2 2.227 PL 78.00 PF 0.7 209 28.0 0.0 37.1 0.0 2.3 120 FTG 2T PE 0.6 30 26.5 0.0 37.1 0.0 0.006 TL 106.80 PV 0.0 Pipe: 63 28.5 2.227 PL 132.00 PF 1.0 17 26.5 0.0 39.2 0.0 2.4 120 FTG 2T PE 0.6 210 28.0 0.0 37.5 0.0 0.006 TL 160.80 PV 0.0 Pipe: 64 28.5 2.227 PL 8.00 PF 0.1 210 28.0 0.0 37.5 0.0 2.4 120 FTG PE 0.0 211 28.0 0.0 37.4 0.0 0.006 TL 8.00 PV 0.0 Pipe: 65 28.5 2.227 PL 8.00 PF 0.1 211 28.0 0.0 37.4 0.0 2.4 120 FTG PE 0.0 212 28.0 0.0 37.4 0.0 0.006 TL 8.00 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 JOB TITLE: CARLSBAD RESEARCH/BELOW MEZZ .20/1500 06/22/99 PIPE DATA (cont'd) PIPE TAG Q(GPM) DIA( IN) LENGTH PRESS. END ELEV. N:OZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) Pipe: 66 28.5 2.227 PL 8.00 PF 0.1 212 28.0 0.0 37.4 0.0 2.4 120 FTG PE 0.0 213 28.0 0.0 37.3 0.0 0.006 TL 8.00 PV 0.0 Pipe: 67 28.5 2.227 PL 8.00 PF 0.1 213 28.0 0.0 37.3 0.0 2.4 120 FTG PE 0.0 214 28.0 0.0 37.3 0.0 0.006 TL 8.00 PV 0.0 Pipe: 68 28.5 2.227 PL 8.00 PF 0.1 214 28.0 0.0 37.3 0.0 2.4 120 FTG PE 0.0 215 28.0 0.0 37.2 0.0 0.006 TL 8.00 PV 0.0 Pipe: 69 28.5 2.227 PL 8.00 PF 0.1 215 28.0 0.0 37.2 0.0 2.4 120 FTG PE 0.0 216 28.0 0.0 37.2 0.0 0.006 TL 8.00 PV 0.0 Pipe: 70 28.5 2.227 PL 8.00 PF 0.1 216 28.0 0.0 37.2 0.0 2.4 120 FTG PE 0.0 217 28.0 0.0 37.1 0.0 0.006 TL 8.00 PV 0.0 Pipe: 71 28.5 2.227 PL 8.00 PF 0.1 217 28.0 0.0 37.1 0.0 2.4 120 FTG PE 0.0 218 28.0 0.0 37.1 0.0 0.006 TL 8.00 PV 0.0 Pipe: 72 28 ._5 2.227 PL 78.00 PF 0.7 218 28.0 0.0 37.1 0.0 2.4 120 FTG 2T PE 0.6 29 26.5 0.0 37.0 0.0 0.006 TL 106.80 PV 0.0 Pipe: 73 26.6 2.227 PL 132.00 PF 0.9 16 26.5 0.0 39.2 0.0 2.2 120 FTG 2T PE 0.6 219 28.0 0.0 37.6 0.0 0.006 TL 160.80 PV 0.0 Pipe: 74 26.6 2.227 PL 8.00 PF 0.0 219 28.0 0.0 37.6 0.0 2.2 120 FTG PE 0.0 220 28.0 0.0 37.6 0.0 0.006 TL 8.00 PV 0.0 Pipe: 75 26.6 2.227 PL 8.00 PF 0.0 220 28.0 0.0 37.6 0.0 2.2 120 FTG PE 0.0 221 28.0 0.0 37.5 0.0 0.006 TL 8.00 PV 0.0 Pipe: 76 26.6 2.227 PL 8.00 PF 0.0 221 28.0 0.0 37.5 0.0 2.2 120 FTG PE 0.0 222 28.0 0.0 37.5 0.0 0.006 TL 8.00 PV 0.0 Pipe: 77 26.6 2.227 PL 8.00 PF 0.0 222 28.0 0.0 37.5 0.0 2.2 120 FTG PE 0.0 223 28.0 0.0 37.4 0.0 0.006 TL 8.00 PV 0.0 Pipe: 78 26.6 2.227 PL 8.00 PF 0.0 223 28.0 0.0 37.4 0.0 2.2 120 FTG PE 0.0 224 28.0 o.o 37.4 0.0 0.006 TL 8.00 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 JOB TITLE: CARLSBAD RESEARCH/BELOW MEZZ .20/1500 06/22/99 PIPE DATA (cont'q) PIPE TAG Q(GPM) DIA( IN) LENGTH PRESS. END ELEV. ~uz. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) Pipe: 79 26.6 2.227 PL 8.00 PF 0.0 224 28.0 0.0 37.4 0.0 2.2 120 FTG PE 0.0 225 28.0 0.0 37.3 0.0 0.006 TL 8.00 PV 0.0 Pipe: 80 26.6 2.227 PL 8.00 PF 0.0 225 28.0 0.0 37.3 0.0 2.2 120 FTG PE 0.0 226 28.0 0.0 37.3 0.0 0.006 TL 8.00 PV 0.0 Pipe: 81 26.6 2.227 PL 8.00 PF 0.0 226 28.0 0.0 37.3 0.0 2.2 120 FTG PE 0.0 227 28.0 0.0 37.3 0.0 0.006 TL 8.00 PV 0.0 Pipe: 82 26.6 2.227 PL 78.00 PF 0.6 227 28.0 0.0 37.3 0.0 2.2 120 FTG 2T PE 0.6 28 26.5 0.0 37.3 0.0 0.006 TL 106.80 PV 0.0 Pipe: 83 26.0 2.227 PL 132.00 PF 0.9 15 26.5 0.0 39.2 0.0 2.1 120 FTG 2T PE 0.6 228 28.0 0.0 37.7 0.0 0.005 TL 160.80 PV 0.0 Pipe: 84 26.0 2.227 PL 8.00 PF 0.0 228 28.0 0.0 37.7 0.0 2.1 120 FTG PE 0.0 229 28.0 0.0 37.6 0.0 0.005 TL 8.00 PV 0.0 Pipe: 85 26.0 2.227 PL 8.00 PF 0.0 229 28.0 0.0 37.6 0.0 2.1 120 FTG PE 0.0 230 28.0 0.0 37.6 0.0 0.005 TL 8.00 PV 0.0 ... Pipe: 86 26.0 2.227 PL 8.00 PF 0.0 230 28.0 0.0 37.6 0.0 2.1 120 FTG PE 0.0 231 28.0 0.0 37.5 0.0 0.005 TL 8.00 PV 0.0 Pipe: 87 26.0 2.227 PL 8.00 PF 0.0 231 28.0 0.0 37.5 0.0 2.1 120 FTG PE 0.0 232 28.0 0.0 37.5 0.0 0.005 TL 8.00 PV 0.0 Pipe: 88 26.0 2.227 PL 109.00 PF 0.7 232 28.0 0.0 37.5 0.0 2.1 120 FTG 2T PE 0.6 27 26.5 0.0 37.4 0.0 0.005 TL 137.80 PV 0.0 Pipe: 89 24.0 2.227 PL 274.50 PF 1. 6 14 26.5 0.0 39.2 0.0 2.0 120 FTG 4T PE 0.0 26 26.5 0.0 37.6 0.0 0.005 TL 332.10 PV 0.0 Pipe: 90 23.7 2.227 PL 274.50 PF 1. 5 13 26.5 0.0 39.2 0.0 2.0 120 FTG 4T PE 0.0 25 26.5 0.0 37.7 0.0 0.005 TL 332.10 PV 0.0 Pipe: 91 23.6 2.227 PL 274.50 PF 1. 5 12 26.5 0.0 39.2 0.0 1. 9 120 FTG 4T PE 0.0 24 26.5 0.0 37.7 0.0 0.005 TL 332.10 PV 0.0 7 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 JOB TITLE: CARLSBJ\D RESEARCH/BELOW MEZZ .20/1500 06/22/99 PIPE DATA (cont'q) PIPE TAG Q(GPM) DIA( IN) LENGTH PRESS. END ELEV. ~uz. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) Pipe: 92 23.6 2.227 PL 274.50 PF 1. 5 11 26.5 0.0 39.3 0.0 1. 9 120 FTG 4T PE 0.0 23 26.5 0.0 37.8 0.0 0.005 TL 332.10 PV 0.0 Pipe: 93 23.6 2.227 PL 274.50 PF 1. 5 10 26.5 0.0 39.3 0.0 1. 9 120 FTG 4T PE 0.0 22 26.5 0.0 37.8 0.0 0.005 TL 332.10 PV 0.0 Pipe: 94 23.5 2.227 PL 274.50 PF 1. 5 9 26.5 0.0 39.3 0.0 1. 9 120 FTG 4T PE 0.0 22 26.5 0.0 37.8 0.0 0.004 TL 332.10 PV 0.0 Pipe: 95 23.5 2.227 PL 274.50 PF 1. 5 8 26.5 0.0 39.3 0.0 1. 9 120 FTG 4T PE 0.0 21 26.5 0.0 37.8 0.0 0.004 TL 332.10 PV 0.0 Pipe: 96 360.4 3.356 PL 5.00 PF 1. 2 35 28.0 0.0 36.3 0.0 13.1 120 FTG L PE 0.0 36 28.0 0.0 35.1 0.0 0.095 TL 12.70 PV 1.1 Pipe: 97 360.4 3.356 PL 14.50 PF 2.1 36 28.0 0.0 35.1 0.0 13.1 120 FTG L PE 7.4 37 11. 0 0.0 40.4 0.0 0.095 TL 22.20 PV 1.1 Pipe: 98 360.4 3.356 PL 212.00 PF 22.3 37 11. 0 0.0 40.4 0.0 13.1 120 FTG 3L PE 0.0 38 11. 0 0.0 18.0 0.0 0.095 TL 235.10 PV 1.1 Pipe: 99 337.5 3.356 PL 14.00 PF 1. 2 38 11. 0 0.0 18.0 0.0 12.2 120 FTG PE 0.0 39 11.0 0.0 16.9 0.0 0.084 TL 14.00 PV 1.0 Pipe: 100 251.7 3.356 PL 12.00 PF 0.6 39 11. 0 0.0 16.9 0.0 9.1 120 FTG PE 0.0 40 11.0 0.0 16.3 0.0 0.049 TL 12.00 PV 0.6 Pipe: 101 167.3 3.356 PL 10.00 PF 0.2 40 11.0 0.0 16.3 0.0 6.1 120 FTG PE 0.0 41 11. 0 0.0 16.0 0.0 0.023 TL 10.00 PV 0.2 Pipe: 102 83.6 3.356 PL 8.50 PF 0.1 41 11. 0 0.0 16.0 0.0 3.0 120 FTG PE 0.0 42 11. 0 0.0 16.0 0.0 0.006 TL 8.50 PV 0.1 Pipe: 103 20.3 1.104 PL 8.75 PF 0.9 102 11.0 5.5 14.6 21. 0 6.8 120 FTG PE 0.0 101 11. 0 5.5 13.7 20.3 0.105 TL 8.75 PV 0.3 Pipe: 104 41. 3 1.452 PL 7.75 PF 1. 4 42 11. 0 0.0 16.0 0.0 8.0 120 FTG 6.00 PE 0.0 102 11.0 5.5 14. 6' 21. 0 0.102 TL 13.75 PV 0.4 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 t JOB TITLE: CARLSBAD RESEARCH/BELOW MEZZ .20/1500 06/22/99 PIPE DATA (cont'd) PIPE TAG Q(GPM) DIA( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) Pipe: 105 20.8 1.104 PL 8.75 PF 1.0 103 11. 0 5.5 15.2 21. 5 7.0 120 FTG PE 0.0 104 11. 0 5.5 14.3 20.8 0.109 TL 8.75 PV 0.3 Pipe: 106 42.3 1.452 PL 1.00 PF 0.7 42 11. 0 0.0 16.0 0.0 8.2 120 FTG 6.00 PE 0.0 103 11. 0 5.5 15.2 21. 5 0.107 TL 7.00 PV 0.5 Pipe: 107 20.4 1.104 PL 8.75 PF 0.9 106 11. 0 5.5 14.6 21. 0 6.8 120 FTG PE 0.0 105 11.0 5.5 13.7 20.4 0.105 TL 8.75 PV 0.3 Pipe: 108 41. 4 1. 452 PL 7.75 PF 1. 4 41 11. 0 0.0 16.0 0.0 8.0 120 FTG 6.00 PE 0.0 106 11. 0 5.5 14.6 21. 0 0.103 TL 13.75 PV 0.4 Pipe: 109 -20.8 1.104 PL 8.75 PF 1.0 107 11. 0 5.5 14.3 20.8 7.0 120 FTG PE 0.0 108 11. 0 5.5 15.3 21. 5 0.109 TL 8.75 PV 0.3 Pipe: 110 42.3 1. 452 PL 1.00 PF 0.7 41 11.0 0.0 16.0 0.0 8.2 120 FTG 6.00 PE 0.0 108 11. 0 5.5 15.3 21. 5 0.107 TL 7.00 PV 0.5 Pipe: 111 20.5 1.104 PL 8.75 PF 0.9 110 11. 0 5.5 14.8 21. 2 6.9 120 FTG PE 0.0 109 11. 0 5.5 13.9 20.5 0.106 TL 8.75 PV 0.3 Pipe: 112 41. 7 1.452 PL 7.75 PF 1. 4 40 11. 0 0.0 16.3 0.0 8.1 120 FTG 6.00 PE 0.0 110 11. 0 5.5 14.8 21. 2 0.104 TL 13.75 PV 0.4 Pipe: 113 21. 0 1.104 PL 8.75 PF 1.0 111 11. 0 5.5 15.5 21. 7 7.0 120 FTG PE 0.0 112 11. 0 5.5 14.5 21. 0 0.111 TL 8.75 PV 0.3 Pipe: 114 42.6 1. 452 PL 1.00 PF 0.8 40 11.0 0.0 16.3 0.0 8.3 120 FTG 6.00 PE 0.0 111 11. 0 5.5 15.5 21. 7 0.108 TL 7.00 PV 0.5 Pipe: 115 20.9 1.104 PL 8.75 PF 1.0 114 11. 0 5.5 15.4 21. 6 7.0 120 FTG PE 0.0 113 11. 0 5.5 14.4 20.9 0.110 TL 8.75 PV 0.3 Pipe: 116 42.5 1. 452 PL 7.75 PF 1. 5 39 11. 0 0.0 16.9 0.0 8.2 120 FTG 6.00 PE 0.0 114 11. 0 5.5 15.4 21. 6 0.107 TL 13.75 PV 0.5 Pipe: 117 21. 4 1.104 PL 8.75 PF 1.0 115 11. 0 5.5 16.1 22.0 7.2 120 FTG PE 0.0 116 11.0 5.5 15.1 21. 4 0.114 TL 8.75 PV 0.3 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 13 ' JOB TITLE: CARLSBAD RESEARCH/BELOW MEZZ .20/1500 PIPE DATA (cont'd) 06/22/99 PIPE TAG Q(GPM) DIA( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) Pipe: 118 43.4 1. 452 PL 1.00 PF 0.8 39 11. 0 0.0 16.9 0.0 8.4 120 FTG 6.00 PE 0.0 115 11.0 5.5 16.1 22.0 0.112 TL 7.00 PV 0.5 Pipe: 120 22.9 1.104 PL 5.00 PF 0.7 38 11.0 0.0 18.0 0.0 7.7 120 FTG PE 0.0 117 11. 0 5.5 17.4 22.9 0.131 TL 5.00 PV 0.4 NOTES: ( 1 ) Calculations were performed by the HASS 5.5.0 computer program under license no. 8926J521 granted by HRS Systems, Inc. 2193 Ranchwood Dr., N.E. Atlanta, GA 30345 (2) The system h~s been balanced to provide an average imbalance at each node of 0.001 gpm and a maximum imbalance at any node of 0.098 gpm. (3) Velocity pressures are printed for information only, and are not used in balancing the system. Maximum water velocity in any pipe is 13.1 ft/sec. (4) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: F MATERIAL: DFLO HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A Ell Tee LNGELL CHKVLV BFYVLV GATVLV ALMVLV 2.227 7. 20 14.40 4.30 15.80 8.60 1. 40 14.40 4.328 11.20 28.50 8.50 31. 30 17.10 2.80 28.50 6.403 1 . 60 37.70 11. 30 40.20 12.60 3.80 35.20 D DPVLV 14.40 14.20 23.90 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 14 • JOB TITLE: CARLSBAD WATER SUPPLY CURVE RESEARCH/BELOW MEZZ .20/1500 ~ 06/22/99 p R E s s u R E ( p s I ) 120+ I I I I I I 110+ *\\\\\\Q\i\\\\\\\\\\ I I I I 100+ I I I I I I 90+ I I I I I I 80+ I I I I I I 70+ I I I I I I 60+ I I I I I I 50+ I I I I I I 40+ I I I I I I 30+ I I I I X ~ ~ 1------------------------------,------------------------------ 20+ LEGEND " I I I I I I 10+ X = Required Water Supply 62.90 psi@ 610.5 gpm I O = Availaole Water Supply l 107.18 psi@ 610.5 gpm I I " " " " " " " ~ lQJ 5 psi@ 1530 gpm Flow Test Point O++-+---+----+-----+------+--------+--------+---------+-----------+ 400 600 800 1000 . 1200 1400 1600 1800 2000 FLOW (GPM) September 28, 1998 1. PRODUCT NAME Viking Micromatic® Model M Sprinkler Styles: Upright, Pendent, and Conventional Manufactured since 1997 2. MANUFACTURER THE VIKING CORPORATION 210 N. Industrial Park Road Hastings, Michigan 49058, U.S.A. Telephone: (616) 945-9501 (877) 384-5464 Fax: (616) 945-9599 e-mail: techsvcs@vikingcorp.com 3. PRODUCT DESCRIPTION The Viking Micromatic® Model M Sprin- kler is a small, thermosensitive glass- bulb spray sprinkler. The sprinkler is available in several styles, finishes, tem- perature ratings, and orifice sizes to meet design requirements. The small frame and rugged 5 mm glass bulb are aesthetically pleasing. Used in conjunc- tion with one of the various corrosion-re- sistant coatings, the unit provides pro- tection against many corrosive environ- ments. In addition, the special polyester or Teflon® coatings can also be used in decorative applications where colors are desired. During fire conditions, the heat-sensitive liquid in the glass bulb expands, causing the bulb to shatter, releasing the pip cap and sealing spring assembly. Water flowing through the sprinkler orifice strikes the sprinkler deflector, forming a uniform spray pattern to extinguish or control the fire. 4. TECHNICAL DATA See Table 2 (page 11 c) and Table 3 (page 11 d) for list of approvals. TECHNICAL DATA ~ 'r .,; igure A.·:,.:.'.,': Maximum spacing: 15 ft. (4,57 m) Minimum spacing: 6 ft (1,8 m) Minimum operating pressure: 7 PSI (48,3 kPa) Glass-bulb fluid temperature rated to -65 °F (-55 °C) Rated 175 PSI (1 207 kPa) water working pressure Factory tested hydrostatically to 500 PSI (3 448 kPa) Spring: USA Patent No. 4,167,974 Materials: Frame -Brass castings UNS-C84400 Deflector -Brass UNS-C26000 Bulb -Glass with glycerin solution; Nominal 5 mm diameter Seal -Teflon® tape Spring -Nickel alloy Screw -Brass UNS-C36000. Pip Cap -Copper UNS-C11000 and Stainless Steel UNS-S30400 Teflon® Sprinklers: Spring -Nickel alloy, exposed Screw -Brass UNS-C36000 Pip Cap -Copper UNS-C 11000 and Stainless Steel UNS-S30400; Teflon® coated Polyester Sprinklers: Spring -Nickel alloy, exposed Screw -Brass UNS-C36000 Pip Cap -Copper UNS-C11000 and Stainless Steel UNS-S30400 Accessories: Sprinkler Wrench Standard Micromatic® Wrench: Part No. 05000CM Wrench for coated and recessed sprinklers: Part No. 07398W Refer to "Sprinkler Accessories" for other accessories. Sprinkler 11 a MIC ROMA TIC® MODELM SPRINKLER Available Finishes: Chrome-Enloy® (patents pending), Brass, Bright Brass, White Polyester, Black Polyester, Black Teflon®, or Wax-Coated Brass or Polyester 5. AVAILABILITY AND SERVICE Viking sprinklers are available through a network of domestic, Canadian, and international distributors. See the Yel- low Pages of the telephone directory for a local distributor (listed under "Sprinklers-Automatic-Fire") or contact The Viking Corporation. Viking Technical Data may be found on The Viking Corporation's Web site at http://www.vikingcorp.com. The Web site may include a more recent edition of this Technical Data page. 6. GUARANTEES For details of warranty, refer to Viking's current price schedule, or contact The Viking Corporation directly. 7. INSTALLATION WARNING: Viking sprinklers are manu- factured and tested to meet the rigid requirements of the approving agency. The sprinklers are designed to be in- stalled in accordance with recognized installation standards. Deviation from the standards or any alteration to the sprinkler after it leaves the factory in- cluding, but not limited to, painting, plat- ing, coating, or modification, may render the sprinkler inoperative and will auto- matically nullify the approval and any guarantee made by The Viking Corpora- tion. A. Sprinklers are to be installed in ac- cordance with the latest published standards of the National Fire Protec- tion Association, Factory Mutual, Loss Prevention Council, Assemblee Pleniere, Verband der Sachver- sicherer or other similar organiza- tions, and also with the provisions of governmental codes, ordinances, and standards whenever applicable. B. Sprinklers must be handled with care. They must be stored in a cool, dry place in their original shipping con- tainer. Never install sprinklers that have been dropped, damaged, or ex- posed to temperatures in excess of the maximum ambient temperature allowed. Never install any glass-bulb sprinkler if the bulb is cracked or if there is a loss of liquid from the bulb. If a glass bulb lacks the appropriate amount of fluid, it should be set aside Note: Units of measure in parentheses may be approximations. Form No. F_100397 Replaces page 13 a-d and page 11 a-d, dated August 3, 1998 (updated list of approvals). Sprinkler 11 b TECHNICAL DATA Sprinkler Nominal Sprinkler Celling Temperature at Sprinkler Bulb Temperature Temperature Rating Max. Ambient Max. Recommended Color3 Classification (Fusing Point) Temp. Allowed1 Ambient Temp.2 Ordinary 135 °F (57 °C) 115 °F (46 °C) 100 °F (38 °c Orange Ordinary 155 °F (68 °C) 135 °F (57 °C 100 °F (38 °C Red Intermediate 175 °F (79 °C) 155 °F (68 °C1 150 °F (65 °C) Yellow Intermediate 200 °F (93 °C) 180 Of (82 °CJ 150 °F (65 °C) Green Intermediate 212 °F (100 °C) 192 °F (88 °C1 150 °F (65 °C) Green High 286 °F (141 °C) 266 °F (130 °C) 225 °F (107 °C) Blue Extra High 360 °F (182 °C) 340 °F (171 °C) 300 °F (149 °C) Mauve Ultra High5 500 °F (260 °C) 480 °F (249 °C) 465 °F (240 °C) Black Sprinkler Finishes: Brass, Bright Brass, Chrome-Enloy®, White Polyester, Black Polyester, and Black Teflon® Corrosion-Resistant Coatlngs4: Polyester and Teflon® In all temperatures, Wax-Coated Brass, and Wax over Polyester in the following temperatures: 135 °F (57 °C) White Wax 175 °F (79 °C) Dark Brown Wax 155 °F (68 °C) Light Brown Wax 200 °F (93 °C) Dark Brown Wax 212 °F (100 °C) Dark Brown Wax FOOTNOTES 1 Based on National Fire Prevention and Control Administration Contract No. 7-34860. 2 Based on NFPA-13. Other limits may apply depending on fire loading, sprinkler location, and other Authority-Having-Jurisdiction requirements. Refer to specific installation standards. 3 Temperature rating is stamped on the deflector. 4 The co~rosion-resistant coatings have passed the standard corrosion test required by the listed approving agencies. These tests cannot and do not represent all possible corrosive environments. Prior to installing, verify through the end user that the coatings are compatible or suitable for the proposed environment. The coatings indicated are applied to the exposed exterior surfaces only and, therefore, cannot be used as open sprinklers. Note that the spring is exposed on the Teflon®-coated sprinkler and the White Polyester sprinkler. 5 Sprinklers of Ultra High temperature rating are intended for use inside ovens, dryers, or similar enclosures with normal operating temperatures above 300 °F (149 °C). Where the ambient temperature around the. Ultra High temperature rated sprinkler is significantly reduced below 300 °F (149 °C), response time of the Ultra High temperature rated sprinkler may be severely retarded. Table 1 and returned to Viking (or an author- ized Viking distributor) for analysis as soon as possible. If the sprinkler is not returned to Viking, it should be destroyed immediately. C. Corrosion-resistant sprinklers must be installed when subject to corrosive atmospheres. When installing cqrro- sion-resistant sprinklers, care must be taken not to damage the corro- sion-resistant coating. Use only the special sprinkler wrench and immedi- ately replace any damaged units. D. Before installation, be sure to have the appropriate sprinkler model and style, with the proper orifice size, temperature rating, and response characteristics. The sprinklers must be installed after the piping is in place to prevent mechanical damage. 1. Install escutcheon (if used), which is designed.to thread onto the ex- ternal threads of the sprinkler. When installing sprinklers using a Model E-1 or Model F-1 Escutch- eon, thread the center adapter ring onto the external threads of the sprinkler. Refer to the "Sprin.- kler Accessories11 section of the Viking Engineering and Design Data book for approved escutch- eons and other accessories. 2. Apply a small amount of pipe-joint compound or tape to the external threads only, taking care not to allow a build-up of compound in the sprinkler orifice. 3. Install the sprinkler on the piping using the special sprinkler wrench only, while taking care not to dam- age the sprinkler operating parts. (Any other type of wrench may damage the unit). DO NOT use the sprinkler deflector to start or thread the sprinkler into a fitting. E. After installation, the entire sprinkler system must be tested in accordance with the recognized installation standards. The test is applied after sprinkler installation to ensure that no damage has occurred to the sprinkler during shipping and installation, and to make sure the unit has been prop- erly tightened. If a thread leak should occur, normally the sprinkler must be removed, new pipe-joint compound or tape applied, and then reinstalled. This is due to the fact that when the joint seal is damaged, the sealing compound or tape is washed out of ·; September 28, 1_998 MICROMATIC® MODEL M SPRINKLER the joint. Air testing the sprinkler pip- ing prior to testing with water may be considered in areas where leakage during testing must be prevented. Refer to to the Installation Guides and the Authority Having Jurisdiction. F. Sprinklers must be protected from mechanical damage. Wet pipe sys- tems must be provided with adequate heat. When installing sprinklers on dry systems, refer to the Installation Guides and the Authority Having Jurisdiction. 8. MAINTENANCE NOTICE: The owner is responsible for maintaining the fire-protection system and devices in proper operating condi- tion. For minimum maintenance and in- spection requirements, refer to the Na- tional Fire Protection Association pam- phlet that describes care and mainte- nance of sprinkler systems. In addition, the Authority Having Jurisdiction may have additional maintenance, testing, and inspection requirements which must be followed. A. Sprinklers must be inspected on a regular basis for corrosion, mechani- cal damage, obstructions, paint, etc. The frequency of the inspections may vary due to corrosive atmospheres, water supplies, and activity around the device. B. Sprinklers that have been painted·or mechanically damaged must be re- placed immediately. Sprinklers showing signs of corrosion shall be tested and/or replaced immediately as required. Micromatic® Model M Sprinklers that are 50 years old shall be tested and/or replaced as re- quired. Sprinklers that have operated cannot be reassembled or re-used, but must be replaced. When replac- ing sprinklers, use only new sprin- klers. C. The sprinkler discharge pattern is critical for proper fire protection. Therefore, nothing should be hung from, attached to, or otherwise ob- struct the discharge pattern. All ob- structions must be immediately re- moved or, if necessary, additional sprinklers installed. D. When replacing existing sprinklers, the system must be removed from service. Refer to the appropriate sys- tem description and/or valve instruc- tions. Prior to removing the system from service, notify all Authorities Having Jurisdiction. Consideration should be given to employment of a fire patrol in the affected area. (continued on page 11 d) ~ September 28, 1998 Thread Nominal Size Orifice N.P.T. B.S.P. lnche 15mm 15 15mm 15 15mm 15 1/2" 17/32 -- 1/2" 17/32 -- 3/4" 17/32 -- 3/4" 17/32 -- 15mm 20 15mm 20 20mm 20 20mm 20 7/16 1/2" 3/8 1/2" 7/16 1/2" 3/8 1/2" 7/16 10mm 10 10mm 10 15mm 3/8 15mm 7/16 -- 15mm 3/8 1/2" 1/2 3/4" 17/32 -- 15mm 15 20mm 20 TECHNICAL DATA MICROMATIC® MODEL M SPRINKLER 5 mm GLASS BULB, STANDARD RESPONSE STANDARD ORIFICE Sprinkler 11 c MICROMATIC® MODELM SPRINKLER See row A ~Er--See row 3 of of Approved I I Approved Temp. Chart A 3 Finish Chart Deflector Nominal Overall Approvals2 S le K-Factor6 Len th Base P/N1 U.S. Metric Inches mm UL C-UL FM NYC3 VdS LPCB 10138 5.5 2.3 --A3 B4 C6 F7 A3 B4 C6 F7 A D5 A3 B4 C6 -- 10139 5.5 2.3 --A3 B4 C6 F7 A3 B4 C6 F7 A 7 D5 F7 A3 B4 C6 A2 A 1 B 10233 5.5 2.3 58 10173 7 9 58 A3 84 C6 A3 84 C6 A7 D5 E1 10174 7 9 58 10193 7 9 58 A3 B4 C6 F7 A3 B4 C6 F7 A7 D5 E1 A3 B4 C6 -- LARGE ORIFICE 10220 8.0 2.4 61 A3 B4 C6 F7 A3 B4 C6 F7 A7 D5 F7 A3 84 4 10223 8.0 11 5 2.4 61 A3 B4 C6 F7 A3 B4 C6 F7 A7 D5 F7 A3 84 10141 8.0 11 5 2.4 61 A3 B4, C6 F7 A3 B4 C6 F7 A7 D5 F7 A3, B4 C6 A2 A1, 88 Pendent4 10142 8.0 11 5 2.4 61 A3 84 C6 F7 A3 84 C6 F7 A7 05 F7 A3 84 C6 A2 1 88 Pendent4 10187 --A3 B4 C6 F7 A3 84 C6 F7 D5 --A 1 88 U ri ht 10190 --A3 84 C6 F7 A3 84 C6 F7 D5 --A 1 88 U ri ht 10169 8.0 11,5 2.4 61 A3, 84, C6 A3, 84, C6 05, E1 A2 A1, 88 Pendent4 10170 8.0 115 2.4 61 A3 84 C6 A3 84 C6 05 E1 A2 A1 88 SMALL ORIFICE 10191 58 A3 84 C6 F7 A3 84 C6 F7 10218 2.7 2.3 A3, B4, C6, F7 A3, B4, C6, F7 A7, D5 A3,84 10219 4.0 2.3 --A3, 84, C6, F7 A3, B4, C6, F7 A3,84 p 10221 2.7 2.3 58 A3 B4 C6 F7 A3 B4 C6 F7 A7 D5 A3 84 Pendent4 10222 4.0 58 A3, B4, C6, F7 A3, 84, C6, F7 A3,84 Pendent4 10175 5 8 2.3 58 A2 A1 B U ri ht 10176 5,8 2.3 58 A2 A1, 88 U r t 10192 58 A3 84 C6 F7 A3 B4 C6 F7 E5 Pendent4 10188 --A3 B4 C6 F7 A3 B4 C6 F7 Pendent4 10189 --A3 B4 C6 F7 A3 B4 C6 F7 CONVENTIONAL Conv. 10227 5.5 2.3 A3 84 C6 A3 84 C6 A2 A1 88 Conv. 10228 8.0 2.4 A3 84 C6 A3 84 C6 A2 A1 88 Conv. 10172 7 9 58 A3 84 C6 A3,B4 C6 A2 A1 88 Conv. 10168 11,5 61 A3, 84, C6 A3,84,C6 A2 A1: 88 APPROVED TEMPERATURES APPROVED FINISHES A-135 °F (57 °C), 155 °F (68 °C), 175 °F (79 °C), 200 °F (93 °C), 286 °F (141 °C), and 360 °F (182 °C) B -135 °F (57 °C), 155 °F (68 °C), 175 °F (79 °C), and 200 °F (93 °C) C -286 °F (141 °C) D -135 °F (57 °C), 155 °F (68 °C), 175 °F (79 °C), 200 °F (93 °C), and 212 °F (100 °C) E -135 °F (57 °C), 155 °F (68 °C), 175 °F (79 °C), 200 °F (93 °C), 212 °F (100 °C), 286 °F (141 °C), and 360 °F (182 °C) F -500 °F (260 °C) 7 FOOTNOTES 1 -Brass, Bright Brass, and Chrome-Enloy® 2 -Brass, Bright Brass, Chrome-Enloy®, White Polyester>, and Black Polyester> ® 3 -Brass, Bright Brass, Chrome-Enloy®, Black Teflon 5, White Polyester>, and Black Polyester5 4 -Wax-Coated Brass and Wax over Polyester (corrosion resistant) 5 -Wax-Coated Brass (corrosion resistant) 6 -200 °F (93 °C) Wax Coating (corrosion resistant); maximum ambient temperature allowed at ceiling = 150 °F (65 °C) 7 -Brass and Chrome-Enloy® 8 -Wax-Coated Brass, Wax Over Polyester, White Polyester, Black Polyester, and Black Teflon 1 Base part number shown. For complete part number, refer to price list. . 2 This table shows the listings and approvals available at the time of printing. Other approvals are in process. Check with the manufacturer for any additional approvals. 3 Approved by the New York City Board of Standards and Appeals, MEA No. 89-92-E, Volume 12. 4 Refer to "Sprinkler Accessories" section for approved escutcheons and other accessories. 5 UL and C-UL approved as a corrosion-resistant sprinkler. 6 Metric K-Factor shown is for use when pressure is measured in kPa. When pressure is measured in BAR, multiply the metric K-Factor shown by 10.0. 7 Sprinklers of Ultra High temperature rating are intended for use inside ovens, dryers, or similar enclosures with normal operating temperatures above 300 °F (149 °C). Where the ambient temperature around the Ultra High temperature rated sprinkler Is significantly reduced below 300 °F (149 °C), response time of the Ultra High temperature rated sprinkler may be severely retarded. Table 2 Sprinkler 11 d TECHNICAL DATA MICROMATIC® MODEL M SPRINKLER 5 mm GLASS BULB, STANDARD RESPONSE September 28, 1998 MICROMATIC® MODELM SPRINKLER KEY See row A :--7 r--See row 3 of of Approved Approved INSTALLED WITH E-1 RECESSED ESCUTCHEON7 Temp. Chart A 3 Finish Chart Thread Nominal Deflector Nominal Overall ApprovaIs2 Size Orifice Style K-Factor8 Length N.P.T. B.S.P. Inches mm Description Base P/N1 U.S. Metric Inches mm UL C-UL FM7 NYC3 VdS LPCB 1/2" --1/2 --Pendent4 10139 5.5 --2.3 --83 83 D1 83 82 83 3/4" --17/32 --Pendent4 10142 8.0 --2.4 --83 83 D1 83 82 83 --15mm --15 Pendent4 10173 --7,9 --58 83 83 D1 --82 83 --20mm --20 Pendent4 10170 --11,5 --61 83 83 D1 --82 83 INSTALLED WITH F-1 ADJUSTABLE ESCUTCHEON6 1/2" --1/2 --Pendent4 10139 5.5 --2.3 --83 83 --83 C1 83 3/4" --17/32 --Pendent4 10142 8.0 --2.4 --83 83 --83 C1 83 --15mm --15 Pendent4 10173 --7,9 --58 --------C1 83 --20mm --20 Pendent4 10170 --11,5 --61 --------C1 83 APPROVED TEMPERATURES APPROVED FINISHES A-135 °F (57 °C), 155 °F (68 °C), 175 °F (79 °C), 1 -Brass, Bright Brass, and Chrome-Enloy® 200 °F (93 °C), 286 °F (141 °C), and 360 °F (182 °C) 2 -Brass, Bright Brass, Chrome-Enloy®, White Polyester5, and Black Polyester5 B -135 Of (57 °C), 155 Of (68 °C), 175 Of (79 °C), 3 -Brass, Bright Brass, Chrome-Enloy®, Black Teflon®5, White Polyester5, and 200 °F (93 °C) and Black Polyester5 C -286 °F (141 °C) 4 -Wax-Coated Brass and Wax over Polyester (corrosion resistant) 5 -Wax-Coated Brass (corrosion resistant) D -135 °F (57 °C), 155 °F (68 °C), 175 °f (79 °C), 6 -200 °f (93 °C) Wax Coating (corrosion resistant); maximum ambient 200 °F (93 °C), and 212 °F (100 °C) temperature allowed at ceiling = 150 °F (65 °C) FOOTNOTES 1 Base part number shown. For complete part number, refer to price list. . 2 This table shows the listings and approvals available at the time of printing. Other approvals are in process. Check with manufacturer for any additional approvals. 3 Approved by the New York City Board of Standards and Appeals, MEA No. 89-92-E, Volume 12. 4 Refer to "Sprinkler Accessories" section for approved escutcheons and other accessories. 5 UL and C-UL approved as a corrosion-resistant sprinkler. 6 E-1 Recessed Escutcheons and F-1 Adjustable Escutcheons must be ordered separately from sprinklers. Refer to the price list. 7 FM approval of recessed standard orifice and large orifice Model M pendent sprinklers with the E-1 Escutcheon is limited to Wet Systems and Preaction Systems qualifying as Wet Systems, for hazard occupancies up to and including Ordinary Hazard Group II. . 8 Metric K-Factor shown is for use when pressure is measured in kPa. When pressure is measured in BAR, multiply the metric K-factor shown by 10.0. Table 3 1. Remove the system from service, drain all water, and relieve all pressure on the piping. 2. Using the special sprinkler wrench, remove the old sprinkler and in- stall the new unit. Care must be taken to ensure that the replace- ment sprinkler is the proper model and style, and has the appropriate orifice size, temperature rating, and response characteri:,tics. A fully stocked spare sprinkler cabi- net should be provided for this purpose. 3. Place the system back in service and secure all valves. Check and repair all leaks. E. Sprinkler systems that have been subjected to a fire must be returned to service as soon as possible. The entire system must be inspected for damage, and repaired or replaced as necessary. Sprinklers that have been exposed to corrosive products of combustion or high ambient tempera- tures, but have not operated, should be replaced. Refer to the Authority Having Jurisdiction for minimum replacement requirements. Replaces page 13 a-d and page 11 a-d, dated August 3, 1998 (updated list of approvals). Form No. F _ 100397 ,Ill ....... • • LOBE® FIRE SPRINKLER CORPORATION EXTENDED COVERAGE ORDINARY HAZARD EXTRA LARGE ORIFICE AUTOMATIC SPRINKLERS M0DELX BULB SPRAY SERIES UPRIGHT • PENDENT PENDENT RECESSED DESCRIPTI0NAND OPERATION The Globe Model X Extended Coverage Ordinary Hazard Extra Large Orifice Sprinkler is a low profile yet durable design which utilizes a 3mm frangible glass ampule as the thermosen- sitive element. While the sprinkler provides an aesthetically pleasing appearance, it serves to protect various areas of coverage. This sprinkl_er seri~s is available in various styles, temperature ratings and several finishes to meet many varying design requirements. The Globe Model X Extended Coverage Ordinary Hazard Extra Large Orifice Sprinkier is to be installed per NFPA 13 guidelines. The heart of Globe's Model X sprinkler proven actuating assembly is a hermetically sealed frangible glass ampule that contains a precisely measured amount of fluid. When heat is absorbed, the. liquid within the bulb expands increasing the internal pressure. At the prescribed temperature the internal pressure within the ampule exceeds the strength of the glass causing the glass to shatter. This results in water discharge which is distributed in a pattern dependent upon deflector style used. \TECHNICALDATA' I Patent Pending. See reverse side for Approvals and Specifications. Temperature Rating· -I 55°F (68°C), I 75°F (79°C), 200°F (93°C), 286°F ( 141 °C). V, Water Working Pressure Rating -175 psi ( 1207 kPa). · Factory tested hydrostatically to 500 psi (3448 kPa) . .. Maximum low temperature glass bulb rating is -67°F (-55°C). · Frame -bronze Deflector .. brass Screw -brass Bulb seat -engineering plastic , O-ring -silicone Bulb -glass with glycerin solution, 3mm. . Escutcheon Assembly -steel EXTENDED COVERAGE ORDINARY HAZARD UPRIGHT EXTENDED COVERAGE ORDINARY HAZARD PENDENT RECESSED EXTENDED COVERAGE ORDINARY HAZARD PENDENT C SPRINKLER TEMPERATURE RATING/CLASSIFICATION and COLOR CODING CLASSIFICATION ORDINARY BULB COLOR ORANGE/RED ~,f.P.A. MAXIMUM CEILING TEMPERATURE • INTERMEDIATE 1 YELLOW/GREEN 3e0c . , 66°C HIGH 4077 AIRPARK DRIVE. STANDISH. MICHIGAN 48658 NOVEMBER 1995 A-15b BLUE 0 l079C 517-846-4583 • FAX 517-846-923 I BULLETIN ASB-E.C.0.H., REV.# I ' EXTENDED COVERAGE ORDINARY HAZARD EXTRA LARGE ORIFICE AUTOMATIC SPRINKLERS M0DELX BULB SPRAY SERIES UPRIGHT • PENDENT PENDENT RECESSED SPECIFICATIONS ORIFICE SIZE NOMINAL "K" FACTOR THREAD SIZE LENGTH FINISHES Factory Bronze *Satin Chrome 5/8" (16 mm) I 1.5 ( 166 metric) 3/4" NPT 2 7/16" (6.19 cm) Bright Chrome White Polyester *Black Polyester *Lead Coated NOTE: METRIC CONVERSIONS ARE APPROXIMATE. ~INISHES AVAILABLE ON SPECIAL ORDER. APPROVALS MiN. DISTANCE 155°F 175°F 200°F 286°F CANADIAN I U.L. STYLE BETWEEN 68°C 1,0c 93°c 1~1oc U.L. SPRINKLERS UPRIGHT II' X X X X X X PENDENT 9' X X X X X X PENDENT RECESSED 9' X X X X X X U.L. LISTING DESIGN DESIGN AREA ORDINARY GROUP I ORDINARY GROUP l OF I COVERAGE MIN. PRESSURE FLOW IN G.P.M. MIN. PRESSURE FLOW IN Feet Meters l ◄x I ◄ ◄.3 X ◄.3 16x 16 ◄.9 X ◄.9 18x 18 5.5 X 5.5 20x20 6.1 x6.I 2" 01A. UIN. MOU: ... CEILINO 1 29/32" OIA. 1•• X 3/4•• CROSS SECTION I LOBE. FIRE SPRINKLER CORPORATION NOVEMBER 1995 P.S.I. 6.3 10.9 18.1 27.2 1/8" ....... 7/IJ" UAX, P.S.I. G.P.M. 29 11.5 39 38 19.7 51 ◄9 3,1.9 65 60 ◄8.◄ 80 ORDERING INFORMATION SPECIFY ~Quantity " Model Number • Style •Orifice "' Temperature • Finishes desired 0 Quantity -Model X Wrenches -PIN 3330 I 0 •Quantity -Model X Recessed Wrenches -PIN 3330 I I GLOBE~ PRODUCT WARRANTY Globe agrees to repair -or replace any of its own manufactured products found to be defective in material or workmanship for a period of one year from date of shipment. For specific details of our warranty please refer to Price List Terms and Conditions of Sale (Our Price List). ◄077 AIRPARK DRIVE, STANDISH, MICHIGAN ◄8658 517-8◄6-◄583 FAX 517-8◄6-923 I PRINTED U.S.A. BULLETIN ASB-E.C.O.H., REV. # I • • • .-ebruary 15, 1996 1. PRODUCT NAME Viking Model M Extra Large Orifice Sprinkler 2. MANUFACTURER THE VIKING CORPORATION 210 N. Industrial Park Road Hastings, Michigan 49058 U.S.A. Telephone: (616) 945-9501 (800) 968-9501 Fax Number: (616) 945-9599 From outside U.S.A. Telephone: + 1 (616) 945-9501 Fax Number: + 1 (616) 945-9599 3. PRODUCT DESCRIPTION The Viking Model M Extra Large Orifice Sprinkler is a thermo-sensitive glass- bulb spray sprinkler. A rugged 5mm glass-bulb, an extra large orifice, and the familiar Model M design, are combined in the standard response Model M Extra Large Orifice Sprinkler. The extra large orifice provides greater flows at lower pressures than those pro- duced by standard orifice or large orifice sprinklers. This feature allows reduced pipe sizing for hydraulically calculated sprinkler systems which require high densities of water. The Model M Extra Large Orifice Sprinkler may eliminate the need for a fire pump or reduce the size of the pump if it is required. On existing systems, replacing large orifice sprinklers with extra large orifice sprin- klers may provide the higher densities required to allow an increase in the haz- ard classification of an occupancy . Viking Model M Extra Large Orifice Sprinklers are available in both upright and pendent styles with finishes and temperature ratings to meet desiin re- quirements. The special Teflon and polyester coatings can be used in deco- rative applications where colors are de- sired. In addition, these two finishes are corrosion resistant and provide protec- tion against many corrosive environ- ments. During fire conditions, the heat sensitive liquid in the glass-bulb expands, causing the bulb to shatter, releasing the pip cap and sealing spring assembly. The water flowing through the sprinkler orifice strikes the sprinkler deflector forming a uniform spray pattern to extinguish or control the fire. Viking Model M Extra Large Orifice Sprinklers may be ordered and/or used as open sprinklers (glass-bulb and pip cap assembly removed) on deluge sys- tems. TECHNICAL DATA The Viking Model M Extra Large Orifice Upright Sprinkler is UL listed and FM Approved for use in High Piled Storage Occupancies. See Approval Chart and Figure A. When acceptable to the Authority Having Jurisdiction, Viking Model M Extra Large Orifice Upright sprinklers may be used to protect single, double, multiple-row, and portable rack storage of Class I-IV group A and B plastics, cartoned, expanded or unexpantled, as well as exposed unexpanded with: a maximum storage height of , ' 20 ft. (6,1 m), a maximum ceiling height of 25 ft. (7,6 m), 36 inches (914,4 mm) minimum deflector to top of storage clearance, design density of 0.60 gpm/sq. ft. (24,5 I/min/sq. meter), and a design area of 2000 sq. ft. (186 sq. meters) for wet systems or 2600 sq. ft. (242 sq. meters), for dry systems. Sprinkler 13 e MODELM EXTRA LARGE ORIFICE SPRINKLER Up~ght 4. TECHNICAL DATA See Chart (page 13 g) for list of approvals. Glass Bulb Fluid Temperature rated to -65°F (-55°C) Rated 175 PSI (1 207 kPa) water work- ing pressure Factory tested hydrostatically to 500 PSI (3 448 kPa) Thread size: 3/4 NPT (20mm) Orifice Size: Nominal 5/8" (16mm) K Factor: 11 .5 (16,6 Metric for use when pressure is measured in kPa) Spring: USA Patent No. 4,167,974 Bulb: USA Patent No. 4,796,710 Spacing requirements: Refer to Ap- proval Chart and Figure A Minimum operating pressure require- ments: Refer to to Approval Chart and Figure A Materials: Frame: Brass castings UNS-C84400 Deflector: Brass UNS-C26000 Bulb: Glass; Nominal 5mm diameter Seal: Teflon® Tape Spring: Nickel Alloy Sprinkler Nominal Sprinkler Ceiling Temperature at Sprinkler Temperature Temperature Rating Max. Ambient Max. Recommend. Bulb Classification (Fusing Point) Temp. Allowed1 'Ambient Temp.2 Color3 Ordinary 135°F(57°C) 115°F(46°C) 100°F(38°C) Orange Ordinary 155°F(68°C) 135°F(57°C) 100°F(38°C) Red Intermediate 175°F(79°C) 155°F(68°C) 150°F(65°C) Yellow Intermediate 200°F(93°C) 180°F(82°C) 150°F(65°C) Green High 286°F(141°C) 266°F(130°C) 225°F(107°C) Blue Sprinkler Finishes: Brass, Polished Chrome, Black Teflon® and White Polyester. Corrosion Resistant Coatings4: Black Teflon® and White Polyester in all temperatures and Wax coated brass in the following temperatures: 135°F(57°C) White Wax 175°F(79°C) Dark Brown Wax 155°F(68°C) Light Brown Wax 200°F(93°C) Dark Brown Wax. 1 Based on National Fire Prevention and Control Administration Contract No. 7-34860. 2 Based on NFPA-13. Other limits may apply depending on fire loading, sprinkler location and other authority having jurisdiction requirements. Refer to specific installation standards. 3 Temperature rating is stamped on deflector. 4 The Corrosion Resistant Coatings have passed the standard corrosion test required by the listed approving agencies. These tests cannot and do not represent all possible corrosive environments. Prior to installing, verify through the end user, that the coatings are compatible or suitable for the proposed environment. The coatings indicated are applied to the exposed exterior surfaces only and therefore cannot be used as open sprinklers. Note that the spring is exposed on the Teflon~ coated sprinkler and the White Polyester sprinkler. Note: Units of measure in parentheses may be approximations. Form No. 010692 Replaces Sprinkler page 13 e, f, & g dated April 1, 1994 (Added FM Approved upright ELO . .) Sprinkler •13 f February 15, 1996 TECHNICAL DATA MODEL M EXTRA LARGE ORIFICE SPRINKLER \ UL & ULC Spacing and Minimum Pressure Requirements* Maximum Spacing (UL & C-UL Upright and UL & ULC Pendent) Ordinary Hazard Occupancies (UL & C-UL Upright and UL & ULC Pendent): 130 Ft2 (12,0 m2) Extra Hazard Occupancies (UL & C-UL Upright and UL & ULC Pendent): 90 Ft2 ( 8,4 m2) for pipe schedule systems. 100 Ft2 ( 9,3 m2) for systems hydraulically calculated according to NFPA 13 with densities of .25 GPM/Ft2 (10,2 Umin/m2) or greater. 130 Ft2 ~ 12,1 m2) for systems hydraulically calculated according to NFPA 13 with densities less than .25 GPM/Ft2 {10,2 Umin/m ). High Piled Storage (UL & C-UL Upright): 100 Ft2 ( 9,3 m2) for systems hydraulically calculated according to NFPA 231, 231 C, or 231 D with densities of .25 GPM/Ft2 (10,2 Umin/m2) or greater. · 130 Ft2 ( 1221 m2) for systems hydraulically calculated according to NFPA 231, 231C, or 231 D with densities less than .25 GPM/Ft (10,2 Umin/m2). Maximum Distance Between Sprinklers (UL & C-UL Upright and UL & ULC Pendent) Ordinary Hazard Occupancies (UL & C-UL Upright and UL & ULC Pendent): 15 Ft (4,6 m) Extra Hazard Occupancies (UL & C-UL Upright and UL & ULC Pendent): 12 Ft (3,7 m) -Exception #1: Maximum distance between sprinklers= 12'-6" (3,8 m) in bays 25 ft. (7,6 m) wide. Exception #2: Maximum distance between sprinklers= 15'-0" (4,6 m) for systems hydraulically calculated according to NFPA 13 with densities less than .25 GPM/Ft2 (10,2 Umin/m2) .. High Piled Storage Occupancies (UL & C-UL Upright): 12 Ft (3,7 m) -Exception #1: Maximum distance between sprinklers= 12'-6" (3,8 m) in bays 25 ft. (7,6 m) wide. Exception #2: Maximum distance between sprinklers= 15'-0" (4,6 m) for systems hydraulically calculated according to NFPA 13 with densities less than .25 GPM/Ft2 (10,2 Umin/m2). Minimum Distance Between Sprinklers (UL & C-UL Upright and UL & ULC Pendent) Ordinary Hazard & Extra Hazard (UL & C-UL Upright and UL & ULC Pendent) 6 Ft (1.8 m) -Unless provided with baffles installed according to NFPA 13 High Piled Storage Occupancies (UL & C-UL Upright only): 6 Ft (1 .8 m) -Unless provided with baffles installed according to NFPA 13 Minimum Operating Pressure (UL & C-UL Upright and UL & ULC Pendent) Ordinary Hazard & Extra Hazard (UL & C-UL Upright and UL & ULC Pendent) 7 PSI (48,3 kPa) High Piled Storage Occupancies (UL & C-UL Upright only): 10 PSI (70 kPa) FM** Approval Spacing & Minimum Pressure Requirements Maximum Spacing (FM Upright only) Ordinary Hazard, Extra Hazard, and High Piled Storage Occupancies (FM Upright only): 1 00 Ft2 (9 ,3 m2) Maximum Distance Between Sprinklers (FM Upright only) Ordinary Hazard, Extra Hazard, and High Piled Storage Occupancies (FM Upright only): 12 Ft (3,7 m) Minimum Distance Between Sprinklers (FM Upright only) Ordinary Hazard, Extra Hazard, and High Piled Storage Occupancies (FM Upright only): 7Ft(2,1 m) Minimum Operating Pressure (FM Upright only) Ordinary Hazard, Extra Hazard, and High Piled Storage Occupancies (FM Upright only): 10 PSI (70 kPa) Figure A Listing and Approval Spacing and Minimum Pressure Requirements Requirements *UL, ULC, & C-UL listing of ELO Sprinklers requires installation to comply with recommendations set forth in NFPA Installation Standards. UL, ULC, & C-YL spacing and minimum pressure requirements shown are taken from NFPA 13 (1994 ed.), 231 (1995 ed.), 231-C (1995 ed.), and 231-D (1994 ed) and are provided ** for reference only. For FM Approval, installation must compy with requirements of applicable Factory Mutual Loss Prevention Data Sheets. l' February 15, 1996 TECHNICAL DATA MODEL M 5mm GLASS BULB STANDARD RESPONSE EXTRA LARGE ORIFICE Sprinkler 13 g MODEL M EXTRA LARGE ORIFICE SPRINKLER KEY r--Temperature i .--Finish A 1 x-Escutcheon (Pdt. Sprinkler only) Thread Nominal Deflector Nominal Overall Approval 2 Size Orifice Style K Factor3 Length N.P.T. B.S.P. Inches MM Description Base P/N 1 U.S. Metric Inches MM UL4 ULC4 C-UL5 NYC6 3/4" 20mm 5/8" 16 Pendent 3W 20mm 5/8" 16 Upright APPROVED TEMPERATURES A -135°F (57°C), 155°F(68°CJ, 175°F ( 79°C), 200°F (93°C), 286°F (141 C) , B -135°F (57°C), 155°F(68°C), 175°F ( 79°C), 200°F (93°C) C -286°F (141°C) D -155°F(68°CJ, 175°F ( 79°C), 200°F (93°C), 286°F (141 C) E -155°F(68°C), 175°F ( 79°C), 200°F (93°C) A2X A2X 07961 11.5 16,6 2.75 69,9 B2Y B2Y B4X B4X D2 -- 09679 11.5 16,6 2.75 69,9 E4 --cs -- APPROVED FINISHES 1 -Brass, Chrome 2 -Brass, Chrome, Black Teflon®· and White Polyester 3 -Brass, Chrome, and Black Teflon® 4 -Wax coated Brass. Corrosion Resistant 5 -Brass with 200°F (93°C) wax coating. (For corrosion resistance.) Maximum ambient ceiling temperature at ceiling= 150°F (65°C). FOOTNOTES --A3X --B3Y --B4X D2 -- E4 --D1 cs -- APPROVED ESCUTCHEONS X -Standard (surface) Y -Standard (surface) or recessed with E-1 escutcheon 1 Base part number shown. For complete part number, see price list. 2 This Chart shows the listin~s and approvals available at the time of printing. Other approvals are in process. Check with the manufacturer for any additional approvals. 3 Metric K Factor shown is for use when pressure is measured in kPa. When pressure is measured in BAR, multiply the metric K Factor shown by 10.0. 4 For UL and ULC listing requir~ments concerning ELO sprinkler spacing and minimum pressure requirements, refer to Figure A and applicable installation standards. 5 Listed by Underwriters Laboratories Inc. for use in Canada. 6 Accepted for use, City of New York Department of Buildings MEA 89-92-E Vol. III. 7 For FM Approval requirements concerning ELO sprinkler spacing and minimum pressure requirements, refer to Figure A. Also refer to applicable FM Loss Prevention Data sheets. Pintle Screw: Brass UNS-C36000. Pip C~: Copper UNS -C31600 Teflon Sprinklers: Spring: Nickel Alloy; Exposed Pintle Screw: Brass UNS-C36000 Tin plated, painted black for appearance only Pip Cap: Leaded Bronze UNS-C31600 Teflon® coated Polyester Sprinklers: Spring: Nickel Alloy; Exposed Pintle Screw: Brass UNS-C36000 Tin plated, painted white for appearance only Pip Cap: Leaded Bronze UNS-C31600 Tin plated Accessories: Sprinkler Wrench Standard ELO wrench: PN 07297M Wrench for coated & recessed ELO sprinklers: PN 07565W/8 (1 /2" ratchet required) Available Finishes: Chrome, Brass, Black Teflon® or White Polyester 5. AVAILABILITY AND SERVICE Viking sprinklers are available through a network of Domestic, Canadian, and In- ternational Distributors, see the Yellow Pages of the telephone directory (listed under "Sprinklers Automatic Fire") or write to The Viking Corporation. 6. GUARANTEES For details of warranty, refer to Viking's current list price schedule or contact Vi- king directly. 7. INSTALLATION WARNING: Viking sprinklers are manu- factured and tested to meet the rigid requirements of the approving agency. The sprinklers are designed to be in- stalled in accordance with recognized installation standards. Deviation from the standards or any alteration to the sprinkler after it leaves the factory in- eluding, but not limited to, painting, plating, coating or modification, may render the sprinkler inoperative and will automatically nullify the approval and any guarantee made by The Viking Cor- poration. ' A. Sprinklers are to be installed in ac- cordance with the latest published standards of the National Fire Protec- tion Association, Factory Mutual, Loss Prevention Council, Assemblee Pleniere, Verband der Sachver- sicherer or other similar organiza- tions and also with the provisions of governmental codes, ordinances and standards whenever applicable. The use of Extra Large Orifice sprinklers may be limited due to occupancy and hazard. Refer to the Authority Hav- ing Jurisdiction prior to installation. B. Sprinklers must be handled with care. They must be stored in a cool, dry place in their original shipping con- tainer. Never install sprinklers that have been dropped, damaged or ex- posed to temperatures in excess of r l • Sprinkler 13 h 7/16" 1-3/4" (11,1mm) TECHNICAL DATA February 15, 1996 MODELM EXTRA LARGE ORIFICE SPRINKLER 3/4" '-c2omm) Model M NPT 7/16" ...... (11, 1 mm) Model M Extra Large Orifice Model M Pendent Sprinkler Model M Extra Large Orifice Pendent Sprinkler Extra Large Orifice Upright Sprinkler Extra Large Orifice Installed with Model E-1 Installed with 1/8" (3,1mm) Escutcheon Pendent Sprinkler Recessed Escutcheon the maximum ambient temperature allowed. Never install any glass bulb sprinkler if the bulb is cracked or if there is a loss of liquid from the bulb. (These sprinklers should be de- stroyed immediately). C. Corrosion resistant sprinklers must be installed when subjectto c!orrosive atmospheres. When installing corro- sion resistant sprinklers, take care not to damage the corrosion resistant coating. Use only the special wrench designed for installing coated Viking sprinklers (any other wrench may damage the unit). Note: All dimensions are approximate. Figure B compound or tape applied and rein- stalled. This is due to the fact that when the joint seal is damaged, the sealing compound or tape is washed out of the joint. Air testing the sprin- kler piping prior to testing with water may be considered in areas where leakage during testing must be pre- vented. Refer to the Installation Guides, and the Authority Having Ju- risdiction. F. Sprinklers must be protected from mechanical damage. Wet pipe sys- tems must be provided with adequate heat. When installing Extra Large Orifice Sprinklers on dry syst~ms, refer to the Installation Guides, and the Authority Having Jurisdiction. 8. MAINTENANCE D. The sprinkler must be installed after the piping is in place to prevent me- chanical damage. Before installing, make sure the appropriate model, style, orifice size and temperature rating are used. NOTICE: The owner is responsible for 1. Install escutcheon, (if used) which maintaining the fire protection system is designed to thread on to the and devices in proper operating condi- extemal threads of the sprinkler. tion. For minimum maintenance and in- Refer to "Sprinkler Accessories" spection requirements, refer to the Na- for approved escutcheons and tional Fire Protection Association Pam- other accessories. phlet that describes care and mainte- 2. Apply a small amount of pipe joint nance of sprinkler systems. In addition, compound or tape to the external the Authority Having Jurisdiction may threads of the sprinkler only, tak-have additional maintenance, testing ing care not to allow a build up of and inspection requirements which must compound in the sprinkler inlet. be followed. 3. Install the sprinkler on the piping A. The Sprinklers must be inspected on using the special sprinkler wrench .a reQular basis for corrosion, me- only, taking care not to over-charncal damage, obstructions, tighten or damage the sprinkler paint, etc. The frequency of the in- operating parts. DO NO1 use the spections may vary due to corrosive deflector to start or thread the atmospheres, water supplies and ac- sprinkler into a fitting. tivity around the device. E. After installation, the entire sprinkler 8. Sprinklers that have been painted or system must be tested in accordance mechanically damaged must be re- with the recognized installation placed immediately. Sprinklers standards. The test is applied after showing signs of corrosion shall be the sprinkler installation to insure no tested and/or replaced immediately damage has occurred to the sprinkler as required. Standard response during shipping and installation, and Sprinklers that are 50 years old shall to make sure the sprinkler has been be tested and/or replaced as re- properly tightened. If a thread leak quired. Sprinklers that have oper- should occur, normally the sprinkler ated cannot be reassembled or re- must be removed, new pipe joint used,-but must be replaced. When Replaces Sprinkler page 13 e, f, & g dated April 1, 1994 (Added FM Approved upright ELO.) replacing sprinklers, use only new sprinklers. C. The sprinkler discharge pattern is critical for proper fire protection, therefore, nothing should be hung from, attached to, or otherwise ob- struct the discharge pattern. All ob- structions must be immediately re- moved or, if necessary, additional sprinklers installed. D. When replacing existing sprinklers, the system must be removed from service. Refer to the appropriate sys- tem description and/or valve instruc- tions. Prior to removing the system from service, notify all Authorities Having Jurisdiction. Consideration should be given to employment of a fire patrol in the affected area. 1. Remove the system from service, draining all water and relieving all pressure on the piping. 2. Using the special sprinkler wrench, remove the old sprinkler and in- stall the new unit. Care must be taken to replace the sprinkler with the proper model, style, orifice size and temperature rating. A fully stocked spare sprinkler cabi- net should be provided for this purpose. 3. Place the system back in service and secure all valves. Check and repair all leaks. E. Sprinkler systems that have been subjected to a fire must be returned to service as soon as possible. The entire system must be inspected for damage and repaired or replaced as necessary. Sprinklers that have been exposed to corrosive products of combustion or high ambient tem- peratures, but have not operated, should be replaced. Refer to the Authority Having Jurisdiction for mini- mum replacement requirements. Form No. 010692