Loading...
HomeMy WebLinkAbout6628 SANTA ISABEL; ; AS940081; Permit7/28/22, 11:29 AM Job Address: Permit Type: Parcel No: Lot#: Reference No.: PC#: Project Title: Applicant: AS940081 Permit Data City of Carlsbad AUTOMATIC SPRINKLER-COMM Permit No: AS940081 6628 SANTA ISABEL Status: ISSUED ST ASC Applied 12/21/1994 2153300100 Approved: 4/30/1997 0 Issued: 4/30/1997 Inspector: 17568 SF CHURCH BUILDING SANTA ISABEL SPRINKLERS/OVERHEAD Owner: AAA FIRE SPRINKLERS ROMAN CATHOLIC BISHOP OF SAN D 10925 HARTLEY RD #H SANTEE CA 619 449-7728 Fees($) 532.25 about:blank Add'I Fees ($) Total($) Balance($) 0 532.25 0 1 /1 F I R E D E P A R M E N T PERMIT Permit No: AS940081 12/21/94 14:54 Page 1 of 1 Job Address: 6628 SANTA ISABEL ST Suite: Permit Type: AUTOMATIC SPRINKLER-COMMERCIAL Parcel No: 215-330-01-00 Construction Type: VN rr-{J Occupancy Group: u-r Description: 17568 SF CHURCH BUILDING : SANTA ISABEL SPRINKLERS/OVERHEAD Project No: A9400552 Bldg Permit#: CB940390 Status: PENDING Applied: 12/21/94 Apr/Issue: Entered By: CB Resp Party: AAA FIRE SPRINKLERS 10925 HARTLEY RD #H SANTEE CA 92071 619 449-7728 Fire Dept. Reference# : 93149 *** Fees Required *** ** F _ es Collected & Credits *** Fees: Adjustments: Total Fees: Fee description 532.25 .00 53 .25 Total ere a.ts: Total Payments: Balan~e Du~: Uni t ·s Fee/Uni . .... .oo .00 532.25 Ext fee Data -------------------~ ~~~~~----~----~ -~-~----'----~----~----------------- Enter# of Systems , Plan Chk Fee > Enter Total# of Heads * TOTAL Permit Fee FIRE PREVENTION BUREAU 2560 ORION WAY, CARLSBAD, CA 92008-7280 (619) 931-2121 80.00 240.00 212.25 532.25 ___ -_-_-_-_-_-_-_-_-_________________ ---------::---------========== A.A.A. FIRE SPRIHKLERS 444 4459 P.02 ASci4ooit ••• -···-• • • • • • • •• • • , •••••• y ..... v. ,... •••• --·· -·-----··--·---·-9"\tp'\••· , •••• , ........... -··-·· ••• ................ _ ....... ~~ ~A<E-:!2._. ___ . __ ---·--· ----· ... ---~····-·--~--~-···· .. . ................... -•. ~~-~---~~'' ... ~-.\!?. ... 0~---~.Ef:) ___ ~----\~~------... ···--........... - .. . ....... .~~•. ~ ~t~'~.~:-Ac? .. ~.(t~LJ ... ~ ... ff~_J .. ~ .. \.~.!~z. . .. .... . 7<i/ OF \\4\\ S-4<:?._(\.:.17. ~s EC.) .. ~. JJ.LJ_~----·-··· ....... . _ .. .. ~ ' ... ~--I~ .. .§:~ __ (!.:_~ _%_ff:._) ': .. -~i?. ,4,>4-.. . . ...... . , ...... , .. ,, ... ,, ....... ,, ......... -.... ··-··. -~·-···-~--~--~~ .. $:.. F,.,.. ~~~~~=, . . . ... .. . ... '• . .. ,. . . :a:::-•' . 4 ... , '• • " .. ,. • • • ' '• _, .... , ........ -.. ' ........ , ...... --· --... ..... • -·-• ·-• .. • .. -.. • • . . . . ~H .. tr.re. e. __ .. ... .. ... ... .. _ .. ____ . ___ . ·.. . ....... _. . ... . . . .. . . ... .. ~w~. -'~u ·~-~~~-~~T---··---·····-·-.. ·---.. ···--··· .. ·· . "'"\J\~.--~~\.t;i=. __ -:1_2c) c.es. ~ -·-.. . -_., ~ •• k----•-••-•• •••••-~ 4.-§ .. 4..:~.?◄ J.t .. &;) ....... ,., .......... _., __ ,._,, .. -•,-,--,., "' '\"' \ "'' • .,,.,., .... ~-.... ~o~. ~ .......... _ ... ··-· ........ ------. _____ .. __ ,._, __ ....................... , .............. , ... . ............ , ..... . .. 0-\~--~-~l;; __ C~T:. __ uf.~ NATtj~_~...::r\tl\?. ~Tr~!'~~ .. . . ~'S. .'.'1\LL .. t3E.._.~\_~~~~~( I ~E~ . Pi.L . ~~r1UQNAL..~?---~~-~--~crref.:) .. D t ■ Ames 3000ss-Welohts & Dimensions flnchN) NotWL tMWt. SIZE A B . C D E (Optn) F with a tt1 w/o 01tt1 21/a" 22'4 38" 10" 3¼" 18" 17'/4" 166# 68# 3" 22" 38" 10" 3't'4" 2ow· 17W' 230. 70# 4'" n" ◄QM 10" 4•)," 24W' 11w· 240/f 73# 6" 27V2" ~.,,, .. 15" 51,.<,.. 32'/t" 151/a" 3~ 120# 8" 29111" 521/1" 1711, .. G\I, .. 3-P/l~ 19V~" 820# 200# -10" 29½" 551/a'' 17111" 8" 4B" 2z· 8~ 230# ■ 21/2"& 3"Dotumontod Flaw Characlsrlsl/cs (lncludlno shut-otf vMvesJ 100 200 300 400 500 &OOGPM Row Rats (IJPM) ■ 4" Docum,ni,ii/ Row Charact1rllllc1 flncludi11g $hut•ott v~Jves) 10 . . ' . . . I• ................... = ................... ! ................... =······ .. ······· .. ··!···~·· .... ·········=···················:········· j 8 .................. j .......... ~ .. ~!.JP.f-2 .. : .......... '. .................. 1 ....... 4•. ; ........ . J : .. :: :: :: . : : :: : :::: :r ....... :: :: : :::: :: ! :: : : :: : : : : : : : ; : : :: : ! : : ......... : : : . : : : ~ :: : : : : .. : : . : ..... : : r::::::::::::::::::: ! : : : : : : : :: 0 ..._ _______ ~ ..................... _____________ .... o -100 200 300 400 soo aoo GPM Row Rat, (OPM) . ■ B"Oocum,n/sd Row Charact1rls//a, (Including shut•ofl v~lves) 10 1i"a ···················:········· .......... i ................... : ................... ; ................... i .•..•.•.•. ~ i ; ~ i 6° i ii ::::::: :: ::::::::::/:::::::::: :::::::::!: ::::::::::::::: :::/::::::::::::::::: ::1 ::: :::::::::: :: : : ::1:: :: : : : : : :: : : : ::·::: 1::::::: :: 0 250 500 750 1000 1260 1500 GPM Flow Riis (GPM) ■ 8"& 10"Dacum1111l1d FlawCharaclerllllcs (Pending) F Specifications The double check detector assembly consists of two lndspendsntly oper- atlngJ spring loaded check valves, two UL, FM, OSYreslllentwedgegateva/ves, and bypass asumbly. The bypass assem- bly consists of a meter(cublc ft. or gal- lons), a double check Including shut off valves and required test cocks. Each · cam .. check shall be Internally loaded and provide a positive drip tight closure. against reverse flow. Cam-check In- cludes a stainless steel cam arm and · spring, robber faced disc and a replace-,.._ ) able seat. The body shall be manufac- tured lrom 300 series stainless stul, 100% lead f res, with a single two-bolt grooved style access cover. No special tools shall be required tor servicing, Double chock detector shall be 3000ss, Physical Characteristics Sizes -2½", 3•~ C 6'~ 8'J, 10n .. Ratod working pressure -175 psi · . : Hydrostatic pressure • 350 psi Temperature Range -32° F .. 110° F Body material• 300 series stainless steel Flange dimension In accordance with AWWA Class D . *Contact the factory for s~clflc approvals Form# OCOA/SS 3/93 ,____,; AMEmS AAA Fi Tenant Improver 1en Specialist HYDRAULIC DESIGN INFORMATION SHEET ·NAME9, 9·.-~:r\ ~ ~ LOCATION {c;/o'2f!:> ~ '2-ee&_ DATE \'2 .. Zc::>.C\4 BUILDING ~\4 SYSTEM No,_\ ____ o __ F=--.;...._...\ ___ _ CONTRACTOR ~'C&,F CONTRACT NO • ..M97 I CALCULATED BY---1::~~1:..-i::;__ _____ __.;. _____________ DRAWING NO, :::Z:Gf:~ • CONSTRUCTIO~; ~ COMBUSTIBLE O NON-COMBUSTIBLE CEILING HEIGHT VA@g; FT, OCCUPANCY ~ .. z (!) en w 0 ::E w t-en >-Cf.) fl NFPA 13: 0 NFPA 231 PJI LT, HAZ •. 0 NFPA 231C: ORD. HAZ. GP. 0 1 0 2 0 3 0 EX. HAZ. FIGURE_______ CURVE ______ _ 0 OTHER (Specify)------------------------------0 SPECIFIC RULING ___________ MADE BY ______ DATE _____ _ AREA OF SPRJNKLER OPERATION \;i::;?(:) q? DENSITY. ~~ :!: AREA PER. SPRINKLER ~ ~ ~ HOSE ALLOWANCE GPM: . INSIDE __ p __ _ HOSE ALLOWANCE GPM: OUTSIDE, -~...ii;::. __ RACK SPRINKLER ALLOWANCE. SYSTEM TYPE ,A WET O DRY O DELUGE PRE-ACTION SPRINKLER OR NOZZLE . MAKE 1?:Ef,JAC?i 6: MODEL ~ SIZE l,z" K-FACTOR_ '5.Co __ _ TEMPERATURE RATING 14:$0 . . CALCULATION GPM REQUIRED ~4],c::57 PSI REQUIRED 9ZCJ4 AT BASE OF RISER. SUMMARY "C" FAC·TORµSED: OVEAHEAD _ _,_\'2~~~~·---UNDERGROUNO_t~9:?-==~: __ _ >-.J a.. Cl. ::, Cl) er w ... < == w (!) < cc 0 >-Cl) >->-0 0 ::E :E 0 u WATER FLOW TEST ·DATE & TIME Ce· :~:Pj4- STATIC PSI t.....,..._-;}.,.__ __ RESIDUAL PSI __ 42K..~------- GPM FLOWtNG l';EPC> ELEVATION _ __.$'-'--- RATED AT PSI ELEVATION LOCATJON ·:;s1JE 9 .i: WELL GP SOURCE OF INFORMf-TION_\/.¥.,i~l::::IJ.i:d:5.:B:1..~d..d. l...L.,~· ~,✓-!a.:!..:.J• Dt:::J..., ------------------- ___________ CLASS _______ _ _________ AREA _______ -=---~I D SINGLE ,, 0 DOUBLE . 0 MULTIPL ~ (.) < a: ____ % PACING IN INCHES ___ TRANSVERSE __ _ RACK _____ % 0 AUTOMATIC STORAG.E O ENCAPSULATED 0 SOLID SHELVING O NON- O OPEN ENCAPSULATED OF STORAGE TO CEILING (619) 444-4459 648 Trenton St., El Cajon, CA 92019 FAX: (619) 444-24 9 ,-... en a.. '-" Q) ... :J OJ OJ <I) ... 0.. 125 ·: SIGMA DYNAMICS CORP. 77;00 Supply / Deman~ Graph 120 115 110 105 100 95 90 85 80 75 70 65 60 55 50 45 40 35 30 25 20 15 10 5 • _.. ..... D) .. ' .. I ·--•-• ~' I' 4''0 ~f ~, fcf2 ~A O 200 400 600 80D 1000 1200 System Demand .. Sprinkler Demand Additional Flows Hose at Source Total Demand 53.73 PSI@ 297.07 6PM 0.00 6PM 100.00 6PM 53.73 PSI@ 397.07 GPM V 1400 Water Flow (GPM) -•- I I Margin Pressure 16.iO PSI Flow 1708.?1 6PM -...... \ s -- "6100 1800 Wlmter Supply .. Sttftic 70.60 PSI . Residual 61.60 PSI@ 1500.00 6PM Elm,at1on 1.30 PSI ; -- Nl.85 2000 SUBMITTAL ,SERIAL N0:2905HY1 ST. ELIZABETH AREA #1 ( .10/1500) FLOW TEST RESULTS Water Supply STATIC 69.30 PSI RESIDUAL 60.30 PSI @ 1500.00 GPM ELEVATION OF TEST 3.00 Ft CITY PRESSURE AVAILABLE .AT 397 .1 GPi"'i 69.83 PSI SUMMARY OF SPRINKLER OUTFLOWS MINIMUM SPR 100 101 - 102 103 104 105 106 107 108 109 110 111 112 113 114 115 ACTUAL FLOW FLOW K-FACTOR PRESSURE 22.55 19.18 18.15 16.39 15.40 22.40 19.05 18.03 16-. 28 15.29 23.88 21.45 19.75 18.77 15 .50 _ 15.00 15.00 15.00 ·1s.oo 15.00 15.00 15.00 15.00 15 00 15.00 15.00 15.00 15.00 15.00 15.00 15.00 15.00 5.60 5.60 5.60 5.60 5.60 5.60 5.60 5.60 5.60 5.60 5.60 5.60 5.60 5.60 5.60 5.60 TOTAL WATER REQUIRED FOR SYSTEM OUTSIDE HOSE STREAMS AT 0 TOTAL WATER REQUIREMENT PRES~URE REQUIRED AT 0 MAXIMUM PRESSURE UNBALANCE IN LOOPS MAXIMUM V~LOCITY IN PIPES 16.22 11.73 10.50 ~3 . 57 7 . .56 16.00 11 .57 1.0.36 8 .45 7.45 1.8 .10 14 .6 8 12.44 11.24 7.66 7.17 297.07 GPM 100.00 GPM 397.07 GPM 53.73 PSI 0.05 PSI 17.16 FPS 11-19-1994 PAGE 1 '. ·'• I " SUBMITTAL SERIAL N0:2905HY1 11-19-1994 PAGE 2 ST. ELIZABETH .. AREA ~1 ( .10/1500) FRO'M· TO . " 'FLOW . . l)IAM . EQUIV P-LOSS PRESSURE ~ .. l..El,I GTH PIPE SUMMARY GPM IN .. Ft PSI/Ft PSI 114 115 1.087 L 7.50 0.0643 PT 7.17 ( 115) Q 1.?. 00 F=O F 0 .. 00 PE 0.00 BN C120 T 7 .. 50 PF 0.48 l• ..,,_.... 113 114D0 15.50 1.087 L 15 .. 00 0.2388 PT 7.65 ( 114) Q 30.50 F=O F 0.00 PE 0 .. 00 BN C120 T 15.00 PF 3.58 112 113D0 18.77 1.416 L 7.50 0 .. 1600 PT 11.23 ( 113) Q 49.27 F=0 F 0.00 PE 0.00 ,,..., BN C120 T 7.50 PF 1.20 111 112D0 19.75 1.416 L 7.50 0.2986 PT 12.43 ( 112) Q 69.02 F=O F 0·.00 PE ·0.00 BN C120 T 7.50 PF 2.24 110 ·111D0 21.45 1.650 L 15.00 0.2339 PT -14 .. 67 ( 111) Q 90.47 F=O F 0 .. 00 PE 0.00 BN C120 T 15.00 PF 3.51 13 110D0 23.88 1.650 L 18.00 0.3608 PT 18.18 ( 110) Q 114.35 F=.T ~ 2E F 16 .. 00 PE 3.90 BN C120 T 3t1 .00 PF 12.27 ')') PT 34.35 ( 13) --~-~-------------.. 108 109 1.087 L 15.00 0.0666 PT 7A5 ( 109) Q 15.29 F=O F 0 .. 00 PE 0.00 BN C120 T 15.00 PF 1.00 107 108DQ 16.28 1.087 L 7.50 0.2546 PT 8.45 ( 108) Q 3!_.57 F=O F 0.00 PE 0.00 BN C120 T 7.50 PF 1.91 106 107DQ 18.03 1.416 L 7.50 0 .1620 PT 10.36 ( 107) I Q 49.59 F=0 F 0.00 PE 0.00 BN C120 T 7.50 PF 1.22 105 106DQ 19.05 1.416 L 15.00 0.2956 PT 11.58 ( 106) Q 68.65 F=0 F 0.00 PE 0.00 BN C120 T 15.00 PF 4.43 12 105D0 22~40 1.650 L 37.00 0.2367 PT 16.01 ( 105) Q 91.05 F=T,2E F 16.00 PE 5.85 ~ !' BN C120 T 53.00 PF 12.55 PT 34 .41 ( 12) --~~-~~---~-~~~-~- 103 104 1.087 L 15.00 0.0675 PT 7.56 ( 104) Q 15.40 F=0 F 0.00 PE 0.00 BN C120 T 15.00 PF 1 · .. 01 SUBMITTAL SERIAL N0:2905HY1 11-19-1994 PAGE 3 ST. ELIZABETH AREA #1-·( ~10/1500) I l . :I .v ' • I ! ' . \ ., . ' ··F·R·o~f .. to ' ~-....... ... FLOW DIAM EQUIV P-LOSS PRESSURE LENGTH PIPE SUMMARY GPM IN Ft PSI/Ft PSI :i 7 .. 50 0.2579 PT 8.57 ( 103) '! 102 ·103D0 . 16.39 I :1 .08? L Q 31. 79' F=O F 0.00 PE 0.00 BN C120 T 7.50 PF 1.93 101 102D0 -1a .1s 1.416 L 7.50 0 .1641 PT 10.50 ( 102) ·-- Q 49.94 F=O F 0 .. 00 PE 0.00 BN C120 T 7 .. 50 PF 1.23 1Q0 101D0 19.18 1.416 L 15.00 0.2994 PT 11 .. 73 ( 101) Q 69.12 F=O F 0.00 .PE 0.00 SN C120 T 15.00 PF 4.49 11 100D0 22.55 1.650 L 37 .. 00 0.2397 PT 16.22 ( 100) .. l•!1 Q 91.67 F=T,2E F 16.00 PE 5.85 f· i :~ BN C120 T 53.00 PF 12.70 PT 34.77 ( 11) ~~~~~--~-~~-~~~~~~ ..,.._,.,. 14 -13 2.731 L 40.00 0.0129 PT ·34 .35 ( 13) Q 71 •. 17 F=3E F 12.00 PE -0.22 CM C120 T 52.00 PF 0.67 ·~ -16 14 2.731 L 6.00 0.0129 PT 34.80 ( 14) Q 71.17 F=T F 12.00 PE 1 .. 08 ·CM C120 T 18.00 PF 0.23 17 16 . 2 ~731 L 10.50 0 ~-0129 PT 36 .. 11 ( 16) . ' Q 21·.17 · ':: ... F=3E F 12.00 PE 0.00 . .. CM C120 T 22.50 PF 0.29 18' 17 2.731 1 L 108.00 0.0129 PT 36.40 ( 17) ~- Q 71.17 · F=4E/3E , EE F 31.00 PE -0.87 CM C120 T 139.00 PF 1.79 19·_ 18 2.731 L 9.50 0.0129 PT 37.32 (. 18) Q ' · ,.71.17 F=O F 0.00 PE 0.00 CM C120 T 9.50 PF 0 .12 20 19 2.731 L 6.00 0.0129 PT 37.44 ( 19) : ' • ' f' ;,\ Q 71 ~ 17 . F=O F 0.00 PE 0.00 ..,,.,,.,.. CM C120 T 6.00 PF 0 .. 08 21 · 20 2.731 L. 23.50 0.0129 PT 37.52 ( 20) Q 71.17 ·F=4E F 16.00 PE 1 .. 52 ~ "!. J • • CM .. C120 T 39.50 PF 0.51 1 '):.", ' ! ~ 22 21 2.731 L 1.00 0.0129 PT 39.55 ( 21) Q 71~17 F=O F 0.00 PE 0.00 ·CM C120 T 1.00 PF 0.01 .. ··- > ;; ; • . ,;t . SUBMITTAL SERIAL ·N0:2905HY1 · 11-19-1994 ' PAGE 4 ST. ELIZABETH AREA #1 (.,.10/1500.) FROM TO FLOW DIAM EQUIV P-LOSS PRESSURE 'LENGTH PIPE SUMMARY GPM IN Ft PSI/Ft PSI 23 22 2.731 L 114.17 0.0129 PT 39.56 ( 22) ,..,....,.. a 71.17 F=EE., 4E/E F 23 .. 00 PE 0.29 CM C120 T 137.17 PF 1.77 4 23 2.731 L 4 5 .. 00 0.0129 PT 41.62 ( 23) ,..,. ' 0 71.17 F=E,3EE F 13.00 PE 1.01 CM C120 T 58.00 PF 0.75 !Ii ,· ( 4) PT 43.38 .:;' ; -~-~~~~~--~~~~~~~- 12 13 ·2.731 L 10.00 0.0051 PT 34.35 ( 13) Q 43.18 F=O F 0.00 PE 0.00 -- CM C120 T 10.00 PF 0.05 11 12D0 91.05 2.731 L 9.00 0.0417 PT 34.40 ( 12) .,,...,.... Q 134.23 F=O F 0.00 PE 0.00 CM C120 T 9.00 PF 0.38 10 11D0 91~67 2.731 L 10.00 0.1093 PT 34.78 ( 11) a 225.90 F=O F 0.00 PE 0.00 CM C120 T 10.00 PF 1.09 4 10 2.731 L 23 .·so 0.1093 PT 35.87 ( 10) Q 225.90 F=T,2E F 20 .00 PE 2.82 CM C120 T 43.50 PF 4.75 3 4DQ 71.17 2.731 L 2.00 0 .. 1814 PT 43 .. 44 ( 4) Q 2~7.07 F=O F 0.00 PE 0.00 • I '. FM C120 T 2.00 PF 0.36 1 3 2.731 L 11.00 0.1814 PT 43.80 ( 3) Q 297.07 F=T F 12.00 PE 4.77 FR C120 T 23.00 PF 4 .17 0 1 4.240 L 240 .00 0.0141 PT 52.74 ( 1) a 297.07 F=T,GV/3E,3EE F 78 .. 00 PE -3.49 UN C150 T 318.00 PF 4.48 PT 53.73 ( 0) MAXIMUM PRESSURE UNBALANCE IN LOOPS 0 .. 05 PSI MAXIMUM VELOCITY IN PIPES 17.16 FPS AAA.Fir Tenant Improvement Specialists HYDRAULIC DESIGN INFORMATION SHEET ·NAME5?1'• ~\H ~ ~ LOCATION 1/:k;'Zt!::, :=Ar:-AA l?e:8a.. BUILDING ~B SYSTEM No.__._\ __ o ___ ~_, ___ _ CONTRACTOR ~\C&E CONTRACT NO. ~9:J J CALCULATED BY_,.;t?AB...:.....1~------.;...._------------DRAWING NO. ::::z.Gf::-2 CONSTRUCT!~ COMBUSTIBLE O NON-COMBUSTIBLE CEILING HEIGHT Vp,[Z\1=;? OCCUPANCY~~~ll,a:l,l.,_;;:;;;~-------------~----------------~ z c,. en w 0 :E w t-en >-(,') fl NFPA 13: 0 NFPA 231 lll LT. HAZ .. 0 NFPA 231C: . ORD. HAZ. GP. 0 1 0 2 0 3 □ FIGURE ______ CURVE ______ _ 0 OTHER (SpecJfy)-----------------------------0 SPECIFIC f:lULING ___________ MADE BY ______ DATE _____ _ AREA OF SPRINKLER OPERATION \S;;:(:) 9? DENSITY ..... ::=\ AREA PER. SPRINKLER ~ ~ '1? HOSE ALLOWANCE Gf:'M: . INSIDE _---#-¢ __ _ HOSE ALLOWANCE GPM: OUTSIDE, --..i.........,~-- AACK SPRINKLER ALLOWANCE. SYSTEM TYPE fJ) WET O DRY O DELUGE PRE-ACTION SPRINKLER OR NOZZLE . MAKE 12E( )Ae:i 6 MODEL ~ SIZE 1::z" K-FACTOR _'5.Co __ _ I TEMPERATURE RATING 1~0 . . cALcuLAT10N GPM Reau1Reo ~,4.eo · PSI REQUIRED 8,fp;C)'b AT BASE OF RISER. SUMMARY "C" FAOT0RµSED: OVERHEAO_-L.\'2=~=~·---UNDERGROUND_~~9:?-==~: __ _ ' >- ..J a.. a. ::, en a: w I-< == w C) < a: 0 ... I Cl) >-1--o 0 :E :E 0 . 0 WATER ELQ\ALIE§.J;_ -DATE & TIME c;:~.~ STATIC PSI -::::r;:J___."--,1... __ _ RES !DUAL PSI __ 4;,i;;...s;~------ GPM FL0WtNG l';::00 ELEVATION ___ $.._' __ _ LOCATION . :i:?\JE. Y / SOURCE OF INFORMf'TION_V~W+B~~~~.a..· ~· --'-=·=-~'Y...z..:•:..a::P~,...._----------------~ ___________ CLASS ______ _ ~------------AREA _______ __.-n, STORAG ____ % PALLETIZED__..:;;..._ __ RACK----- ~ 0 < er 0 SINGLE , D DOUBLE . 0 MULTIPL PACING IN INCHES ___ TRANSVERSE __ _ 0 AUTOMATIC STORAGE O ENCAPSULATED 0 SOLID SHELVING . 0 NON- O OPEN ENCAPSULATED OF STORAGE TO CEJLING 648 Trenton St., El Cajon, CA 92019 ~ 125 120 115 110 105 100 95 90 85 80 75 S-T. ELIZABETH AREA i2 ( .. 10/1500) SIGNA ,DYNAMICS CORP. ~ 7D• a.. '-,.J' 65 Q) ... i 60 GO f 55 a.. 5D 45 40 35 3D 25 2D 15 10 5 -- j I I 16~ I]:') I r .,_ --==• ---. I ~~ , ' ti ---~· ~ f; bZ4 ... ,i, '- O 200 400 600 800 1000 1200 System Demand .. Sprinkler Demand 59.45 PSI@ 374.62 6PM Additional Flows 0.00 6PM Hose at Source 100.00 6PM Total Demand 59.45 PSI@ 474.62 GPM 1400 Water Flow (GPM) -•- 7700 Supply / Demand Graph I I Margin Pressure 10.07 PSI Flow 1208.97 6PM -(s~ -- 1600 1800 Water Supply .. Static 70.60 PSI Residual 61.60 PSI@ 1500.00 6PM Elevation 1.30 PSI -- Nt.85 2000 sDBMIYrAL SERIAL No:29osHY1 ST. ELIZABETH ·. AREA #2 ( .10/1500) I • • .. ,,.... . FLOW TEST RESULTS Water Supply STATIC 69.30 PS! RESIDUAL 60.30 PSI @ 1500 .. 00 GPM ELEVATION OF TEST 3.00 Ft CITY PRESSURE AVAILABLE AT 474.6 GPM 69 .. 53 PSI SUMMARY OF SPRINKLER OUTFLOWS ACTUAL ·· MINIMUM SPR · FLOW FLOW K-FACTOR PRE SS URE 150 151 152 153 154 155 156 157 158 159 '160 161 162 163 22 .17 21.34 21 .10 22.77 21.21 20 .13 24.88 18.36 17.43 16.81 24.97 19 .16 18.20 17 .52 - 14.82 14 .82 14.82 14.82 14.82 1._ 14.82 14.82 16.81 16.81 16.81 14.82 · 16 .81 16.81 16.81 164 · ·23 .46 14 .82 165.-' . 22 •1oo ·J . .'· 14· .82 '· 166 ··· 20.85 14.82 167 22.24 14.82 5 .60 5.60 5.60 5 .60 5 .60 5r.60 5.60 5.60 5.60 5.60 5.60 5.60 5.60 5.60 5.60 5.60 5.60 5.60 TOTAL WATER REQUIRED FOR SYS TEM OUTSIDE ~HOSE .STREAMS AT 0 TOTAL WATER REQUIREMENT PRESSURE REQUIRED AT 0 MAXIMUM PRESSURE UNBALANCE IN LOOPS MAXIMUM VELOCITY IN PIPES 15.6 7 1.4 .53 14 .. 2 0 16.5 4 14.35 12.9 3 19 .73 10 .. 75 9 .. 69 9.01 19 .. 89 11.70 10 .56 9.79 17 .55 15A4 13.86 15.77 :$7 ,-1 • 62 GPM 100.00 GPM 474 .62 GPM 59.45 PSI 0.05 PSI 20 .52 FPS 11-19-1994 PAGE 1... ... SUBMITTAL SERIAL N0:2905HY1 11-19-1994 PAGE 2 ST. ELIZABETH AREA #2 ( .10/1500) FROM TO FLOW DIAM EQUIV P-LOSS PRESSURE LENGTH PIPE SUMMARY GPM IN Ft PSI/Ft PSI 155 159 1.087 L 19.00 0.0793 PT 9.01 ( 159) Q 16.81 F=3E F 6.00 PE 1.95 BN C120 T 25.00 PF 1.98 73 155D0 20 .13 1.416 L 6.50 0.0940 PT 12.94 ( 155) Q 36.94 F=T F 6.00 PE -0.65 BN Cl20 T 12.50 PF 1.17 PT 13.46 ( 73) ------------------ 75 162 1.087 L 12.50 0.0919 PT 10.56 ( 162) Q 18.20 F=T,2E F 9.00 PE 1.95 BN C120 T 21.50 PF 1.98 165 75D0 38.37 1.650 L 10.00 0.0981 PT 14.49 ( 75) Q 56.57 F=O F 0.00 PE 0.00 BN C120 T 10.00 PF 0.98 74 165D0 22.00 1.650 L 2.00 0 .1802 PT 15.47 ( 165) Q 78.57 F=O F 0.00 PE 0.00 BN C120 T 2.00 PF 0.36 PT 15.83 ( 74) ------------------ 73 158 1.087 L 12.50 0.0849 PT 9.69 ( 158) Q 17.43 F=T,2E F 9.00 PE 1.95 BN C120 T 21.50 PF 1.83 154 73D0 36.94 1.650 L 10.00 0 .0912 PT 13.47 ( 73) Q 54.38 F=O F 0.00 PE 0.00 BN C120 T 10.00 PF 0.91 72 154D0 21.21 1.650 L 2.00 0.1678 PT 14.38 ( 154) Q 75.59 F=O F 0.00 PE 0.00 BN C120 T 2.00 PF 0.34 PT 14.72 ( 72) ------------------ 42' 164 1.087 L 4.00 0 .1470 PT 17.55 ( 164) Q 23.46 F=E F 2.00 PE -0.22 BN C120 T 6.00 PF 0.88 PT 18.21 ( 42) ------------------ 41 160 1.087 L 10.00 0 .1650 PT 19.89 ( 160) Q 24.97 F=2E,T F 9.00 PE 0.00 BN C120 T 19.00 PF 3 .14 21 41 1.416 L 2.00 0.0455 PT 23.03 ( 41) Q 24.97 F=T/T F 12.00 PE 0.87 NR C120 T 14.00 PF 0.64 PT 24.54 ( 21) SUBMITTAL SERIAL N0:2905HY1 11-19-1"1':fl+ i-'MUI-j - ST. ELIZABETH AREA #2 ( .10/1500) FROM TO FLOW DIAM EQUIV P-LOSS PRESSURE LENGTH PIPE SUMMARY GPM IN Ft PSI/Ft PSI -~---------------- 40 156 1.087 L 6 .. 00 0 .. 1638 PT 19.73 ( 156) Q 24.88 F=2T,E F 12 .. 00 PE -0.65 BN C120 T 18.00 PF 2.95 20 40 1.650 L 0 .. 50 0.0215 PT 22.03 ( 40) Q 24.88 F=T/T F 16 .. 00 PE 0 .. 22 NR C120 T 16 .. 50 PF 0.35 .. -.. --·•·'--" .... PT 22 .. 60 ( 20) ~----------------- 166 163 1 .. 087 L 19 .. 00 0.0857 PT 9 .. 79 ( 163) Q 17.52 F=3E F 6 .. 00 PE 1..95 BN C120 T 25 .. 00 PF 2 .. 14 75 166D0 20 .as· 1 .. 416 L 6 .. 50 0 .1008 PT 13.88 ( 166) Q 38.37 F=T F 6 .. 00 PE -0 .. 65 BN C120 T 12.50 PF 1.26 PT 14 .. 49 ( 75) ----------------~- 74 161 1.087 L 12 .. 50 0 .. 1010 PT 11.70 ( 161) Q 19.16 ') F=T,2E F 9 .. 00 PE 1 .. 95 BN C120 T 21 .. 50 PF 2 .17 42 74D0 78.57 1.650 L 5.00 0 .. 2698 PT 15.82 ( 74) Q 97.73 F=E F 4 .. 00 PE 0.00 BN C120 T 9.00 PF 2.43 22 42D0 23 .. 46 1 .. 650 L 2 .. 50 0 .. 4017 PT 18 .. 25 ( 42) Q 121 .. 19 F=T/T F 16 .. 00 PE -1 .. 08 NR .C120 T 18 .. 50 PF 7 .. 43 PT 24 .. 60 ( 22) --------------~--~ 72 157 1.087 L 12.50 0 .. 0934 PT 10 .. 75 ( 157) Q 18.36 F=T,2E F 9 .. 00 PE 1.95 BN C120 T 21.50 PF 2 .. 01 39 72D0 75 .. 59 1.650 L 5.00 0.2508 PT 14.71 ( 72) Q 93.95 F=E F 4 .. 00 PE 0.00 BN C120 T 9.00 PF 2 .. 26 PT 16 .. 97 ( 39) -~~-~------------- 39 153 1 .. 087 L 5 .. 50 0 .. 1391 PT 16 .. 54 ( 153) Q 22 .. 77 F=E F 2 .. 00 PE -0 .. 65 BN C120 T 7 .. 50 PF 1 .. 04 19 39D0 93 .. 95 1 .. 650 L 5 .. 50 0 .. 3748 PT 16.93 ( 39) Q 116 .. 72 F=T/T F 16 .. 00 PE -2 .. 38 SUBMITTAL SERIAL N0:2905HY1 11-19-1994 PAGE 4 ST. ELIZABETH AREA #2 ( .10/1500) FROM TO FLOW DIAM EQUIV P-LOSS PRESSURE LENGTH PIPE SUMMARY GPM IN Ft PSI/Ft PSI ------------------ 76 167 1.416 L 22.00 0.0367 PT 15.77 ( 167) 0 22.24 F=2E,T F 12.00 PE -3.68 SN C120 T 34.00 PF 1.25 PT 13.34 ( 76) ------------------ 71 152 1.087 L 19.00 0 .1209 PT 14.20 ( 152) 0 21.10 F=3E F 6.00 PE -3.68 SN C120 T 25.00 PF 3.02 PT 13.54 ( 71) ------------------ 76 151 1.416 L 3.50 0.0341 PT 14.53 ( 151) 0 21.34 F=T F 6.00 PE -1.52 SN C120 T 9.50 PF 0.32 71 76D0 22.24 1.416 L 1.50 0.1276 PT 13.33 ( 76) Q 43.58 F=O F 0.00 PE 0.00 SN C120 T 1.50 PF 0 .19 70 71D0 21.10 1.650 L 7.50 0 .1258 PT 13.52 ( 71) 0 64.69 F=2E/T F 16.00 PE 0.00 SN C120 T 23.50 PF 2.96 PT 16.48 ( 70) -------------r---- 70 150 1.087 L 5.50 0 .1324 PT 15.67 ( 150) Q 22.17 F=2T,E F 12.00 PE -1.52 SN C120 T 17.50 PF 2.32 38 70D0 64.69 1.650 L 3.50 0.2169 PT 16.47 ( 70) Q 86.86 F=2E F 8.00 PE 0.00 SN C120 T 11.50 ·PF 2.49 18 38 1.650 L 0.50 0.2169 PT 18.96 ( 38) Q 86.86 F=T/T F 16.00 PE 0.22 NR C120 T 16.50 PF 3.58 PT 22.76 18) ------------------ 20 19 2.731 L 6.00 0.0040 PT 22.63 19) Q 37.83 F=O F 0.00 PE 0.00 CM C120 T 6.00 PF 0.02 21 20D0 24.88 2.731 L 23.50 0.0102 PT 22.65 ( 20) Q 62.71 F=4E F 16.00 PE 1.52 CM C120 T 39.50 PF 0.40 22 21D0 24.97 2.731 L 1.00 0.0190 PT 24.57 ( 21) Q 87.68 F=O F 0.00 PE 0.00 CM C120 T 1.00 PF 0.02 SUBMITTAL SERIAL N0:2905HY1 11-19-1994 PAGE 5 • ST . ELIZABETH AREA #2 ( .10/1500 ) FROM TO FLOW DIAM EQUIV P-LOSS PRESSURE LENGTH PIPE SUMMAf~Y GPM IN Ft PSI/Ft PSI 23 22D0 121.19 2.731 L 114.17 0.0945 PT 24.59 ( 22) Q 208.86 F=EE,4E/E F 23.00 PE 0.29 CM C120 T 137. 17 PF 12.96 4 23 2.731 L 45.00 0.0945 PT 37.84 ( 23) Q 208.86 F=E,3EE F 13.00 PE 1.01 CM C120 T 58.00 PF 5.48 PT 44.33 4) ------------------ 18 19 2.731 L 9.50 0.0156 PT 22.63 19) Q 78.89 F=O F 0.00 PE 0.00 CM C120 T 9.50 PF 0 .15 17 18D0 86.86 2.731 L ~ .0616 PT 22 .78 ( 18) Q 165.75 F=4E/3E,EE F 31.00 PE 0.87 CM C120 T 139 .00 PF 8 .56 16 17 2.731 L 10.50 0.0616 PT 32.21 ( 17) Q 165.75 F=3E F 12.00 PE 0.00 CM Cl20 T 22.50 PF 1.39 14 16 2.731 L 6 .00 0.0616 PT 33.60 ( 16) Q 165.75 F=T F 12 .00 PE -1.08 CM C120 T 18.00 PF 1.11 13 14 2.731 L 40.00 0 .0616 PT 33 .63 ( 14) Q 165.75 F=3E F 12.00 PE 0.22 CM C120 T 52.00 PF 3.20 12 13 2.731 L 10.00 0.0616 PT 37.05 ( 13) Q 165.75 F=O F 0.00 PE 0.00 CM C120 T 10.00 PF 0.62 11 12 2.731 L (ro) 9 .oo 0.0616 PT 37.67 ( 12) Q 165.75 F=O F 0.00 PE 0.00 CM C120 T 9.00 PF 0.55 ·10 11 2.731 L 10 .00 0.0616 PT 38.22 ( 11) Q 165.75 F=O F 0.00 PE 0.00 CM C120 T 10 .00 PF 0.62 4 10 2.731 L 23.50 0.0616 PT 38.84 ( 10) Q 165.75 F=T,2E F 20 .00 PE 2 .82 CM C120 T 43.50 PF 2.68 3 4D0 208.86 2 .731 L 2 .00 0.2785 PT 44.34 4 ) Q 374.62 F=O F 0.00 PE 0.00 FM C120 T 2.00 PF 0.56 > SUBMITTAL SERIAL N0:2905HY1 11-19-1994 PAGE 6 ST. ELIZABETH AREA #2 ( .10/1500) FROM TO FLOW DIAM EQUIV P-LOSS PRESSURE LENGTH PIPE SUMMARY GPM IN Ft PSI/Ft PSI 1 3 2.731 L 11 .. 00 0.2785 PT 44.90 ( 3) Q 374.62 F=T F 12.00 PE 4.77 FR C120 T 23 .00 PF 6.41 ~ 7 4.240 L 2 40.00 0 .0216 PT 56 .. 08 ( 1) Q 374.62 F=T,GV/3E,3EE F 78 .. 00 PE -3 .. 49 UN C150 T 318.00 PF 6.87 PT 59 .. 46 ( 0) MAXIMUM PRESSURE UNSALANCE IN LOOPS 0.05 PSI MAXIMUM VELOCITY IN PIPES 20.52 FPS