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HomeMy WebLinkAbout2303 OCEAN ST; ; AS140173; Permit7/19/22, 2:00 PM AS 140173 Permit Data City of Carlsbad Sprinkler Permit Job Address: 2303 OCEAN ST Permit Type: SPRINK Parcel No: 2030102200 Lot #: 0 Permit No: AS140173 Status: ISSUED Applied 7/16/2014 Approved: 7/29/2014 Reference No.: Issued: 7/29/2014 PC #: Inspector: Project Title: OCEAN ST RESIDENCES BLDG 1 PROVIDE NEW FIRE SPRINKLER SYSTEM NEW 2-STORY WOOD FRAME RESIDENTIAL BLDG PER NFPA 13D OVER A PODIUM GARAGE. Applicant: INNOVATIVE FIRE PROTECTION INC STE 101 8779 COTTONWOOD AV SANTEE CA (619) 593-8200 (619)593-9133 Owner: OCEAN STREET 8 OWNER LLC ATTN:GENERAL COUNSEL 3300 P G A BLVD #820 PALM BCH GDNS FL Fees ($) Add'I Fees ($) Total ($) Balance ($) 470 0 470 a about:blank 1/1 Parsley Consulting 350 West 9" Avenue, Suite 206 RECE1V)) Escondido, California 920255053 Phone (760) 745-6181 eMaih parsle vconsulffirgg @coxnegUL 1 2014 W0bjt0 http://www.parsleycoiisulfing.com I CAQSBAD IR July 10, 2014 __!PARMENT Fire Code Official City of Carlsbad Fire Department Office of Fire Protection Services 1635 Faraday Avenue Carlsbad, California 92008 Subject: Fire Sprinkler Review for Ocean Street Residence & Garage, 2303 Ocean Street, Carlsbad, CA Dear Sir: We have reviewed the submittal as prepared by Innovative Fire. Based on our review it is our opinion that the submittal is in substantial conformance with the applicable codes and standards in force at this time, including local adopted ordinances. Further submittal should not be required. Sincerely, P,OUyNG Kenneth W. WagoneT Office Manager End (1) Working Drawings - 3 sets Hydraulic Calculations - 3 sets Review Comments Note: A copy of this letter has been transmitted via e-mail to Innovative Fire on July 10, 2014 File: i:\Plan Reviews\Rev2 1426 1.1.Docx Parsley Consulting Plan Review Comments for Ocean Street Residence & Garage page 2 of 2 1) There was a minor issue on the lateral bracing of the mains in the garage. Revisions were made and have been affixed to the drawing, and some redline marks added. No resubmittal is required. File: I:\Plan Reviews\Rev2 14261.1 .Docx OCEAN STREET RESIDENCES BLDG# STREET# STREET AS# FA# CB# 1 2303 OCEANST- AS140173 FA140086 CB131212 2 2309 OCEAN ST AS140174 FA140087 CB131214 3 2315 OCEAN ST AS140175 FA140088 CB131216 4 2321 OCEAN ST A5140176 FA140089 CB131218 5 2327 OCEAN ST AS140177 FA140090 CB131220 6 233 OCEAN ST AS140178 FA140091 CB131222 7 2339 OCEAN ST A5140179 FA140092 CB131224 8 2345 OCEAN ST A5140180 FA140093 CB131226 9 2353 OCEAN ST AS140181 FA140094 CB131248 10 2363 OCEAN ST A5140182 FA140095 CB131233 11 2373 OCEAN ST AS140183 FA140096 CB131237 12 2383 OCEAN ST A5140184 FA140097 CB131241 13 2393 OCEAN ST A5140185 J FA140098 CB131245 14 03 oceAw sr A1S46Z00 I _ - - I gob INNOVATIVE FIRE PROTECTION, INC. I I OVERHEAD FIRE SPRINKLER SYSTEM I ENGINEERING SUBMITTAL I OCEAN STREET RESIDENCES 2303 OCEAN ST. CARLSBAD, CA 92008 MAY 309 2014 lh.e 111:1 It's IIaV t)e2:I viitvd mi ppaIeitI iiurliaIice v. tb citiritit apphcihic cnks md tiandids in ftircc ii he jiiishemniii, Thu imtern (:iiirt:iii mine ii is vnw fl UppFi ni ii npiIiC:i!iii tot o hmldmii! scot-mi 5 iii the C\PECSS Liii ni iii 5!! that his OS i'S ill ii!) V!I\ iCiC5CS din I55VtiCF CE (('I'frzmor or ttivir iritcsm!uti ei!i!i!iu_'nl ii UlVhiwo Rim sek respusinthtliv in ttd ciuuilplitimmen W ith Said isis iiti sitiuiiaids, ineiudmiig he butte inn lode i' toe aimy rs1smiimnmhiily or ulciuctenciese Fines. 1115!,umuns or neatincimee in lhesc plmns su iiIier s,r 'mm iuuieui in 111i, review. i)!ie7/P(6((4 Reviewei:/ th.mEMMI':NI) At-I-ROyAl E I (DM1-tENt) .\i'PROV\I AS NOTED 8779 Cottonwood Ave., Ste. 101 a Santee, CA 92071 • TEL: 619.593.8200 • FAX: 619.593.9133 ifpinc.net • CA License #C.16.711148 I 1 I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 6/2/2014 C:\HASS84\D5376 OCEAN ST DA GAR 01.SDF JOE TITLE: OCEAN STREET GARAGE 16x16 WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. 8 DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SRi 83.7 74.2 859.8 78.4 630.3 58.3 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 630.3 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 250.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 380.3 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM). SRi 0.0 SOURCE 58.3 380.3 R21 0.0 - - - - 58.0 - - - P21 0.0 - - - - 44.0 - - - DPi 0.0 - - - - 42.8 - - - BR1 1.0 - - - - 41.7 - - - TR1 9.0 - - - - 36.5 - - - 1A 9.0 - - - - 29.5 - - - lB 9.0 - - - - 26.2 - - - 1C 9.0 - - - - 21.2 - - - 1D 9.0 - - - - 20.9 - - - 1E 9.0 - - - - 20.8 - - - 1CR 9.5 - - - - 20.7 - - - 1DR 9.5 - - - - 18.1 - - 1ER 9.5 - - - - 18.2 - - - 101 9.5 K=11.20 20.0 50.1 102 9.5 K=11.20 15.0 43.4' 103 9.5 K=11.20 14.6 42.8 104 9.5 K=11.20 13.9 41.8 105 9.5 K=11.20 13.7 41.5 106 9.5 K=11.20 14.2 42.2 107 9.5 K=11.20 12.9 40.2 108 9.5 K=11.20 12.3 39.3 109 9.5 K=11.20 12.1 39.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 6/2/2014 C:\HASS84\D5376 OCEAN ST DA GAR 01.SDF JOB TITLE: OCEAN STREET GARAGE 16x16 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) FL/FT (PSI) Pipe: 1 380.3 5.850 PL 20.00 PF 0.3 SRI 0.0 SRCE 58.3 (N/A) 4.5 150 FTG TG PE 0.0 R21 0.0 0.0 58.0 0.0 0.005 TL 71.00 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE R21 0.0 0.0 58.0 0.0 14.0 psi, 380.3 gpm P21 0.0 0.0 44.0 0.0 Pipe: 3 380.3 5.850 PL 125.50 PF 1.2 P21 0.0 0.0 44.0 0.0 4.5 150 FTG 6E PE 0.0 DPi 0.0 0.0 42.8 0.0 0.005 TL 257.50 PV Pipe: 4 380.3 4.026 PL 4.00 PF 0.6 DPi 0.0 0.0 42.8 0.0 9.6 120 FTG E PE -0.4 BR1 1.0 0.0 41.7 0.0 0.043 TL 14.00 PV Pipe: 5 380.3 4.310 PL 9.00 PF 1.8 BR1 1.0 0.0 41.7 0.0 8.4 120 FTG ECG PE -3.5 TR1 9.0 0.0 36.5 0.0 0.031 TL 56.39 PV Pipe: 6 380.3 4.310 PL 184.50 PF 7.0 TR1 9.0 0.0 36.5 0.0 8.4 120 FTG 3E PE 0.0 1A 9.0 0.0 29.5 0.0 0.031 TL 226.32 PV Pipe: 7 380.3 4.310 PL 65.00 PF 3.3 1A 9.0 0.0 29.5 0.0 8.4 120 FTG 3E PE 0.0 lB 9.0 0.0 26.2 0.0 0.031 TL 106.82 PV Pipe: 8 380.3 4.310 PL 145.00 PF 4.9 lB 9.0 0.0 26.2 0.0 8.4 120 FTG E PE 0.0 1C 9.0 0.0 21.2 0.0 0.031 TL 158.94 PV Pipe: 9 330.2 4.310 PL 15.80 PF 0.4 1C 9.0 0.0 21.2 0.0 7.3 120 FTG ---- PE 0.0 1D 9.0 0.0 20.9 0.0 0.024 TL 15.80 PV Pipe: 10 160.8 4.310 PL 15.80 PF 0.1 1D 9.0 0.0 20.9 0.0 3.5 120 FTG ---- PE 0.0 lB 9.0 0.0 20.8 0.0 0.006 TL 15.80 PV Pipe: ii 50.1 2.203 PL 0.50 PP 0.3 1C 9.0 0.0 21.2 0.0 4.2 120 FTG T PE -0.2 iCR 9.5 0.0 20.7 0.0 0.019 TL 14.14 PV Pipe: 12 169.5 2.203 PL 0.50 PF 2.6 1D 9.0 0.0 20.9 0.0 14.3 120 FTG T PE -0.2 1DR 9.5 0.0 18.1 0.0 0.183 TL 14.14 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 6/2/2014 C:\HASS84\D5376 OCEAN ST DA GAR 01.SDF I JOB TITLE: OCEAN STREET GARAGE 16x16 - PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. I NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 13 160.8 2.203 PL 0.50 PF 2.3 1E 9.0 0.0 20.8 0.0 13.5 120 FTG T PE -0.2 I 1ER 9.5 0.0 18.2 0.0 0.166 TL 14.14 PV Pipe: 14 50.1 2.203 PL 24.00 PF 0.7 I 1CR 9.5 0.0 20.7 0.0 4.2 120 FTG T PE 0.0 101 9.5 11.2 20.0 50.1 0.019 TL 37.64 PV • Pipe: 15 169.5 2.203 PL 3.00 PF 3.0 I 1DR 9.5 0.0 18.1 0.0 14.3 120 FTG T PE 0.0 102 9.5 11.2 15.0 43.4 0.183 TL 16.64 PV Pipe: 16 63.0 2.203 PL 14.00 PF 0.4 • 102 9.5 11.2 15.0 43.4 5.3 120 FTG ---- PE 0.0 103 9.5 11.2 14.6 42.8 0.029 TL 14.00 PV I Pipe: 17 63.0 2.203 PL 14.00 PF 0.4 102 9.5 11.2 15.0 43.4 5.3 120 FTG ---- PE 0.0 103 9.5 11.2 14.6 42.8 0.029 TL 14.00 PV I Pipe: 18 83.3 2.203 PL 14.00 PF 0.7 103 9.5 11.2 14.6 42.8 7.0 120 FTG ---- PE 0.0 I 104 9.5 11.2 13.9 41.8 0.049 TL 14.00 PV Pipe: 19 41.5 2.203 PL 15.00 PF 0.2 104 9.5 11.2 13.9 41.8 3.5 120 FTG ---- PE 0.0 I 105 9.5 11.2 13.7 41.5 0.014 TL 15.00 PV Pipe: 20 160.8 2.203 PL 10.30 PF 4.0 I 1ER 106 9.5 9.5 0.0 11.2 18.2 14.2 0.0 42.2 13.5 120 0.166 FTG TL T 23.94 PE PV 0.0 Pipe: 21 118.5 2.203 PL 14.00 PF 1.3 106 9.5 11.2 14.2 42.2 10.0 120 FTG ---- PE 0.0 I 107 9.5 11.2 12.9 40.2 0.094 TL 14.00 PV - Pipe: 22 78.3 2.203 PL 14.00 PF 0.6 I 107 9.5 11.2 12.9 40.2 6.6 120 FTG ---- PE 0.0 108 9.5 11.2 12.3 39.3 0.044 TL 14.00 PV • Pipe: 23 39.0 2.203 PL 14.00 PF 0.2 1 108 9.5 11.2 12.3 39.3 3.3 120 FTG ---- PE 0.0 109 9.5 11.2 12.1 39.0 0.012 TL 14.00 PV I I I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 6/2/2014 C:\HASS84\D5376 OCEAN ST DA GAR 01.SDF I JOB TITLE: OCEAN STREET GARAGE 16x16 NOTES (HASS) I Calculations were performed by the HASS 8.4 computer program under license no. 16080621 granted by HRS Systems, Inc. 208 Southside Square I Petersburg, TN 37144 (931) 659-9760 I The system has been calculated to provide an average imbalance at each node of 0.003 gpm and a maximum imbalance at any node of 0.074 gpm. I (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 14.3 ft/sec at pipe 12. 1 Items listed in bold print on the cover sheet are automatically transferred from the calculation report. Available pressure at source node SRl under full flow conditions is psi compared to the minimum required pressure of 20.00 psi. I 76.95 PIPE FITTINGS TABLE I Pipe Table Name: STANDARD.PIP PAGE: A MATERIAL: S40 HWC: 120 I Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPVlv NPTee I 4.026 10.00 20.00 6.00 22.00 12.00 2.00 20.00 20.00 20.00 PAGE: E MATERIAL: PVC200 HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) K T L C B G N I Ell Tee LngEll ChkVlv BfyVlv GatVlv NPTee 5.850 22.00 46.00 14.00 49.00 15.00 5.00 46.00 I PAGE: G MATERIAL: DynaFlow HWC: 120 - Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPVlv NPTee I 2.203 6.82 13.64 4.09 15.00 8.18 1.36 13.64 13.64 13.64 4.310 13.94 27.87 8.36 30.66 16.72 2.79 27.87 27.87 27.87 I I I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 6/2/2014 C:\HASS84\D5376 OCEAN ST DA GAR 01.SDF JOB TITLE: OCEAN STREET GARAGE 16x16 N 0 0 0 0 0 0 0 0 0 • co (N 0 I I I I I I I a co tT Lf) co 0 H U) a 0 (N -H U) 0 H 0) a 00 -H 4J CL4 (a 4J (I) H SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 6/2/2014 C:\HASS84\D5376 OCEAN ST DA GAR 01.SDF JOB TITLE: OCEAN STREET GARAGE 16x16 WATER SUPPLY CURVE 84*\\\\\\\\ I \\\\\\\\ I \\\0\\\\ 77+ \\\\\\\\ I \\\\\\\\ I 74.2 psi 8 860 gpm-> * I Flow Test Point 70+ 63+ I x P 56+ R I E S I S 49+ U I R I E I 42+ P I S I 35+ 28+ 21+ 14+ LEGEND I X = Required Water Supply I 58.29 psi 8 630.3 gpm 7+ I 0 = Available Water Supply I 78.35 psi 8 630.3 gpm ------+------+--------+--------+---------+-----------+ 200 300 400 500 600 700 800 900 1000 FLOW (GPM) I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 6/4/2014 C:\HASSE3\D5379 OCEAN STREET 13D 1 2HD.SDF I JOB TITLE: D5379 OCEAN STREET 13-D UNIT 1 WATER SUPPLY DATA I SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) 1 83.7 74.2 859.0 83.7 31.5 56.2 AGGREGATE FLOW ANALYSIS: FLOW AT SOURCE 31.5 GPM 'TOTAL TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.. 0 GPM OTHER HOSE STREAM ALLOWANCES 5 .0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 26.5 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE I (FT) (PSI) (GPM) SOURCE 56.2 31.5 Ml I l0.0 0.0 - - - - 55.9 - - - M2 0.0 - - - - 52.9 - - - R 2.5 - - - - 51.7 - - - I P 2.5 - - - - 40.7 - - - 2A 0.0 - - - - 41.7 - - - 2B 0.0 - - - - 41.6 - - - • 2C 0.0 - - - - 41.4 - - - 2D 0.0 - - - - 40.7 - - - 2E 0.0 - - - - 39.6 - - - 0.0. - - - - 37.9 I 3A 3B 12.5 HOSE STREAM 31.5 5.0 3 14.5 - - - - 27.9 - - - 4 16.0 - - - - 26.8 - - - 16.5 - - - - 26.4 - - - I 4A 4B 17.0 - - - - 24.7 - - - 4C 18.0 - - - - 21.6 - - - 6 I 33.0 33.0 - - - - - - - - 9.1 8.5 - - - - - - 6A 32.0 - - - - 8.9 - - - 7 33.0 - - - - 8.1 - - - I 8 33.0 - - - - - - - 8A 32.0 K= 4.90 7.6 13.5 9 33.0 - - - - 7.5 - - - 9A 32.0 K= 4.90 7.0 13.0 I I I ' SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN STREET 13D 1 2HD.SDF I JOB TITLE: D5379 OCEAN STREET 13-D UNIT 1 PIPE DATA I PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) I Pipe: 1 31.5 1.959 PL 10.00 PF 0.2 - 1 0.0 SRCE 56.2 (N/A) 3.4 150 FTG TG PE 0.0 Ml 0.0 0.0 55.9 0.0 0.010 TL 26.00 PV I Pipe: 2 FIXED PRESSURE LOSS DEVICE Ml 0.0 0.0 55.9 0.0 3.0 psi, 31.5 gpm I M2 0.0 0.0 52.9 0.0 Pipe: 3 31.5 1.959 PL 3.00 PF 0.1 M2 0.0 0.0 52.9 0.0 3.4 150 FTG 2E PE -1.1 R 2.5 0.0 51.7 0.0 0.010 TL 15.00 PV Pipe: 4 FIXED PRESSURE LOSS DEVICE 2.5 0.0 51.7 0.0 11.0 psi, 31.5 gpm I R P 2.5 0.0 40.7 0.0 • Pipe: 5 31.5 2.445 PL 10.00 PF 0.1 I P 2.5 0.0 40.7 0.0 2.2 150 FTG 2E PE 1.1 2A 0.0 0.0 41.7 0.0 0.003 TL 30.00 PV I Pipe: 6 31.5 3.068 PL 35.00 PF 0.1 I 2A 0.0 0.0 41.7 0.0 1.4 150 FTG T PE 0.0 2B 0.0 0.0 41.6 0.0 0.001 TL 60.00 PV I Pipe: 7 31.5 2.445 PL 60.00 PF 0.2 2B 0.0 0.0 41.6 0.0 2.2 150 FTG E PE 0.0 2C 0.0 0.0 41.4 0.0 0.003 TL 70.00 PV I Pipe: 8 31.5 2.067 PL 80.00 PF 0.7 2C 0.0 0.0 41.4 0.0 3.0 150 FTG L2E PE 0.0 I 2D 0.0 0.0 40.7 0.0 0.007 TL 98.00 PV Pipe: 9 31.5 1.610 PL 35.00 PF 1.0 0.0 0.0 40.7 0.0 5.0 150 FTG E PE 0.0 I 2D 2E 0.0 0.0 39.6 0.0 0.025 TL 41.00 PV Pipe: 10 31.5 1.610 PL 25.00 PF 1.8 0.0 0.0 39.6 0.0 5.0 150 FTG 5E2T PE 0.0 I 2E 3A 0.0 0.0 37.9 0.0 0.025 TL 71.00 PV • Pipe: 11 31.5 1.505 PL 15.00 PF 1.0 I 3A 0.0 0.0 37.9 0.0 5.7 150 FTG ET PE -5.4 3B 12.5 H.S. 31.5 5.0 0.034 TL 28.00 PV I Pipe: 12 26.5 1.101 PL 10.00 PF 2.8 • 3B 12.5 H.S. 31.5 5.0 8.9 150 FTG 2E PE -0.9 - 3 14.5 0.0 27.9 0.0 0.115 TL 24.00 PV I I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN STREET 13D 1 2HD.SDF I JOB TITLE: D5379 OCEAN STREET 13-D UNIT 1 PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. - END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 13 26.5 1.101 PL 3.00 PF 0.5 0.0 27.9 0.0 8.9 150 FTG C PE -0.6 4 1 14.5 16.0 0.0 26.8 0.0 0.115 TL 4.00 PV Pipe: 14 26.5 1.101 PL 1.00 PF 0.1 I 4 16.0 0.0 26.8 0.0 8.9 150 FTG ---- PE -0.2 4A 16.5 0.0 26.4 0.0 0.115 TL 1.00 PV I Pipe: 15 26.5 1.101 PL 1.00 PF 1.5 4A 16.5 0.0 26.4 0.0 8.9 150 FTG EB PE -0.2 4B 17.0 0.0 24.7 0.0 0.115 TL 13.00 PV 1 Pipe: 16 26.5 1.049 PL 1.00 PF 2.6 - 4B 17.0 0.0 24.7 0.0 9.9 120 FTG BT PE -0.4 4C 18.0 0.0 21.6 0.0 0.220 TL 12.00 PV I Pipe: 17 26.5 1.101 PL 37.00 PF 6.1 4C 18.0 0.0 21.6 0.0 8.9 150 FTG 2E2R PE -6.5 I 5 33.0 0.0 9.1 0.0 0.115 TL 53.00 PV Pipe: 18 8.9 1.101 PL 30.00 PF 0.6 5 33.0 0.0 9.1 0.0 3.0 150 FTG B5R PE 0.0 I 6 33.0 0.0 8.5 0.0 0.015 TL 40.00 PV Pipe: 19 0.0 1.101 PL 13.00 PF 0.0 33.0 0.0 8.5 0.0 0.0 150 FTG BR PE 0.4 I 6 6A 32.0 0.0 8.9 0.0 0.000 TL 19.00 PV Pipe: 20 8.9 1.101 PL 21.00 PF 0.4 I 6 33.0 0.0 8.5 0.0 3.0 150 FTG SR PE 0.0 7 33.0 0.0 8.1 0.0 0.015 TL 26.00 PV I Pipe: 21 8.9 1.101 PL 22.00 PF 0.6 1 7 33.0 0.0 8.1 0.0 3.0 150 FTG 2EBR PE 0.0 8 33.0 0.0 7.4 0.0 0.015 TL 42.00 PV I Pipe: 22 13.5 1.101 PL 1.00 PF 0.2 - 8 33.0 0.0 7.4 0.0 4.6 150 FTG BR PE 0.4 8A 32.0 4.9 7.6 13.5 0.033 TL 7.00 PV I Pipe: 23 -4.7 1.101 PL 13.00 PF 0.1 8 33.0 0.0 7.4 0.0 1.6 ISO FTG ---- PE 0.0 I 9 33.0 0.0 7.5 0.0 0.005 TL 13.00 PV Pipe: 24 13.0 1.101 PL 9.00 PF 0.9 9 33.0 0.0 7.5 0.0 4.4 150 FTG 2EBR PE 0.4 9A 32.0 4.9 7.0 13.0 0.031 TL 29.00 PV Pipe: 25 -17.7 1.101 PL 26.00 PF 1.6 0.0 7.5 0.0 6.0 150 FTG 3R PE 0.0 5 I 33.0 33.0 0.0 9.1 0.0 0.054 TL 29.00 PV I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN STREET 13D 1 2HD.SDF JOB TiTLE: D5379 OCEAN STREET 13-D UNIT 1 NOTES (HASS) Calculations were performed by the HASS 8.4 computer program under license no. 16080621 granted by HRS Systems, Inc. 208 Southside Square Petersburg, TN 37144 (931) 659-9760 The system has been calculated to provide an average imbalance at each node of 0.003 gpm and a maximum imbalance at any node of 0.069 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 9.9 ft/sec at pipe 16. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. Available pressure at source node 1 under full flow conditions is 83.66 psi compared to the minimum required pressure of 20.00 psi. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPVlv NPTee 1.049 2.00 5.00 2.00 5.00 6.00 1.00 10.00 10.00 5.00 PAGE: E MATERIAL: PVC150 HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Ell Tee LngEll ChkVlv BfyVlv GatVlv NPTee 1.610 6.00 8.00 3.00 14.00 7.00 3.00 11.00 2.067 7.00 10.00 4.00 17.00 8.00 3.00 10.00 2.445 10.00 15.00 6.00 23.00 9.00 3.50 17.00 3.068 13.00 25.00 8.00 30.00 10.00 4.00 25.00 I I I I I 1 I I LI I I I I I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN STREET 13D 1 2HD.SDF I JOB TITLE: D5379 OCEAN STREET 13-D UNIT 1 PAGE: F MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) L E B R C S G I 45 El BrT RunT Cpig SwCk Gate 1.101 1.00 7.00 5.00 1.00 1.00 8.00 2.00 PAGE: K MATERIAL: CT-K HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R C S G N I Eli Tee 45-Eli TeeRun Coupig SwgChk GatViv NPTee 1.959 6.00 12.00 3.00 4.00 0.50 13.00 4.00 12.00 L MATERIAL: CT-L HWC: 150 I PAGE: Diameter Equivalent Fitting Lengths in Feet (in) E T F R C S G N Eli Tee 45-Eli TeeRun Couplg SwgChk GatVlv NPTee I 1.505 4.00 9.00 2.00 3.00 0.50 10.00 0.00 9.00 Li I I r I I I I I I I I U I E Lf) 0 H I-1 CD 04 'ct1 N co CD 0 U)N H. CJ)r co 41 o 41 P4 U) co [1 E 04 cz Q)bl bCJO a) (I)• i (I)- -104r Q)m um04E a) a 04 CJ) 04 EU-H -1Q) tTh Hw 'CoOa) 4 ,Q04 W04J) &1 cj -1 r1 HLL)O>i 11 c_ •o -CI)CO r. . -i W.o . . co U4CD .-1 N 0 0 0 H I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 6/4/2014 C:\HASS83\b5379 OCEAN STREET 13D 1 2HD.SDF JOB TITLE: D5379 OCEAN STREET 13-D UNIT 1 H N L- 0 o 0 0 0 0 ••• • H 0 0 0 • 0 0 0 0 00 N -04 CD-H-- I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN STREET 13D 1 2HD.SDF JOB TITLE: D5379 OCEAN STREET 13-D UNIT 1 I WATER SUPPLY CURVE I 840\\\\\\\\ \\\\\\\\ I I I I I I I I I I I I I I I I \\\\\\\\ 77+ \\\\\\\\ I \\\\\\\\ 74.2 psi @ 859 gpm-> * I Flow Test Point 70+ 63+ P 56X RI El S 49+ UI RI El 42+ P I S I 35+ ) I 28+ 21+ 14+ LEGEND X = Required Water Supply I 56.15 psi @ 31.5 gpm 7+ I 0 = Available Water Supply 83.68 psi @ 31.5 gpm 0++-+---+----+-----+ ------+ --------+ --------+ ---------+ -----------+ 200 300 400 500 600 700 800 900 1000 FLOW (GPM) I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN STREET 13D 1 1HD.SDF JOB TITLE: D5379 OCEAN STREET 13-D UNIT 1 I WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D I NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) I 1 83.7 74.2 859.0 83.7 25.0 58.4 AGGREGATE FLOW ANALYSIS: I TOTAL FLOW TOTAL HOSE AT SOURCE STREAM ALLOWANCE AT SOURCE 25.0 GPM 0.0 GPM OTHER HOSE STREAM ALLOWANCES 5.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 20.0 GPM I NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE I (FT) (PSI) (GPM) 1 0.0 SOURCE 58.4 25.0 I Ml 0.0 - - - - 58.3 - - - M2 0.0 - - - - 55.3 - - - R 2.5 - - - - 54.1 - - - 2.5 - - - - 43.1 I .P 2A 0.0 - - - - 44.1 - - - 2B 0.0 - - - - 44.1 - - - 0.0 - - - - 43.9 - - - I 2C 2D 0.0 - - - - 43.4 - - - 2E 0.0 - - - - 42.8 - - - 3A 0.0 - - - - 41.6 - - - 12.5 HOSE STREAM 35.6 5.0 I 3B 3 14.5 - - - - 33.1 - - - 4 16.0 - - - - 32.2 - - - I 4A 4B 16.5 - - - - 17.0 - - - - 31.9 30.8 - - - - - - 4C 18.0 - - - - 28.8 - - - 5 33.0 - - - - 18.7 - - - I 6 33.0 - - - - 17.5 - - - 6A 32.0 K= 4.90 16.7 20.0 7 33.0 - - - - 17.8 - - - 33.0 - - - - 18.2 - - - I 8 8A 32.0 - - - - 18.7 - - - 9 33.0 - - - - 18.4 - - - 9A 32.0 - - - - 18.8 - - - I I I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN STREET 13D 1 1HD.SDF TITLE: D5379 OCEAN STREET 13-D UNIT 1 I JOB PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. I END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 1 25.0 1.959 PL 10.00 PF 0.2 • 1 0.0 SRCE 58.4 (N/A) 2.7 150 FTG TG PE 0.0 Ml 0.0 0.0 58.3 0.0 0.006 TL 26.00 PV I Pipe: 2 FIXED PRESSURE LOSS DEVICE Ml 0.0 0.0 58.3 0.0 3.0 psi, 25.0 gpm I M2 0.0 0.0 55.3 0.0 Pipe: 3 25.0 1.959 PL 3.00 PF 0.1 M2 0.0 0.0 55.3 0.0 2.7 150 FTG 2E PE -1.1 R 2.5 0.0 54.1 0.0 0.006 TL 15.00 PV Pipe: 4 FIXED PRESSURE LOSS DEVICE 2.5 0.0 54.1 0.0 11.0 psi, 25.0 gpm I R P 2.5 0.0 43.1 0.0 Pipe: 5 25.0 2.445 PL 10.00 PF 0.1 I P 2.5 0.0 43.1 0.0 1.7 150 FTG 2E PE 1.1 2A 0.0 0.0 44.1 0.0 0.002 TL 30.00 PV • Pipe: 6 25.0 3.068 PL 35.00 PF 0.0 • 2A 0.0 0.0 44.1 0.0 1.1 150 FTG T PE 0.0 2B 0.0 0.0 44.1 0.0 0.001 TL 60.00 PV Pipe: 7 25.0 2.445 PL 60.00 PF 0.1 2B 0.0 0.0 44.1 0.0 1.7 150 FTG E PE 0.0 2C 0.0 0.0 43.9 0.0 0.002 TL 70.00 PV I Pipe: 8 25.0 2.067 PL 80.00 PF 0.5 2C 0.0 0.0 43.9 0.0 2.4 1150 FTG L2E PE 0.0 I 2D 0.0 0.0 43.4 0.0 0.005 TL 98.00 PV Pipe: 9 25.0 1.610 PL 35.00 PF 0.7 2D 0.0 0.0 43.4 0.0 3.9 150 FTG E PE 0.0 2E 0.0 0.0 42.8 0.0 0.016 TL 41.00 PV Pipe: 10 25.0 1.610 PL 25.00 PF 1.1 0.0 0.0 42.8 0.0 3.9 150 FTG 5E2T PE 0.0 I 2E 3A 0.0 0.0 41.6 0.0 0.016 TL 71.00 PV - Pipe: 11 25.0 1.505 PL 15.00 PF 0.6 I 3A 0.0 0.0 41.6 0.0 4.5 150 FTG ET PE -5.4 3B 12.5 H.S. 35.6 5.0 0.022 TL 28.00 PV I Pipe: 12 20.0 1.101 PL 10.00 PF 1.6 I 3B 12.5 H.S. 35.6 5.0 6.7 150 FTG 2E PE -0.9 3 14.5 0.0 33.1 0.0 0.068 TL 24.00 PV I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN STREET 13D 1 1HD.SDF TITLE: D5379 OCEAN STREET 13-D UNIT 1 I JOB PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. - END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. I NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 13 20.0 1.101 PL 3.00 PF 0.3 4 I 14.5 16.0 0.0 0.0 33.1 32.2 0.0 0.0 6.7 150 0.068 FTG TL C 4.00 PE PV -0.6 Pipe: 14 20.0 1.101 PL 1.00 PF 0.1 16.0 0.0 32.2 0.0 6.7 150 FTG ---- PE -0.2 I 4 4A 16.5 0.0 31.9 0.0 0.068 TL 1.00 PV • Pipe: 15 20.0 1.101 PL 1.00 PF 0.9 4A 16.5 0.0 31.9 0.0 6.7 150 FTG EB PE -0.2 4B 17.0 0.0 30.8 0.0 0.068 TL 13.00 PV I Pipe: 16 20.0 1.049 PL 1.00 PF 1.6 • 4B 17.0 0.0 30.8 0.0 7.4 120 FTG BT PE -0.4 4C 18.0 0.0 28.8 0.0 0.130 TL 12.00 PV I Pipe: 17 20.0 1.101 PL 37.00 PF 3.6 4C 18.0 0.0 28.8 0.0 67 150 FTG 2E2R PE -6.5 S 33.0 0.0 18.7 0.0 0.068 TL 53.00 PV I Pipe: 18 12.7 1.101 PL 30.00 PF 1.2 5 33.0 0.0 18.7 0.0 4.3 150 FTG BSR PE 0.0 I 6 33.0 0.0 17.5 0.0 0.029 TL 40.00 PV Pipe: 19 20.0 1.101 PL 13.00 PF 1.3 I 6 6A 33.0 32.0 0.0 4.9 17.5 16.7 0.0 20.0 6.7 150 0.068 FTG TL BR 19.00 PE PV 0.4 Pipe: 20 -7.3 1.101 PL 21.00 PF 0.3 I 6 33.0 0.0 17.5 0.0 2.5 150 FTG SR PE 0.0 7 33.0 0.0 17.8 0.0 0.011 TL 26.00 PV • Pipe: 21 -7.3 1.101 PL 22.00 PF 0.4 7 33.0 0.0 17.8 0.0 2.5 150 FTG 2EBR PE 0.0 8 33.0 0.0 18.2 0.0 0.011 TL 42.00 PV I Pipe: 22 0.0 1.101 PL 1.00 PF 0.0 • 8 33.0 0.0 18.2 0.0 0.0 150 FTG BR PE 0.4 8A 32.0 0.0 18.7 0.0 0.000 TL 7.00 PV U Pipe:. 23 -7.3 1.101 PL 13.00 PF 0.1 8 33.0 0.0 18.2 0.0 2.5 150 FTG ---- PE 0.0 9 33.0 0.0 18.4 0.0 0.011 TL 13.00 PV I Pipe: 24 0.0 1.101 PL 9.00 PF 0.0 9 33.0 0.0 18.4 0.0 0.0 150 FTG 2EBR PE 0.4 9A 32.0 0.0 18.8 0.0 0.000 TL 29.00 PV Pipe: 25 -7.3 1.101 PL 26.00 PF 0.3 0.0 18.4 0.0 2.5 150 FTG 3R PE 0.0 5 I 33.0 33.0 0.0 18.7 0.0 0.011 TL 29.00 PV I P SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN STREET 13D 1 1HD.SDF JOB TITLE: D5379 OCEAN STREET 13-D UNIT 1 I NOTES (HASS) Calculations were performed by the HASS 8.4 computer program under license no. 16080621 granted by HRS Systems, Inc. 208 Southside Square Petersburg, TN 37144 (931) 659-9760 The system has been calculated to provide an average imbalance at each node of 0.004 gpm and a maximum imbalance at any node of 0.099 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 7.4 ft/sec at pipe 16. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. Available pressure at source node 1 under full flow conditions is 83.68 psi compared to the minimum required pressure of 20.00 psi. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP I PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N I Eli Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPVlv NPTee 1.049 2.00 5.00 2.00 5.00 6.00 1.00 10.00 10.00 5.00 I PAGE: E Diameter (in) 1.610 2.067 2.445 3.068 MATERIAL: PVC150 HWC: 150 Equivalent Fitting Lengths in Feet E T L C B G N Ell Tee LngEll ChkVlv BfyVlv GatVlv NPTee 6.00 8.00 3.00 14.00 7.00 3.00 11.00 7.00 10.00 4.00 17.00 8.00 3.00 10.00 10.00 15.00 6.00 23.00 9.00 3.50 17.00 13.00 25.00 8.00 30.00 10.00 4.00 25.00 I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN STREET 13D 1 1HD.SDF I . JOB TITLE: D5379 OCEAN STREET 13-D UNIT 1 PAGE: FMATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet I (in) L E B R C S G 45 El BrT RunT Cplg SwCk Gate 1.101 1.00 7.00 5.00 1.00 1.00 8.00 2.00 PAGE: K Diameter (in) 1 1.959 PAGE: L Diameter (in) 1.505 I I LI I I I I I I I I I MATERIAL: CT-K HWC: 150 Equivalent Fitting Lengths in Feet E T F R C S G N Ell Tee 45-Ell TeeRun Couplg SwgChk GatVlv NPTee 6.00 12.00 3.00 4.00 0.50 13.00 4.00 12.00 MATERIAL: CT-L HWC: 150 Equivalent Fitting Lengths in Feet E T F R C S G N Eli Tee 45-Eli TeeRun Couplg SwgChk GatVlv NPTee 4.00 9.00 2.00 3.00 0.50 10.00 0.00 9.00 I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN STREET 13D 1 1HD.SDF JOB TITLE: D5379 OCEAN STREET 13-D UNIT 1 I 0 0 0 H I co IS) I 0 H -1 I 04 0 04 -H C!) I -H Cl) I CJ)N H . CJ)m P E a 04 Wb bloo l-i a) O lO>i'U UI UILfl u)Lr -(ca 1-4 U) a) 04 UI) )C!)0 HUI -. rd(j)O(a U)Qil-44-) (U HG 1-1 U) -HC'O>i -.-ILO PC1)CJ) Y-- m W•-- 00 00 14 Ln I 3I I I N 0 0 0 0 0 0 H 0 0 0 0 0 0 0 00 N 00 I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN STREET 13D 1 1HD.SDF I JOB TITLE: D5379 OCEAN STREET 13-D UNIT 1 WATER SUPPLY CURVE I 840\\\\\\\\ I \\\\\\\\ \\\\\\\\ I 77+ \\\\\\\\ \\\\\\\\ \\\\\\\\ 74.2 psi @ 859 gpm-> * I I Flow Test Point 70+ 63+ x P 56+ RI El S 49+ UI RI El 42+ 28+ 21+ 14+ LEGEND I X = Required Water Supply I 58.42 psi @ 25.0 gpm 7+ I 0 = Available Water Supply 83.69 psi @ 25.0 gpm I I? 0++-+---+----+-----+ ------+ --------+ --------+ ---------+ -----------+ 200 300 400 500 600 700 800 900 1000 FLOW (GPM) I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B8 ATTIC 7HD.SDF I JOB TITLE: D5379 OCEAN STREET BLDG 8 WATER SUPPLY DATA I SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SR2 83.7 74.2 859.0 82.6 270.4 81.7 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 270.4 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 170.4 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE I (FT) (PSI) (GPM) 0.0 SOURCE 81.7 170.4 I SR2 R2 2.5 - - - - 80.2 - - - P2 2.5 - - - - 69.2 - - - UG2 0.0 - - - - 69.6 - - - I B8 1.5 - - - - 67.1 - - - BOR 2.5 - - - - 62.3 - - - TOR 6.5 - - - - 55.2 - - - 10.0 - - - - 47.2 - - - I 1A 1A1 10.0 - - - - 47.5 - - - 1A2 10.0 - - - - 45.0 - - - lB 10.0 - - - - 43.5 - - - I 1C 10.0 - - - - 43.3 - - - 1D 10.0 - - - - 43.3 - - - 1E 10.0 - - - - 43.1 - - - 20.0 - - - - 38.8 - - - I 2A 2B 20.0 - - - - 38.6 - - - 2B1 20.0 - - - - 40.0 - - - 20.0 - - - - 36.9 - - - I 2C 2D 20.0 - - - - 37.0 - - - 2E 20.0 - - - - 35.2 - - - 2F 20.0 - - - - 34.7 - - - I 2G 20.0 - - - - 32.9 - - - 2H 20.0 - - - - 31.7 - - - 21 20.0 - - - - 31.9 - - - 20.0 - - - - 31.0 - - - I 2J 201 19.0 - - - - 35.6 - - - 202 19.0 - - - - 32.2 - - - 203 19.0 - - - - 32.3 - - - I 204 19.0 - - - - 31.5 - - - 3A 24.0 - - - 22.2 - - - 3B 24.0 - - - - 29.4 - - - 24.0 K= 5.60 20.9 5.6 I 301 302 24.0 K= 5.60 20.1 257 303 24.0 K= 5.60 19.9 25.0 I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B8 ATTIC 7HD.SDF I . JOB TITLE: D5379 OCEAN STREET BLDG 8 NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE I (FT) (PSI) 304 24.0 K= 5.60 20.0 24.0 K= 5.60 20.8 I 305 306 24.0 K= 4.20 27.7 22.1 307 24.0 K= 4.20 27.7 22.1 I I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B8 ATTIC 7HD.SDF TITLE: D5379 OCEAN STREET BLDG 8 I JOB PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. I END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 1 170.4 4.070 PL 17.00 PF 0.4 - SR2 0.0 SRCE 81.7 (N/A) 4.2 150 FTG ETG PE -1.1 R2 2.5 0.0 80.2 0.0 0.006 TL 71.00 PV I Pipe: 2 FIXED PRESSURE LOSS DEVICE R2 2.5 0.0 80.2 0.0 11.0 psi, 170.4 gpm I P2 2.5 0.0 69.2 0.0 Pipe: 3 170.4 4.070 PL 29.00 PF 0.7 P2 2.5 0.0 69.2 0.0 4.2 150 FTG 2ETL PE 1.1 UG2 0.0 0.0 69.6 0.0 0.006 TL 107.00 PV Pipe: 4 170.4 4.070 PL 200.00 PF 1.9 0.0 0.0 69.6 0.0 4.2 150 FTG 3ET2L PE -0.6 I UG2 B8 1.5 0.0 67.1 0.0 0.006 TL 305.00 PV - Pipe: 5 170.4 2.003 PL 3.00 PF 4.4 I B8 1.5 0.0 67.1 0.0 17.4 120 FTG 2E PE -0.4 BOR 2.5 0.0 62.3 0.0 0.294 TL 14.91 PV • Pipe: 6 170.4 2.067 PL 4.00 PF 5.3 • BOR 2.5 0.0 62.3 0.0 16.3 120 FTG BC PE -1.7 TOR 6.5 0.0 55.2 0.0 0.252 TL 21.00 PV Pipe: 7 170.4 2.003 PL 23.00 PF 6.2 TOR 6.5 0.0 55.2 0.0 17.4 150 FTG E PE -1.5 1A1 10.0 0.0 47.5 0.0 0.194 TL 32.00 PV I Pipe: 7A 89.5 2.003 PL 6.00 PF 0.4 1A1 10.0 0.0 47.5 0.0 9.1 150 FTG ---- PE 0.0 I 1A 10.0 0.0 47.2 0.0 0.059 TL 6.00 PV Pipe: 7B 80.9 2.003 PL 26.00 PF 3.1 10.0 0.0 47.5 0.0 8.2 150 FTG 2E2B PE -4.3 I 1A1 2B1 20.0 0.0 40.0 0.0 0.049 TL 64.00 PV Pipe: 8 89.5 1.598 PL 4.00 PF 2.1 10.0 0.0 47.2 0.0 14.3 150 FTG B PE 0.0 I 1A 1A2 10.0 0.0 45.0 0.0 0.177 TL 12.00 PV • Pipe: 8A 44.8 1.598 PL 32.00 PF 1.6 1A2 10.0 0.0 45.0 0.0 7.2 150 FTG ---- PE 0.0 lB 10.0 0.0 43.5 0.0 0.049 TL 32.00 PV Pipe: 9 33.7 2.003 PL 8.00 PF 0.2 U lB 10.0 0.0 43.5 0.0 3.4 150 FTG B PE 0.0 I I 1C 10.0 0.0 43.3 0.0 0.010 TL 18.00 PV I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B8 ATTIC 7HD.SDF TITLE: D5379 OCEAN STREET BLDG 8 I JOB PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 10 11.1 1.598 PL 37.00 PF 0.2 I lB 1D 10.0 10.0 0.0, 0.0 43.5 43.3 0.0 0.0 1.8 150 0.004 FTG TL E 44.00 PE PV 0.0 Pipe: 11 11.1 1.598 PL 40.00 PF 0.2 I 1D 10.0 0.0 43.3 0.0 1.8 150 FTG B PE 0.0 1E 10.0 0.0 43.1 0.0 0.004 TL 48.00 PV hA 44.7 1.598 PL 23.00 PF 1.9 I Pipe: 1A2 10.0 0.0 45.0 0.0 7.2 150 FTG 2B PE 0.0 1E 10.0 0.0 43.1 0.0 0.049 TL 39.00 PV I Pipe: 12 33.7 2.003 PL 10.00 PF 0.2 • 1C 10.0 0.0 43.3 0.0 3.4 150 FTG E PE -4.3 2A 20.0 0.0 38.8 0.0 0.010 TL 19.00 PV I Pipe: 13 33.7 2.003 PL 8.00 PF 0.2 2A 20.0 0.0 38.8 0.0 3.4 150 FTG E PE 0.0 I 2B 20.0 0.0 38.6 0.0 0.010 TL 17.00 PV Pipe: 14 66.9 1.598 PL 31.00 PF 3.9 2B 20.0 0.0 38.6 0.0 10.7 150 FTG E PE 0.0 I 2F 20.0 0.0 34.7 0.0 0.103 TL 38.00 PV Pipe: 15 -33.2 1.598 PL 35.00 PF 1.4 20.0 0.0 38.6 0.0 5.3 150 FTG 2B PE 0.0 I 2B 2B1 20.0 0.0 40.0 0.0 0.028 TL 51.00 PV Pipe: 15A 47.7 1.598 PL 35.00 PF 3.2 I 2B1 20.0 0.0 40.0 0.0 7.6 150 FTG 2EB PE 0.0 2C 20.0 0.0 36.9 0.0 0.055 TL 57.00 PV • Pipe: 16 -14.3 1.598 PL 7.00 PF 0.1 2C 20.0 0.0 36.9 0.0 2.3 150 FTG B PE 0.0 2D 20.0 0.0 37.0 0.0 0.006 TL 15.00 PV I Pipe: 17 55.8 2.003 PL 25.00 PF 1.8 • 1E 10.0 0.0 43.1 0.0 5.7 150 FTG 2E3B PE -4.3 2D 20.0 0.0 37.0 0.0 0.025 TL 73.00 PV Pipe: 18 41.5 1.598 PL 34.00 PF 1.8 2D 20.0 0.0 37.0 0.0 6.6 150 FTG B PE 0.0 I 2E 20.0 0.0 35.2 0.0 0.043 TL 42.00 PV Pipe: 19 41.5 1.598 PL 4.00 PF 0.5 2E 20.0 0.0 35.2 0.0 6.6 150 FTG B PE 0.0 I 2F 20.0 0.0 34.7 0.0 0.043 TL 12.00 PV Pipe: 20 0.0 1.101 PL 1.00 PF 0.0 20.0 0.0 35.2 0.0 0.0 150 FTG B PE 0.4 I 2E 201 19.0 0.0 35.6 0.0 0.000 TL 6.00 PV I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B8 ATTIC 7HD.SDF I JOB TITLE: D5379 OCEAN STREET BLDG 8 PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 21 108.4 1.598 PL 7.00 PF 1.8 I 2F 20.0 0.0 34.7 0.0 17.3 150 FTG ---- PE 0.0 2G 20.0 0.0 32.9 0.0 0.253 TL 7.00 PV Pipe: 22 64.2 1.598 PL 4.00 PF 1.2 I 2G 20.0 0.0 32.9 0.0 10.3 150 FTG B PE 0.0 2H 20.0 0.0 31.7 0.0 0.096 TL 12.00 PV Pipe: 23 0.0 1.101 PL 1.00 PF 0.0 2H 20.0 0.0 31.7 0.0 0.0 150 FTG B PE 0.4 202 19.0 0.0 32.2 0.0 0.000 TL 6.00 PV I Pipe: 24 44.2 1.394 PL 11.00 PF 1.0 2G 20.0 0.0 32.9. 0.0 9.3 150 FTG ---- PE 0.0 21 20.0 0.0 31.9 0.0 0.093 TL 11.00 PV Pipe: 25 0.0 1.101 PL 1.00 PF 0.0 21 20.0 0.0 31.9 0.0 0.0 150 FTG B PE 0.4 I 203 19.0 0.0 32.3 0.0 0.000 TL 6.00 PV Pipe: 26 44.2 1.394 PL 9.00 PF 0.8 21 20.0 0.0 31.9 0.0 9.3 150 FTG ---- PE 0.0 21 20.0 0.0 31.0 0.0 0.093 TL 9.00 PV Pipe: 28 0.0 1.101 PL 5.00 PF 0.0 I 21 20.0 0.0 31.0 0.0 0.0 150 FTG 2B PE 0.4 204 19.0 0.0 31.5 0.0 0.000 TL 15.00 PV Pipe: 29 . 64.2 1.394 PL 24.00 PF 7.8 I 2H 20.0 0.0 31.7 0.0 13.5 150 FTG 3E PE -1.7 3A 24.0 0.0 22.2 0.0 0.187 TL 42.00 PV Pipe: 30 64.2 1.394 PL 1.00 PF 1.3 3A 24.0 0.0 22.2 0.0 13.5 150 FTG E PE 0.0 301 24.0 5.6 20.9 25.6 0.187 TL 7.00 PV I Pipe: 31 38.7 1.394 PL 5.00 PF 0.8 301 24.0 5.6 20.9 25.6 8.1 150 FTG B PE 0.0 302 24.0 5.6 20.1 25.1 0.073 TL 11.00 PV I Pipe: 32 .13.6 1.394 PL 6.00 PF 0.1 302 24.0 5.6 20.1 25.1 2.9 150 FTG B PE 0.0 I 303 24.0 5.6 19.9 25.0 0.011 TL 12.90 PV Pipe: 33 -11.4 1.394 PL 6.00 PF 0.1 303 24.0 5.6 19.9 25.0 2.4 150 FTG B PE 0.0 I 304 24.0 5.6 20.0 25.1 0.008 TL 12.00 PV Pipe: 34 -36.5 1.394 PL 6.00 PF 0.8 I 304 24.0 5.6 20.0 25.1 7.7 150 FTG B PE 0.0 305 24.0 5.6 20.8 25.5 0.066 TL 12.00 PV I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B8 ATTIC 7HD.SDF I . JOB TITLE: D5379 OCEAN STREET BLDG 8 PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 35 -62.0 1.394 PL 43.00 PF 8.6 I 305 24.0 5.6 20.8 25.5 13.0 150 FTG B PE 0.0 3B 24.0 0.0 29.4 0.0 0.175 TL 49.00 PV Pipe: 36 -62.0 1.394 PL 15.00 PF 5.8 I 3B 24.0 0.0 29.4 0.0 13.0 150 FTG 2EB PE 1.7 2C 20.0 0.0 36.9 0.0 0.175 TL 33.00 PV Pipe: 37 22.1 1.101 PL 8.00 PF 1.6 21 20.0 0.0 31.0 0.0 7.4 150 FTG EB PE -1.7 307 24.0 4.2 27.7 22.1 0.082 TL 20.00 PV Pipe: 38 22.1 1.101 PL 8.00 PF 1.6 21 20.0 0.0 31.0 0.0 7.4 150 FTG EB PE -1.7 306 24.0 4.2 27.7 22.1 0.082 TL 20.00 PV I NOTES (HASS) I (1) Calculations were performed by the HASS 8.4 computer program under license no. 16080621 granted by HRS Systems, Inc. I 208 Southside Square Petersburg, TN 37144 (931) 659-9760 I (2) The system has been calculated to provide an average imbalance at each node of 0.003 gpm and a maximum I imbalance at any node of 0.102 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 17.4 ft/sec at pipe 7. Items listed in bold print on thecover sheet are automatically transferred from the calculation report. Available pressure at source node SR2 under full flow conditions is 82.57 psi compared to the minimum required pressure of 20.00 psi. I (6) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP I I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B8 ATTIC 7HD.SDF JOB TITLE: D5379 OCEAN STREET BLDG 8 PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet E T L C B G A D N (in) Eli Tee LngEil ChkVlv BfyVlv GatVlv AlmChk DPVlv NPTee 2.067 5.00 10.00 3.00 11.00 6.00 1.00 10.00 10.00 10.00 PAGE: F MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) L E B R C S G 45 El BrT RunT Cplg SwCk Gate 1.101 1.00 7.00 5.00 1.00 1.00 8.00 2.00 1.394 2.00 6.00 6.00 1.00 1.00 11.00 3.00 2.00 7.00 8.00 1.00 1.00 14.00 3.00 1.598 2.003 2.00 9.00 10.00 1.00 1.00 17.00 3.00 PAGE: H MATERIAL: PVC 200CLASS HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Eli Tee Long Check Butter Gate NPTee 4.070 17.00 34.00 10.00 37.00 20.00 3.00 34.00 I I I I I I I I I I I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B8 ATTIC 7HD.SDF JOB TITLE: D5379 OCEAN STREET BLDG 8 ' I (flO OH I (flN ()) N( LI) a a )c1)fl co W-H •-1W • I c1 flj L-1 H •,-100>j 0 fl ,-1L NCI)C)D (a - c') wI-i I 0 P4 P4 W H co 04 I CD 00 I'D cq I 0 0 0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 I DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B8 ATTIC 7HD.SDF - JOB TITLE: D5379 OCEAN STREET BLDG 8 WATER SUPPLY CURVE I 84*\\\\\\\\ I 0 \\\\\\\\ I I \\\\\\\\ 77+ \\\\\\\\ I 74.2 psi @ 859 gpm-> * I I Flow Test Point 70+ I 63+ P 56+ RI El SI S 49+ UI RI El 42+ P I SI I 35+ 28+ 21+ 14+ LEGEND I X = Required Water Supply 81.70 psi @ 270.4 gpm 7+ I 0 = Available Water Supply 82.58 psi @ 270.4 gpm 0 + + - +:- - - - - - - - + -----+ ------+ --------+ --------+ ---------+ -----------+ 200 300 400 500 600 700 800 900 1000 FLOW (GPM) I I I I I I I I I I I I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B8 SENJU 4HD.SDF - JOB TITLE: D5379 OCEAN STREET BLDG 8 I WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D I NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) 5R2 83.7 74.2 859.0 83.0 205.7 62.5 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 205.7 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 105.7 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE I (FT) (PSI) (GPM) SR2 0.0 SOURCE 62.5 105.7 R2 2.5 - - - - 61.2 - - - P2 2.5 - - - - 50.2 - - - UG2 0.0 - - - - 51.0 - - - 1.5 - - - - 49.6 - - - I B8 BOR 2.5. - - - - 47.3 - - - TOR 6.5 - - - - 43.4 - - - 10.0 - - - - 39.2 - - - I 1A 1A1 10.0 - - - - 39.3 - - - 1A2 10.0 - - - - 38.3 - - - lB 10.0 - - - - 37.6 - - - I 1C 10.0 - - - - 37.5 - - - 1D 10.0 - - - - 37.6 - - - 1E 10.0 - - - - 37.6 - - - 20.0 - - - - 33.1 - - - I 2A 2B 20.0 - - - - 33.0 - - - 2B1 20.0 - - - - 33.7 - - - 20.0 - - - - 32.7 - - - I 2C 2D 20.0 - - - - 32.6 - - - 2E 20.0 - - - - 30.9 - - - 2F 20.0 - - - - 30.8 - - - 20.0 - - - - 30.2 - - - I 2G 2H 20.0 - - - - 30.1 - - - 21 20.0 - - - - 28.8 - - - 20.0 - - - - 28.5 - - - I 2J 201 19.0 K=4.90 30.6 27.1 202 19.0 K= 4.90 29.8 26.8 203 19.0 K= 4.90 28.5 26.2 I 204 19.0 K= 4.90 27.3 25.6 3A 24.0 - - - - 29.0 - - - 3B 24.0 - - - - 30.5 - - - 24.0 - - - - 29.1 - - - I 301 - 302 24.0 - - - - 29.2 - - - 303 I 24.0 - - - - 29.4 - - - I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B8 SENJU 4HD.SDF JOB TITLE: D5379 OCEAN STREET BLDG 8 I i NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE I (FT) (PSI) (GPM) 304 24.0 - - - - 29.6 - - - 24.0 - - - - 29.8 - - - I 305 306 24.0 - - - - 26.7 - - - 307 24.0 - - - - 26.7 - - - 1 I I I I n 1 I I I I I I I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 6/4/2014 C:\HA5583\D5379 OCEAN ST DA B8 SENJU 4HD.SDF TITLE: D5379 OCEAN STREET BLDG 8 I JOB PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. I END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) I Pipe: 1 105.7 4.070 PL 17.00 PF 0.2 - SR2 0.0 SRCE 62.5 (N/A) 2.6 150 FTG ETG PE -1.1 R2 2.5 0.0 61.2 0.0 0.003 TL 71.00 PV I Pipe: 2 FIXED PRESSURE LOSS DEVICE R2 2.5 0.0 61.2 0.0 11.0 psi, 105.6 gpm I P2 2.5 0.0 50.2 0.0 Pipe: 3 105.6 4.070 PL 29.00 PF 0.3 P2 2.5 0.0 50.2 0.0 2.6 150 FTG 2ETL PE 1.1 UG2 0.0 0.0 51.0 0.0 0.003 TL 107.00 PV Pipe: 4 105.6 4.070 PL 200.00 PF 0.8 0.0 0.0. 51.0 0.0 2.6 150 FTG 3ET2L PE -0.6 I UG2 BS 1.5 0.0 49.6 0.0 0.003 TL 305.00 PV Pipe: 5 105.6 2.003 PL 3.00 PF 1.8 I B8 1.5 0.0 49.6 0.0 10.8 120 FTG 2E PE. -0.4 BOR 2.5 0.0 47.3 0.0 0.121 TL 14.91 PV I Pipe: 6 105.6 2.067 PL 4.00 PF 2.2 I BOR 2.5 0.0 47.3 0.0 10.1 120 FTG BC PE -1.7 TOR 6.5 0.0 43.4 0.0 . 0.104 TL 21.00 PV I Pipe: 7 105.6 2.003 PL 23.00 PF 2.6 - TOR 6.5 0.0 43.4 0.0 10.8 150 FTG E PE -1.5 1A1 10.0 0.0 39.3 0.0 0.080 TL 32.00 PV U Pipe: 7A 55.8 2.003 PL 6.00 PF 0.1 1A1 10.0 0.0 39.3 0.0 5.7 150 FTG ---- PE 0.0 I 1A 10.0 0.0 39.2 0.0 0.025 TL 6.00 PV Pipe: 7B 49.8 2.003 PL 26.00 PF 1.3 1A1 10.0 0.0 39.3 0.0 5.1 150 FTG 2E2B PE -4.3 2B1 20.0 0.0 33.7 0.0 0.020 TL 64.00 PV Pipe: 8 55.8 1.598 PL 4.00 PF 0.9 10.0 0.0 39.2 0.0 8.9 150 FTG B PE 0.0 I 1A 1A2 10.0 0.0 38.3 0.0 0.074 TL 12.00 PV • Pipe: 8A 28.9 1.598 PL 32.00 PF 0.7 I 1A2 10.0 0.0 38.3 0.0 4.6 150 FTG ---- PE 0.0 lB 10.0 0.0 37.6 0.0 0.022 TL 32.00 PV I Pipe: 9 25.1 2.003 PL 8.00 PF 0.1 • lB 10.0 0.0 37.6 0.0 2.6 150 FTG B PE 0.0 1C 10.0 0.0 37.5 0.0 0.006 TL 18.00 PV I I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B8 SENJU 4HD.SDF TITLE: D5379 OCEAN STREET BLDG 8 I JOB PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 10 3.8 1.598 PL 37.00 PF 0.0 I lB 1D 10.0 10.0 0.0 0.0 37.6 37.6 0.0 0.0 0.6 150 0.001 FTG TL E 44.00 PE PV 0.0 Pipe: 11 3.8 1.598 PL 40.00 PF 0.0 I 1D 10.0 0.0 37.6 0.0 0.6 150 FTG B PE 0.0 1E 10.0 0.0 37.6 0.0 0.001 TL 48.00 PV hA 26.9 1.598 PL 23.00 PF 0.7 I Pipe: 1A2 10.0 0.0 38.3 0.0 4.3 150 FTG 2B PE 0.0 1E 10.0 0.0 37.6 0.0 0.019 TL 39.00 PV I Pipe: 12 25.1 2.003 -PL 10.00 PF 0.1 • 1C 10.0 0.0 37.5 0.0 2.6 150 FTG E PE -4.3 2A 20.0 0.0 33.1 0.0 0.006 TL 19.00 PV I Pipe: 13 25.1 2.003 PL 8.00 PF 0.1 2A 20.0 0.0 33.1 0.0 2.6 150 FTG E PE 0.0 I 2B 20.0 0.0 33.0 0.0 0.006 TL 17.00 PV Pipe: 14 48.5 1.598 PL 31.00 PF 2.2 2B 20.0 0.0 33.0 0.0 7.8 150 FTG E PE 0.0 2F 20.0 0.0 30.8 0.0 0.057 TL 38.00 PV Pipe: 15 -23.5 1.598 PL 35.00 PF 0.8 20.0 0.0 33.0 0.0 3.8 150 FTG 2B PE 0.0 I 2B 2B1 20.0 0.0 33.7 0.0 0.015 TL 51.00 PV Pipe: iSA 26.4 1.598 PL 35.00 PF 1.1 I 2B1 20.0 0.0 33.7 0.0 4.2 150 FTG 2EB PE 0.0 2C 20.0 0.0 32.7 0.0 0.018 TL 57.00 PV • Pipe: 16 10.3 1.598 PL 7.00 PF 0.0 2C 20.0 0.0 32.7 0.0 1.6 150 FTG B PE 0.0 2D 20.0 0.0 32.6 0.0 0.003 TL 15.00 PV I Pipe: 17 30.7 2.003 PL 25.00 PF 0.6 • hE 10.0 0.0 37.6 0.0 3.1 150 FTG 2E3B PE -4.3 2D 20.0 0.0 32.6 0.0 0.008 TL 73.00 PV Pipe: 18 41.1 1.598 PL 34.00 PF 1.8 2D 20.0 0.0 32.6 0.0 6.6 150 FTG B PE 0.0 I 2E 20.0 0.0 30.9 0.0 0.042 TL 42.00 PV Pipe: 19 14.0 1.598 PL 4.00 PF 0.1 2E 20.0 0.0 30.9 0.0 2.2 150 FTG B PE 0.0 I 2F 20.0 0.0 30.8 0.0 0.006 TL 12.00 PV Pipe: 20 27.1 1.101 PL 1.00 PF 0.7 20.0 0.0 30.9 0.0 9.1 150 FTG B PE 0.4 I 2E 201 19.0 4.9 30.6 27.1 0.119 TL 6.00 PV I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B8 SENJU 4HD.SDF JOB TITLE: D5379 OCEAN STREET BLDG 8 I . PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 21 62.5 1.598 PL 7.00 PF 0.6 I 2F 2G 20.0 20.0 0.0 0.0 30.8 30.2 0.0 0.0 10.0 150 0.091 FTG TL ---- 7.00 PE PV 0.0 Pipe: 22 10.7 1.598 PL 4.00 PF 0.0 I 2G 20.0 0.0 30.2 0.0 1.7 150 FTG B PE 0.0 2H 20.0 0.0 30.1 0.0 0.003 TL 12.00 PV Pipe: 23 26.8 1.101 PL 1.00 PF 0.7 2H 20.0 0.0 30.1 0.0 9.0 150 FTG B PE 0.4 202 19.0 4.9 29.8 26.8 0.117 TL 6.00 PV I Pipe: 24 51.8 1.394 PL 11.00 PF 1.4 • 2G 20.0 0.0 30.2 0.0 10.9 150 FTG ---- PE 0.0 21 20.0 0.0 28.8 0.0 0.125 TL 11.00 PV I Pipe: 25 26.2 1.101 PL 1.00 PF 0.7 21 20.0 0.0 28.8 0.0 8.8 150 FTG B PE 0.4 I 203 19.0 4.9 28.5 26.2 0.112 TL 6.00 PV Pipe: 26 25.6 1.394 PL 9.00 PF 0.3 21 20.0 0.0 28.8 0.0 5.4 150 FTG ---- PE 0.0 21 20.0 0.0 28.5 0.0 0.034 TL 9.00 PV Pipe: 28 25.6 1.101 PL 5.00 PF 1.6 20.0 0.0 28.5 0.0 8.6 150 FTG 2B PE 0.4 I 2J 204 19.0 4.9 27.3 25.6 0.107 TL 15.00 PV Pipe: 29 -16.1 1.394 PL 24.00 PF 0.6 l 2H 20.0 0.0 30.1 0.0 3.4 150 FTG 3E PE -1.7 3A 24.0 0.0 29.0. 0.0 0.014 TL 42.00 PV • Pipe: 30 -16.1 1.394 PL 1.00 PF 0.1 3A 24.0 0.0 29.0 0.0 3.4 150 FTG E PE 0.0 301 24.0 0.0 29.1 0.0 0.014 TL 7.00 PV I Pipe: 31 -16.1 1.394 PL 5.00 PF 0.2 301 24.0 0.0 29.1 0.0 3.4 150 FTG B PE 0.0 302 24.0 0.0 29.2 0.0 0.014 TL 11.00 PV I Pipe: 32 -16.1 1.394 PL 6.00 PF 0.2 302 24.0 0.0 29.2 0.0 3.4 150 FTG B PE 0.0 I 303 24.0 0.0 29.4 0.0 0.014 TL 12.00 PV Pipe: 33 -16.1 1.394 PL 6.00 PF 0.2 303 24.0 0.0 29.4 0.0 3.4 150 FTG B PE 0.0 I 304 24.0 0.0 29.6 0.0 0.014 TL 12.00 PV Pipe: 34 -16.1 1.394 PL 6.00 PF 0.2 24.0 0.0 29.6 0.0 3.4 150 FTG B PE 0.0 I 304 305 24.0 0.0 29.8 0.0 0.014 TL 12.00 PV I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B8 SENJU 4HD.SDF I I JOB TITLE: D5379 OCEAN STREET BLDG 8 PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 35 -16.1 1.394 PL 43.00 PF 0.7 I 305 24.0 0.0 29.8 0.0 3.4 150 FTG B PE 0.0 3B 24.0 0.0 30.5 0.0 0.014 TL 49.00 PV Pipe: 36 -16.1 1.394 PL 15.00 PF 0.5 l 3B 24.0 0.0 30.5 0.0 3.4 150 FTG 2EB PE 1.7 2C 20.0 0.0 32.7 0.0 0.014 TL 33.00 PV Pipe: 37 0.0 1.101 PL 8.00 PF 0.0 2J 20.0 0.0 28.5 0.0 0.0 150 FTG EB PE -1.7 307 24.0 0.0 26.7 0.0 0.000 TL 20.00 PV I Pipe: 38 0.0 1.101 PL 8.00 PF 0.0 2J 20.0 0.0 28.5 0.0 0.0 150 FTG EB PE -1.7 306 24.0 0.0 26.7 0.0 0.000 TL 20.00 PV I NOTES (HASS) I (1) Calculations were performed by the HASS 8.4 computer program under license no. 16080621 granted by HRS Systems, Inc. I 208 Southside Square Petersburg, TN 37144 (931) 659-9760 I (2) The system has been calculated to provide an average imbalance at each node of 0.001 gpm and a maximum ' imbalance at any node of 0.050 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 10.9 ft/sec at pipe 24. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. Available pressure at source node SR2 under full flow conditions is 82.88 psi compared to the minimum required pressure of 20.00 psi. I (6) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP I I I 1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B8 SENJU 4HD.SDF TITLE: D5379 OCEAN STREET BLDG 8 I JOB PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N I Eli Tee LngEii ChkVlv BfyVlv GatVlv AlmChk DPVlv NPTee 2.067 5.00 10.00 3.00 11.00 6.00 1.00 10.00 10.00 10.00 PAGE: F MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) L E B R C S G I 45 El BrT RunT Cplg SwCk Gate 1.101 1.00 7.00 5.00 1.00 1.00 8.00 2.00 1.394 2.00 6.00 6.00 1.00 1.00 11.00 3.00 ' 1.598 2.00 7.00 8.00 1.00 1.00 14.00 3.00 2.003 2.00 9.00 10.00 1.00 1.00 17.00 3.00 PAGE: H MATERIAL: PVC 200CLASS HWC: 150 I Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Eli Tee Long Check Butter Gate NPTee 4.070 17.00 34.00 10.00 37.00 20.00 3.00 34.00 I I I I I I I I I I I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B8 SENJU 4HD.SDF JOB TITLE: D5379 OCEAN STREET BLDG 8 I E Wa) UI a) (Jo I . (flLfl r1 ri (O (Or LC) a) (q E0 c'E a) W )-H •-1W I a)J) H 1U) (Ii -m •HDO>i C! H0 J(T ni- b1 - m I1)c' -•- I 04 04 I N CN rj -H U) I --1 U) o CJ)N I H. - >1 co (14 4J aj c/) I (I) Ill I I I I I N I 0 0 0 0 0 0 0 0 0 0 0 C) 00 (N U)- H - — I 0 0 0 H SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 I DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B8 SENJU 4HD.SDF JOB TITLE: D5379 OCEAN STREET BLDG 8 WATER SUPPLY CURVE I 84*\\\\\\\\ I 0 \\\\\\\\ I \\\\\\\\ I I \\\\\\\\ 77+ \\\\\\\\ I \\\\\\\\ I 74.2 psi @ 859 gpm-> * I Flow Test Point 70+ 63+ x P 56+ RI El SI S 49+ UI RI El 42+ P I 35+ 28+ 21+ 14+ LEGEND II I X = Required Water Supply I 62.46 psi @ 205.7 gpm 7+ I 0 = Available Water Supply I 83.03 psi @ 205.7 gpm 0++-+---+----+-----+ ------+ --------+ --------+ ---------+ ------------ 200 300 400 500 600 700 800 900 1000 FLOW (GPM) I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B10 ATTIC 7HD.SDF TITLE: D5379 OCEAN STREET BLDG 9-12 I JOB WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQtD I NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SR2 83.7 74.2 859.0 82.6 263.2 73.1 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 263.2 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 163.2 GPM NODE ANALYSIS DATA I NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) SR2 0.0 SOURCE 73.1 163.2 I R2 2.5 - - - - 71.6 - - - P2 2.5 - - - - 60.6 - - - UG2 0.0 - - - - 61.1 - - - 1.5 - - - - 58.7 - - - I B10 BOR 2.5 - - - - 54.2 - - - TOR 6.5 - - - - 47.6 I 1A lB 10.0 10.0 - - - - 37.3 - - - - - - - 36.9 - - - 1C 10.0 - - - - 35.2 - - - 1D 10.0 - - - - 35.1 - - - I 2A 20.0 - - - - 27.6 - - - 2B 20.0 - - - - 26.4 - - - 2C 20.0 - - - - 27.5 - - - 20.0 - - - - 27.7 - - - I 2C1 2D 20.0 - - - - 27.3 - - - 2E 20.0 - - - - 26.3 - - - 20.0 - - - - 26.3 - - - I 2E1 2F 20.0 - - - - 25.7 - - - 2G 20.0 - - - - 24.9 - - - 2H 20.0 - - - - 23.3 - - - 20.0 - - - - 22.5 - - - I 21 2J 20.0 - - - - 22.8 - - - 2K 20.0 - - - - 22.2 - - - I 2L 2M 20.0 20.0 - - - - 22.0 - - - - - - - 22.0 - - - 201 19.0 - - - - 23.3 - - - 202 19.0 - - - - 22.6 - - - 19.0 - - - - 22.5 - - - I 203 204 19.0 - - - - 22.5 - - - 3A 24.0 - - - - 24.3 - - - 24.0 - - - - 25.0 - - - I 3B 3C 24.0 - - - - 24.0 - - - 3D 24.0 - - - - 20.4 - - - I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 6/4/2014 C:\HA5583\D5379 OCEAN ST DA B10 ATTIC 7HD.SDF I- JOB TITLE: D5379 OCEAN STREET BLDG 9-12 NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE I (FT) (PSI) 3E 24.0 - - - - 21.3 - - - 24.0 - - - - 23.1 - - - I 3F 301 24.0 K= 5.60 20.0 25.1 302 24.0 K= 5.60 19.9 25.0 303 24.0 K= 5.60 20.0 25.0 304 24.0 K= 5.60 20.4 25.3 305 24.0 K= 5.60 21.4 25.9 306 24.0 K= 4.20 19.1 18.4 307 24.0 K= 4.20 19.5 18.6 L I I I I I I I I I I I I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B10 ATTIC 7HD.SDF TITLE: D5379 OCEAN STREET BLDG 9-12 I JOB PIPE DATA I PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 1 163.2 4.070 PL 17.00 PF 0.4 - SR2 0.0 SRCE 73.1 (N/A) 4.0 150 FTG ETG PE -1.1 R2 2.5 0.0 71.6 0.0 0.006 TL 71.00 PV I Pipe: 2 FIXED PRESSURE LOSS DEVICE R2 2.5 0.0 71.6 0.0 11.0 psi, 163.2 gprn I P2 2.5 0.0 60.6 0.0 Pipe: 3 163.2 4.070 PL 29.00 PF 0.6 P2 2.5 0.0 60.6 0.0 4.0 150 FTG 2ETL PE 1.1 UG2 0.0 0.0 61.1 0.0 0.006 TL 107.00 PV Pipe: 4 163.2 4.070 PL 200.00 PF 1.7 0.0 0.0 61.1 0.0 4.0 150 FTG 3ET2L PE -0.6 I tJG2 B10 1.5 0.0 58.7 0.0 0.006 TL 305.00 PV - Pipe: 5 163.2 2.003 PL 3.00 PF 4.0 I B10 1.5 0.0 58.7 0.0 16.6 120 FTG 2E PE -0.4 BOR 2.5 0.0 54.2 0.0 0.271 TL 14.91 PV I Pipe: 6 163.2 2.067 PL 4.00 PF 4.9 I BOR 2.5 0.0 54.2 0.0 15.6 120 FTG CB PE -1.7 TOR 6.5 0.0 47.6 0.0 0.232 TL 21.00 PV Pipe: 7 163.2 2.003 PL 22.00 PF 8.8 TOR 6.5 0.0 47.6 0.0 16.6 150 FTG 3E PE -1.5 1A 10.0 0.0 37.3 0.0 0.179 TL 49.00 PV I Pipe: 8 50.7 1.598 PL 7.00 PF 0.4 1A 10.0 0.0 37.3 0.0 8.1 150 FTG ---- PE 0.0 I lB 10.0 0.0 36.9 0.0 0.062 TL 7.00 PV Pipe: 9 50.7 1.598 PL 24.00 PF 4.8 lB 10.0 0.0 36.9 0.0 8.1 150 FTG 2E5B PE -4.3 2C1 20.0 0.0 27.7 0.0 0.062 TL 78.00 PV Pipe: 10 63.4 1.598 PL 14.00 PF 2.1 10.0 0.0 37.3 0.0 10.1 150 FTG B PE 0.0 I 1A 1C 10.0 0.0 35.2 0.0 0.094 TL 22.00 PV • Pipe: 11 49.1 1.598 PL 30.00 PF 2.2 U 1A 10.0 0.0 37.3 0.0 7.8 150 FTG B PE 0.0 1D 10.0 0.0 35.1 0.0 0.058 TL 38.00 PV I Pipe: 12 63.4 1.598 PL 13.00 PF 3.3 • 1C 10.0 0.0 35.2 0.0 10.1 150 FTG 2EB PE -4.3 2A 20.0 0.0 27.6 0.0 0.094 TL 35.00 PV I I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B10 ATTIC 7HD.SDF I. JOB TITLE: D5379 OCEAN STREET BLDG 9-12 PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 13 49.1 1.598 PL 30.00 PF 4.4 10.0 0.0 35.1 0.0 7.8 150 FTG 2E4B PE -4.3 I 1D 2E1 20.0 0.0 26.3 0.0 0.058 TL 76.00 PV Pipe: 14 48.4 1.598 PL 13.00 PF 1.2 I 2A 20.0 0.0 27.6 0.0 7.7 150 FTG B PE 0.0 2B 20.0 0.0 26.4 0.0 0.057 TL 21.00 PV I Pipe: 15 30.0 1.598 PL 42.00 PF 1.5 2B 20.0 0.0 26.4 0.0 4.8 150 FTG E2B PE 0.0 2G 20.0 0.0 24.9 0.0 0.023 TL 65.00 PV I Pipe: 16 15.0 1.598 PL 14.00 PF 0.1 • 2A 20.0 0.0 27.6 0.0 2.4 150 FTG ---- PE 0.0 2C 20.0 0.0 27.5 0.0 0.007 TL 14.00 PV Pipe: 17 -21.1 1.598 PL 6.00 PF 0.2 2C 20.0 0.0 27.5 0.0 3.4 150 FTG B PE 0.0 I 2C1 20.0 0.0 27.7 0.0 0.012 TL 14.00 PV Pipe: 18 29.6 1.598 PL 18.00 PF 0.4 2C1 20.0 0.0 27.7 0.0 4.7 150 FTG ---- PE 0.0 2D 20.0 0.0 27.3 0.0 0.023 TL 18.00 PV Pipe: 19 36.2 1.598 PL 30.00 PF 1.3 20.0 0.0 27.5 0.0 5.8 150 FTG B PE 0.0 I 2C 2E 20.0 0.0 26.3 0.0 0.033 TL 38.00 PV Pipe: 20 -11.2 1.598 PL 6.00 PF 0.1 I 2E 20.0 0.0 26.3 0.0 1.8 150 FTG B PE 0.0 2E1 20.0 0.0 26.3 0.0 0.004 TL 14.00 PV • Pipe: 21 37.8 1.598 PL 17.00 PF 0.6 • 2E1 20.0 0.0 26.3 0.0 6.0 150 FTG ---- PE 0.0 2F 20.0 0.0 25.7 0.0 0.036 TL 17.00 PV Pipe: 22 47.4 1.598 PL 17.00 PF 1.4 • 2E 20.0 0.0 26.3 0.0 7.6 150 FTG B PE 0.0 2G 20.0 0.0 24.9 0.0 0.055 TL 25.00 PV Pipe: 23 77.4 1.598 PL 12.00 PF 1.6 2G 20.0 0.0 24.9 0.0 12.4 150 FTG ---- PE 0.0 I 2H 20.0 0.0 23.3 0.0 0.135 TL 12.00 PV Pipe: 24 40.4 1.598 PL 11.00 PF 0.7 2H 20.0 0.0 23.3 0.0 6.5 150 FTG E PE 0.0 21 20.0 0.0 22.5 0.0 0.041 TL 18.00 PV Pipe: 25 36.9 1.598 PL 5.00 PF 0.4 20.0 0.0 23.3 0.0 5.9 150 FTG B PE 0.0 I 2H 21 20.0 0.0 22.8 0.0 0.034 TL 13.00 PV I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B10 ATTIC 7HD.SDF I JOB TITLE: D5379 OCEAN STREET BLDG 9-12 PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 26 0.0 1.101 PL 1.00 PF 0.0 20.0 0.0 22.8 0.0 0.0 150 FTG B PE 0.4 I 2J 201 19.0 0.0 23.3 0.0 0.000 TL 6.00 PV Pipe: 27 36.9 1.598 PL 5.00 PF 0.7 I 21 20.0 0.0 22.8 0.0 5.9 150 FTG 2E PE 0.0 2K 20.0 0.0 22.2 0.0 0.034 TL 19.00 PV I Pipe: 28 0.0 1.101 PL 3.00 PF 0.0 2K 20.0 0.0 22.2 0.0 0.0 150 FTG EB PE 0.4 202 19.0 0.0 22.6 0.0 0.000 TL 15.00 PV I Pipe: 29 36.9 1.598 PL 4.00 PF 0.1 • 2K 20.0 0.0 22.2 0.0 5.9 150 FTG ---- PE 0.0 2L 20.0 0.0 22.0 0.0 0.034 TL 4.00 PV Pipe: 30 0.0 1.101 PL 3.00 PF 0.0 2L 20.0 0.0 22.0 0.0 0.0 150 FTG EB PE 0.4 I 203 19.0 0.0 22.5 0.0 0.000 TL 15.00 PV Pipe: 31 0.0 1.101 PL 3.00 PF 0.0 2L 20.0 0.0 22.0 0.0 0.0 150 FTG EB PE 0.4 204 19.0 0.0 22.5 0.0 0.000 TL 15.00 PV Pipe: 32 36.9 1.598 PL 2.00 PF 0.1 20.0 0.0 22.0 0.0 5.9 150 FTG ---- PE 0.0 U 2L 2M 20.0 0.0 22.0 0.0 0.034 TL 2.00 PV Pipe: 33 18.4 1.101 PL 7.00 PF 1.1 I 2M 20.0 0.0 22.0 0.0 6.2 150 FTG EB PE -1.7 306 24.0 4.2 19.1 18.4 0.058 TL 19.00 PV • Pipe: 34 18.6 1.101 PL 5.00 PF 0.7 • 2M 20.0 0.0 22.0 0.0 6.3 150 FTG E PE -1.7 307 24.0 4.2 19.5 18.6 0.059 TL 12.00 PV I Pipe: 35 18.4 1.598 PL 18.00 PF 0.4 • 2B 20.0 0.0 26.4 0.0 2.9 150 FTG E2B PE -1.7 3A 24.0 0.0 24.3 0.0 0.010 TL 41.00 PV Pipe: 36 29.6 1.598 PL 9.00 PF 0.5 2D 20.0 0.0 27.3 0.0 4.7 150 FTG EB PE -1.7 I 3B 24.0 0.0 25.0 0.0 0.023 TL 24.00 PV Pipe: 37 37.8 1.598 PL 9.00 PF 0.9 2F 20.0 0.0 25.7 0.0 6.0 150 FTG EB PE -1.7 3F 24.0 0.0 23.1 0.0 0.036 TL 24.00 PV Pipe: 38 40.4 1.598 PL 4.00 PF 0.4 20.0 0.0 22.5 0.0 6.5 150 FTG E PE -1.7 I 21 3D 24.0 0.0 20.4 0.0 0.041 TL 11.00 PV I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B10 ATTIC 7HD.SDF I JOB TITLE: D5379 OCEAN STREET BLDG 9-12 PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 39 18.4 1.598 PL 22.00 PF 0.3 I 3A 24.0 0.0 24.3 0.0 2.9 150 FTG E PE 0.0 3C 24.0 0.0 24.0 0.0 0.010 TL 29.00 PV Pipe: 40 29.6 1.598 PL 36.00 PF 1.0 I 3B 24.0 0.0 25.0 0.0 4.7 150 FTG E PE 0.0 3C 24.0 0.0 24.0 0.0 0.023 TL 43.00 PV Pipe: 41 48.0 1.598 PL 40.00 PF 2.7 3C 24.0 0.0 24.0 0.0 7.7 150 FTG B PE 0.0 3E 24.0 0.0 21.3 0.0 0.056 TL 48.00 PV I Pipe: 42 40.4 1.598 PL 1.00 PF 0.3 3D 24.0 0.0 20.4 0.0 6.5 150 FTG E PE 0.0 301 24.0 5.6 20.0 25.1 0.041 TL 8.00 PV Pipe: 43 15.4 1.598 PL 6.00 PF 0.1 301 24.0 5.6 20.0 25.1 2.5 150 FTG B PE 0.0 I 302 24.0 5.6 19.9 25.0 0.007 TL 14.00 PV Pipe: 44 -9.6 1.598 PL 6.00 PF 0.0 302 24.0 5.6 19.9 25.0 1.5 150 FTG B PE 0.0 303 24.0 5.6 20.0 25.0 0.003 TL 14.00 PV Pipe: 45 -34.6 1.598 PL 6.00 PF 0.4 I 303 24.0 5.6 20.0 25.0 5.5 150 FTG B PE 0.0 304 24.0 5.6 20.4 25.3 0.031 TL 14.00 PV Pipe: 46 -59.9 1.598 PL 3.00 PF 0.9 I 304 24.0 5.6 20.4 25.3 9.6 150 FTG B PE 0.0 3E 24.0 0.0 21.3 0.0 0.084 TL 11.00 PV Pipe: 47 -11.9 1.598 PL 3.00 PF 0.0 3E 24.0 0.0 21.3 0.0 1.9 150 FTG B PE 0.0 305 24.0 5.6 21.4 25.9 0.004 TL 11.00 PV Pipe: 48 -37.8 1.598 PL 33.00 PF 1.7 305 24.0 5.6 21.4 25.9 6.0 150 FTG EB FE 0.0 3F 24.0 0.0 23.1 0.0 0.036 TL 48.00 PV I NOTES (HASS) I (1) Calculations were performed by the HASS 8.4 computer program under license no. 16080621 granted by HRS Systems, Inc. I 208 Southside Square Petersburg, TN 37144 (931) 659-9760 I I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B10 ATTIC 7HD.SDF JOB TITLE: D5379 OCEAN STREET BLDG 9-12 (2) The system has been calculated to provide an average I imbalance at each node of 0.002 gpm and a maximum imbalance at any node of 0.065 gpm. I (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 16.6 ft/sec at pipe 5. I (4) Items listed in bold print on the cover sheet are automatically transferred from the calculation report. 1 Available pressure at source node SR2 under full flow conditions is 82.52 psi compared to the minimum required pressure of 20.00 psi. (6) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPVlv NPTee 2.067 5.00 10.00 3.00 11.00 6.00 1.00 10.00 10.00 10.00 PAGE: F MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) L E B R C S G 45 El BrT RunT Cplg SwCk Gate 1.101 1.00 7.00 5.00 1.00 1.00 8.00 2.00 1.598 2.00 7.00 8.00 1.00 1.00 14.00 3.00 2.003 2.00 9.00 10.00 1.00 1.00 17.00 3.00 PAGE: H MATERIAL: PVC 200CLASS HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Ell Tee Long Check Butter Gate NPTee 4.070 17.00 34.00 10.00 37.00 20.00 3.00 34.00 H I I I I I I I I I - - - - - _ - - - - - - - - - - qtj o WATER SUPPLY ANALYSIS 12 100 0 Static: 83.70 psi Resid: 74.20 psi Flow: 859.0 gpm 80.0 A U G E P 60.0 R E S S U R 40.0 E p 5 i 20.0 0.0 -14.'? 200 300 400 500 600 700 800 900 1000 FLOW (GPM) (Note: Dashed Lines indicate extrapolated values from Test Results) I . SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 I DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B10 ATTIC 7HD.SDF . JOB TITLE: D5379 OCEAN STREET BLDG 9-12 WATER SUPPLY CURVE I 84*\\\\\\\\ I 0 \\\\\\\\ \\\\\\\\ I I \\\\\\\\ 77+ \\\\\\\\ I \\\\\\\\ 74.2 psi @ 859 gpm-> * I I Flow Test Point 70+ 63+ P 56+ RI El SI S 49+ UI RI El 42+ 28+ 21+ 14+ LEGEND I X = Required Water Supply I 73.07 psi @ 263.2 gpm 7+ II I 0 = Available Water Supply I 8+2 .64 psi @ 263 .2 gpm + ------+ --------+ --------+ ---------+ -----------+ 200 300 400 500 . 600 700 800 900 1000 FLOW (GPM) I I I I I I I I I I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B10 SENJU 4HD.SDF JOB TITLE: D5379 OCEAN STREET BLDG 9-12 I. WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D I NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SR2 83.7 74.2 859.0 83.0 204.2 68.6 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 204.2 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 104.2 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE I (FT) (PSI) (GPM) SR2 R2 0.0 2.5 SOURCE - - - - 68.6 67.3 104.2 - - - P2 2.5 - - - - 56.3 - - - UG2 0.0 - - - - 57.2 - - - 1.5 - - - - 55.8 - - - I B10 BOR 2.5 - - - - 53.6 - - - TOR 6.5 - - - - 49.7 - - - 10.0 - - - - 44.4 - - - I 1A lB 10.0 - - - - 44.2 - - - 1C 10.0 - - - - 43.4 - - - 1D 10.0 - - - - 43.4 - - - I 2A 20.0 - - - - 37.7 - - - 2B 20.0 - - - - 37.1 - - - 2C 20.0 - - - - 37.6 - - - 20.0 - - - - 37.7 - - - I 2C1 2D 20.0 - - - - 37.6 - - - 2E 20.0 - - - - 37.0 - - - 20.0 - - - - 37.1 - - - I 2E1 2F 20.0 - - - - 37.0 - - - 2G 20.0 - - - - 35.8 - - - 2H 20.0 - - - - 34.3 - - - 20.0 - - - - 34.8 - - - I 21 2J 20.0 - - - - 31.3 - - - 2K 20.0 - - - - 28.7 - - - I 2L 2M 20.0 20.0 - - - - - - - - 28.5 28.5 - - - - - - 201 19.0 K= 4.90 31.0 27.3 202 19.0 K= 4.90 27.5 25.7 I 203 19.0 K= 4.90 27.3 25.6 204 19.0 K= 4.90 27.3 25.6 3A 24.0 - - - - 35.4 - - - 24.0 - - - - 35.7 - - - I 3B 3C 24.0 - - - - 35.4 - - - 3D 24.0 - - - - 33.3 - - - I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B10 SENJU 4HD.SDF I JOB TITLE: D5379 OCEAN STREET BLDG 9-12 NODE ANALYSIS DATA - NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE I (FT) (PSI) (GPM) 3E 24.0 - - - - 34.9 - - - I 3F 301 24.0 - 24.0 - - - - 35.2 - - - - - 33.5 - - - 302 24.0 - - - - 33.9 - - - 303 24.0 - - - - 34.3 - - - '304 24.0 - - - - 34.6 - - - 305 24.0 - - - - 35.0 - - - 306 24.0 - - - - 26.7 - - - 307 24.0 - - - - 26.7 - - - I I I I I I 1 1 1 I 1 I I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B10 SENJU 4HD.SDF - JOB TITLE: D5379 OCEAN STREET BLDG 9-12 I PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. I END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) I Pipe: 1 104.2 4.070 PL 17.00 PF 0.2 - SR2 0.0 SRCE 68.6 (N/A) 2.6 150 FTG ETG PE -1.1 R2 2.5 0.0 67.3 0.0 0.002 TL 71.00 PV I Pipe: 2 FIXED PRESSURE LOSS DEVICE R2 2.5 0.0 67.3 0.0 11.0 psi, 104.2 gpm I P2 2.5 0.0 56.3 0.0 Pipe: 3 104.2 4.070 PL 29.00 PF 0.3 P2 2.5 0.0 56.3 0.0 2.6 150 FTG 2ETL PE 1.1 UG2 0.0 o:o 57.2 0.0 0.002 TL 107.00 PV Pipe: 4 104.2 4.070 PL 200.00 PF 0.8 0.0 0.0 57.2 0.0 2.6 150 FTG 3ET2L PE -0.6 I UG2 B10 1.5 0.0 55.8 0.0 0.002 TL 305.00 PV Pipe: 5 104.2 2.003 PL 3.00 PF 1.8 I B10 1.5 0.0 55.8 0.0 10.6 120 FTG 2E PE -0.4 BOR 2.5 0.0 53.6 0.0 0.118 TL 14.91 PV • Pipe: 6 104.2 2.067 PL 4.00 PF 2.1 I BOR 2.5 0.0 53.6 0.0 10.0 120 FTG CB PE -1.7 TOR 6.5 0.0 49.7 0.0 0.101 TL 21.00 PV I Pipe: 7 104.2 2.003 PL 22.00 PF 3.8 - TOR 6.5 0.0 49.7 0.0 10.6 150 FTG 3E PE -1.5 1A 10.0 0.0 44.4 0.0 0.078 TL 49.00 PV I Pipe: 8 32.2 1.598 PL 7.00 PF 0.2 1A 10.0 0.0 44.4 0.0 5.2 150 FTG ---- PE 0.0 ' lB 10.0 0.0 44.2 0.0 0.027 TL 7.00 PV Pipe: 9 32.2 1.598 PL 24.00 PF 2.1 lB 10.0 0.0 44.2 0.0 5.2 150 FTG 2E5B PE -4.3 2C1 20.0 0.0 37.7 0.0 0.027 TL 78.00 PV Pipe: 10 40.6 1.598 PL 14.00 PF 0.9 10.0 0.0 44.4 0.0 6.5 150 FTG B PE 0.0 I 1A 1C 10.0 0.0 43.4 0.0 0.041 TL 22.00 PV • Pipe: 11 31.4 1.598 PL 30.00 PF 1.0 ' 1A 10.0 0.0 44.4 0.0 5.0 150 FTG B PE 0.0 1D 10.0 0.0 43.4 0.0 0.025 TL 38.00 PV I Pipe: 12 40.6 1.598 PL 13.00 PF 1.4 I 1C 10.0 0.0 43.4 0.0 6.5 150 FTG 2EB PE -4.3 2A 20.0 0.0 37.7 0.0 0.041 TL 35.00 PV I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B10 SENJU 4HD.SDF - JOB TITLE: D5379 OCEAN STREET BLDG 9-12 I PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 13 31.4 1.598 PL 30.00 PF 1.9 10.0 0.0 43.4 0.0 5.0 150 FTG 2E4B PE -4.3 I 1D 2E1 20.0 0.0 37.1 0.0 0.025 TL 76.00 PV Pipe: 14 31.3 1.598 PL 13.00 PF 0.5 I 2A 20.0 0.0 37.7 0.0 5.0 150 FTG B PE 0.0 2B 20.0 0.0 37.1 0.0 0.025 TL 21.00 PV Pipe: 15 28.3 1.598 PL 42.00 PF 1.4 2B 20.0 0.0 37.1 0.0 4.5 150 FTG E2B PE 0.0 2G 20.0 0.0 35.8 0.0 0.021 TL 65.00 PV I Pipe: 16 9.3 1.598 PL 14.00 PF 0.0 • 2A 20.0 0.0 37.7 0.0 1.5 150 FTG ---- PE 0.0 2C 20.0 0.0 37.6 0.0 0.003 TL 14.00 PV I Pipe: 17 -16.2 1.598 PL 6.00 PF 0.1 2C 20.0 0.0 37.6 0.0 2.6 150 FTG B PE 0.0 I 2C1 20.0 0.0 37.7 0.0 0.008 TL 14.00 PV Pipe: 18 16.0 1.598 PL 18.00 PF 0.1 2C1 20.0 0.0 37.7 0.0 2.6 150 FTG ---- PE 0.0 I 2D 20.0 0.0 37.6 0.0 0.007 TL 18.00 PV Pipe: 19 25.5 1.598 PL 30.00 PF 0.7 20.0 0.0 37.6 0.0 4.1 150 FTG B PE 0.0 I 2C 2E 20.0 0.0 37.0 0.0 0.017 TL 38.00 PV Pipe: 20 -18.7 1.598 PL 6.00 PF 0.1 I 2E 20.0 0.0 37.0 0.0 3.0 150 FTG B PE 0.0 2E1 20.0 0.0 37.1 0.0 0.010 TL 14.00 PV Pipe: 21 12.6 1.598 PL 17.00 PF 0.1 2E1 20.0 0.0 37.1 0.0 2.0 150 FTG ---- PE 0.0 2F 20.0 0.0 37.0 0.0 0.005 TL 17.00 PV I Pipe: 22 44.3 1.598 PL 17.00 PF 1.2 - 2E 20.0 0.0 37.0 0.0 7.1 150 FTG B PE 0.0 2G 20.0 0.0 35.8 0.0 0.048 TL 25.00 PV Pipe: 23 72.6 1.598 PL 12.00 PF 1.4 2G 20.0 0.0 35.8 0.0 11.6 150 FTG ---- PE 0.0 l 2H 20.0 0.0 34.3 0.0 0.121 TL 12.00 PV Pipe: 24 -31.5 1.598 PL 11.00 PF 0.5 2H 20.0 0.0 34.3 0.0 5.0 150 FTG E PE 0.0 21 20.0 0.0 34.8 0.0 0.026 TL 18.00 PV Pipe: 25 104.2 1.598 PL 5.00 PF 3.1 20.0 0.0 34.3 0.0 16.7 150 FTG B PE 0.0 I I 2H 21 20.0 0.0 31.3 0.0 0.235 TL 13.00 PV I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B10 SENJU 4HD.SDF - JOB TITLE: D5379 OCEAN STREET BLDG 9-12 I PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. - END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 26 27.3 1.101 PL 1.00 PF 0.7 20.0 0.0 31.3 0.0 9.2 150 FTG B PE 0.4 I 2J. 201 19.0 4.9 31.0 27.3 0.121 TL 6.00 PV Pipe: 27 76.9 1.598 PL 5.00 PF 2.5 I 2J 20.0 0.0 31.3 0.0 12.3 150 FTG 2E PE 0.0 2K 20.0 0.0 28.7 0.0 0.134 TL 19.00 PV • Pipe: 28 25.7 1.101 PL 3.00 PF 1.6 2K 20.0 0.0 28.7 0.0 8.7 150 FTG EB PE 0.4 202 19.0 4.9 27.5 25.7 0.108 TL 15.00 PV Pipe: 29 51.2 1.598 PL 4.00 PF 0.3 • 2K 20.0 0.0 28.7 0.0 8.2 150 FTG ---- PE 0.0 2L 20.0 0.0 28.5 0.0 0.063 TL 4.00 PV Pipe: 30 25.6 1.101 PL 3.00 PF 1.6 2L 20.0 0.0 28.5 0.0 8.6 150 FTG EB PE 0.4 I 203 19.0 4.9 27.3 25.6 0.107 TL 15.00 PV Pipe: 31 25.6 1.101 PL 3.00 PF 1.6 2L 20.0 0.0 28.5 0.0 8.6 150 FTG EB PE 0.4 204 19.0 4.9 27.3 25.6 0.107 TL 15.00 PV Pipe: 32 0.0 1.598 PL 2.00 PF 0.0 20.0 0.0 28.5 0.0 0.0 150 FTG ---- PE 0.0 I 2L 2M 20.0 0.0 28.5 0.0 0.000 TL 2.00 PV Pipe: 33 0.0 1.101 PL 7.00 PF 0.0 I 2M 20.0 0.0 28.5 0.0 0.0 150 FTG EB PE -1.7 306 24.0 0.0 26.7 0.0 0.000 TL 19.00 PV Pipe: 34 0.0 1.101 PL 5.00 PF 0.0 2M 20.0 0.0 28.5 0.0 0.0 150 FTG E PE -1.7 307 24.0 0.0 26.7 0.0 0.000 TL 12.00 PV I Pipe: 35 2.9 1.598 PL 18.00 PF 0.0 • 2B 20.0 0.0 37.1 0.0 0.5 150 FTG E2B PE -1.7 3A 24.0 0.0 35.4 0.0 0.000 TL 41.00 PV I Pipe: 36 16.0 1.598 PL 9.00 PF 0.2 2D 20.0 0.0 37.6 0.0 2.6 150 FTG EB PE -1.7 I 3B 24.0 0.0 35.7 0.0 0.007 TL 24.00 PV Pipe: 37 12.6 1.598 PL 9.00 PF 0.1 2F 20.0 0.0 37.0 0.0 2.0 150 FTG EB PE -1.7 3F 24.0 0.0 35.2 0.0 0.005 TL 24.00 PV Pipe: 38 -31.5 1.598 PL 4.00 PF 0.3 I 21 20.0 0.0 34.8 0.0 5.0 150 FTG E PE -1.7 3D 24.0 0.0 33.3 0.0 0.026 TL 11.00 PV I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B10 SENJU 4HD.SDF TITLE: D5379 OCEAN STREET BLDG 9-12 I JOB PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 39 2.9 1.598 PL 22.00 PF 0.0 I 3A 3C 24.0 24.0 0.0 0.0 35.4 35.4 0.0 0.0 0.5 150 0.000 FTG TL E 29.00 PE PV 0.0 Pipe: 40 16.0 1.598 PL 36.00 PF 0.3 I 3B 24.0 0.0 35.7 0.0 2.6 150 FTG E PE 0.0 3C 24.0 0.0 35.4 0.0 0.007 TL 43.00 PV • Pipe: 41 18.9 1.598 PL 40.00 PF 0.5 3C 24.0 0.0 35.4 0.0 3.0 150 FTG B PE 0.0 3E 24.0 0.0 34.9 0.0 0.010 TL 48.00 PV Pipe: 42 -31.5 1.598 PL 1.00 PF 0.2 • 3D 24.0 0.0 33.3 0.0 5.0 150 FTG E PE 0.0 301 24.0 0.0 33.5 0.0 0.026 TL 8.00 PV I Pipe: 43 -31.5 1.598 PL 6.00 PF 0.4 301 24.0 0.0 33.5 0.0 5.0 150 FTG B PE 0.0 I 302 24.0 0.0 33.9 0.0 0.026 TL 14.00 PV Pipe: 44 -31.5 1.598 PL 6.00 PF 0.4 302 24.0 0.0 33.9 0.0 5.0 150 FTG B PE 0.0 303 24.0 0.0 34.3 0.0 0.026 TL 14.00 PV Pipe: 45 -31.5 1.598 PL 6.00 PF 0.4 24.0 0.0 34.3 0.0 5.0 150 FTG B PE 0.0 I 303 304 24.0 0.0 34.6 0.0 0.026 TL 14.00 PV Pipe: 46 -31.5 1.598 PL 3.00 PF 0.3 I 304 24.0 0.0 34.6 0.0 5.0 150 FTG B PE 0.0 3E 24.0 0.0 34.9 0.0 0.026 TL 11.00 PV • Pipe: 47 -12.6 1.598 PL 3.00 PF 0.1 3E 24.0 0.0 34.9 0.0 2.0 150 FTG B PE 0.0 305 24.0 0.0 35.0 0.0 0.005 TL 11.00 PV Pipe: 48 -12.6 1.598 PL 33.00 PF 0.2 • 305 24.0 0.0 35.0 0.0 2.0 150 FTG EB PE 0.0 3F 24.0 0.0 35.2 0.0 0.005 TL 48.00 PV I NOTES (HASS) I (1) Calculations were performed by the HASS 8.4 computer program under license no. 16080621 granted by HRS Systems, Inc. I 208 Southside Square Petersburg, TN 37144 (931) 659-9760 I I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B10 SENJU 4HD.SDF - JOB TITLE: D5379 OCEAN STREET BLDG 9-12 - (2) The system has been calculated to provide an average I imbalance at each node of 0.002 gpm and a maximum imbalance at any node of 0.099 gpm. I Total pressure at each node is used in balancing the system. Maximum water velocity is 16.7 ft/sec at pipe 25. I (4) Items listed in bold print on the cover sheet are automatically transferred from the calculation report. I (5) Available pressure at source node 5R2 under full flow conditions is 82.94 psi compared to the minimum required pressure of 20.00 psi. (6) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPVlv NPTee 2.067 5.00 10.00 3.00 11.00 6.00 1.00 10.00 10.00 10.00 PAGE: F MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet L E B R C S G (in) 45 El BrT RunT Cplg SwCk Gate 1.101 1.00 7.00 5.00 1.00 1.00 8.00 2.00 1.598 2.00 7.00 8.00 1.00 1.00 14.00 3.00 2.003 2.00 9.00 10.00 1.00 1.00 17.00 3.00 PAGE: H MATERIAL: PVC 200CLASS HWC: 150 Equivalent Fitting Lengths in Feet Diameter (in) E T L C B G N Ell Tee Long Check Butter Gate NPTee 4.070 17.00 34.00 10.00 37.00 20.00 3.00 34.00 I I I I I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B10 SENJU 4HD.SDF JOB TITLE: D5379 OCEAN STREET BLDG 9-12 E tj) I a) 00 I C• N I I I I (O LO I I1)c'i )CI) I I P4 I I OJ.H HQ) H rd)UQ) I cj I Hm H00>i 0 -io DCJ)C!) W 00 I SI I I 0 - N I I H N I -H (ci — I ci) I I -H 04 (ci I I c H. (flr co I - 114 I I 4J I I C') I - I I I I I I N I I I N 0 0 0 0 0 0 I0 0 0 0 0 0 0co LO N H I 0 0 0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 I DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B10 SENJU 4HD.SDF . JOB TITLE: D5379 OCEAN STREET BLDG 9-12 WATER SUPPLY CURVE I 84*\\\\\\\\ I 0 \\\\\\\\ \\\\\\\\ I I \\\\\\\\ 77+ \\\\\\\\ \\\\\\\\ 74.2 psi @ 859 gpm-> * I I Flow Test Point 70+ Ix 63+ P 56+ RI El SI 5 49+ RI El 42+ P I SI I 35+ 28+ 21+ 14+ LEGEND I X Required Water Supply I 68.60 psi @ 204.2 gpm 7+ H I 0 = Available Water Supply I 83.03 psi @ 204.2 gpm 0++-+---+----+-----+ ------+ --------+ --------+ ---------+ -----------+ 200 300 400 500 600 700 800 900 1000 FLOW (GPM) I I I I I I I I I I I I I I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B13 SENJU 4HD.SDF TITLE: D5379 OCEAN STREET BLDG 13 I JOB WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D I NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SRI 83.7 74.2 859.0 83.3 154.4 59.1 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 154.4 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 54.4 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE I (FT) (PSI) (GPM) 5R2 0.0 SOURCE 59.1 54.4 R2 2.5 - - - - 57.9 - - - P2 2.5 - - - - 46.9 - - - UG2 0.0 - - - - 47.9 - - - 0.0 - - - - 47.8 - - - I UG3 B13 1.5 - - - - 45.6 - - - BOR 2.5 - - - - 44.7 - - - 6.5 - - - - 42.3 I TOR 1A 10.0 - - - - 26.6 - - - 1A1 10.0 - - - - 40.4 - - - lB 10.0 - - - - 22.5 - - - I 1C 10.0 - - - - 25.8 - - - 2A 20.0 - - - - 11.7 - - - 2B 20.0 - - - - 9.1 - - - 20.0 - - - - 7.5 - - - I 2C 2D 20.0 - - - - 7.4 - - - 2E 20.0 - -. - - 7.4 - - - IF 20.0 - - - - 7.7 - - - I 201 19.0 K= 4.90 8.9 14.6 202 19.0 K= 4.90 7.3 13.3 203 19.0 K= 4.90 7.6 13.5 19.0 K= 4.90 7.0 13.0 I 204 205 19.0 - - - - 8.1 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B13 SENJU 4HD.SDF JOB TITLE: D5379 OCEAN STREET BLDG 13 I. PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. I END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) I Pipe: 1 54.4 4.070 PL 17.00 PF 0.1 - SR2 0.0 SRCE 59.1 (N/A) 1.3 150 FTG ETG PE -1.1 R2 2.5 0.0 57.9 0.0 0.001 TL 71.00 PV I Pipe: 2 FIXED PRESSURE LOSS DEVICE R2 2.5 0.0 57.9 0.0 11.0 psi, 54.4 gpm I P2 2.5 0.0 46.9 0.0 Pipe: 3 54.4 4.070 PL 29.00 PF 0.1 P2 2.5 0.0 46.9 0.0 1.3 150 FTG 2ETL PE 1.1 UG2 .0.0 0.0 47.9 0.0 0.001 TL 107.00 PV Pipe: 4 54.4 4.070 PL 125.00 PF 0.2 0.0 0.0 47.9 0.0 1.3 150 FTG E2TL PE 0.0 I UG2 UG3 0.0 0.0 47.8 0.0 0.001 TL 220.00 PV - Pipe: 5 54.4 2.445 PL 115.00 PF 1.5 I UG3 0.0 0.0 47.8 0.0 3.7 150 FTG T3EL PE -0.6 B13 1.5 0.0 45.6 0.0 0.009 TL 166.00 PV I Pipe: 6 54.4 2.003 PL 3.00 PF 0.5 I B13 1.5 0.0 45.6 0.0 5.5 150 FTG 2E PE -0.4 BOR 2.5 0.0 44.7 0.0 0.023 TL 21.00 PV Pipe: 7 54.4 2.067 PL 4.00 PF 0.6 BOR 2.5 0.0 44.7 0.0 5.2 120 FTG BC PE -1.7 TOR 6.5 0.0 42.3 0.0 0.030 TL 21.00 PV I Pipe: 8 54.4 2.003 PL 7.00 PF 0.4 TOR 6.5 0.0 42.3 0.0 5.5 150 FTG E PE -1.5 I 1A1 10.0 0.0 40.4 0.0 0.023 TL 16.00 PV Pipe: 9 54.4 1.101 PL 16.00 PF 13.9 1A1 10.0 0.0 40.4 0.0 18.3 150 FTG 2E2R PE 0.0 1 1A 10.0 0.0 26.6 0.0 0.433 TL 32.00 PV Pipe: 10 38.5 1.101 PL 12.00 PF 4.1 10.0 0.0 26.6 0.0 13.0 150 FTG BR PE 0.0 I 1A lB 10.0 0.0 22.5 0.0 0.229 TL 18.00 PV - Pipe: 11 -15.9 1.101 PL 54.00 PF 3.3 I lB 10.0 0.0 22.5 0.0 5.3 150 FTG EB9R PE 0.0 1C 10.0 0.0 25.8 0.0 0.044 TL 75.00 PV I Pipe: 12 -15.9 1.101 PL 13.00 PF 0.8 I 1C 10.0 0.0 25.8 0.0 5.3 150 FTG B PE 0.0 1A 10.0 0.0 26.6 0.0 0.044 TL 18.00 PV 1 I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B13 SENJU 4HD.SDF TITLE: D5379 OCEAN STREET BLDG 13 I JOB PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 13 54.4 1.101 PL 10.00 PF 6.5 10.0 0.0 22.5 0.0 18.3 150 FTG B PE -4.3 I lB 2A 20.0 0.0 11.7 0.0 0.433 TL 15.00 PV Pipe: 14 37.3 1.101 PL 7.00 PF 2.6 I 2A 20.0 0.0 11.7 0.0 12.6 150 FTG B PE 0.0 2B 20.0 0.0 9.1 0.0 0.216 TL 12.00 PV Pipe: 15 14.6 1.101 PL 3.00 PF 0.6 2B 20.0 0.0 9.1 0.0 4.9 150 FTG EBR PE 0.4 201 19.0 4.9 8.9 14.6 0.038 TL 16.00 PV I Pipe: 16 22.7 1.101 PL 11.00 PF 1.6 • 2B 20.0 0.0 9.1 0.0 7.7 150 FTG E PE 0.0 2C 20.0 0.0 7.5 0.0 0.086 TL 18.00 PV Pipe: 17 13.3 1.101 PL 6.00 PF 0.6 2C 20.0 0.0 7.5 0.0 4.5 150 FTG EBR PE 0.4 202 19.0 4.9 7.3 13.3 0.032 TL 19.00 PV Pipe: 18 9.5 1.101 PL 7.00 PF 0.1 2C 20.0 0.0 7.5 0.0 3.2 150 FTG ---- PE 0.0 I 2D 20.0 0.0 7.4 0.0 0.017 TL 7.00 PV Pipe: 19 13.5 1.101 PL 1.00 PF 0.2 20.0 0.0 7.4 0.0 4.5 150 FTG BR PE 0.4 I 2D 203 19.0 4.9 7.6 13.5 0.033 TL 7.00 PV Pipe: 20 -4.0 1.101 PL 4.00 PF 0.0 I 2D 20.0 0.0 7.4 0.0 1.4 150 FTG ---- PE 0.0 2E 20.0 0.0 7.4 0.0 0.004 TL 4.00 PV • Pipe: 21 13.0 1.101 PL 6.00 PF 0.8 2E 20.0 0.0 7.4 0.0 4.4 150 FTG 2EBR PE 0.4 204 19.0 4.9 7.0 13.0 0.031 TL 26.00 PV I Pipe: 22 -17.0 1.101 PL 5.00 PF 0.3 • 2E 20.0 0.0 7.4 0.0 5.7 150 FTG ---- PE 0.0 2F 20.0 0.0 7.7 0.0 0.051 TL 5.00 PV I Pipe: 23 0.0 1.101 PL 16.00 PF 0.0 2F 20.0 0.0 7.7 0.0 0.0 150 FTG E2BR PE 0.4 205 19.0 0.0 8.1 0.0 0.000 TL 34.00 PV I Pipe: 24 -17.0 1.101 PL 62.00 PF 4.0 2F 20.0 0.0 7.7 0.0 5.7 150 FTG 2B7R PE 0.0 2A 20.0 0.0 11.7 0.0 0.051 TL 79.00 PV I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 I DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B13 SENJU 4HD.SDF e JOB TITLE: D5379 OCEAN STREET BLDG 13 NOTES (HASS) Calculations were performed by the HASS 8.4 computer program under license no. 16080621 granted by HRS Systems, Inc. 208 Southside Square Petersburg, TN 37144 (931) 659-9760 The system has been calculated to provide an average imbalance at each node of 0.005 gpm and a maximum imbalance at any node of 0.100 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 18.3 ft/sec at pipe 9. (4) Items listed in bold print on the cover sheet are automatically transferred from the calculation report. Available pressure at source node SR2 under full flow conditions is 83.23 psi compared to the minimum required pressure of 20.00 psi. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP I PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Ell Tee LngE1l ChkVlv BfyVlv GatVlv AlmChk DPVlv NPTee 2.067 5.00 10.00 3.00 11.00 6.00 1.00 10.00 10.00 10.00 PAGE: E MATERIAL: PVC150 HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Ell Tee LngEll ChkVlv BfyVlv GatVlv NPTee 2.445 10.00 15.00 6.00 23.00 9.00 3.50 17.00 PAGE: F MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) L E B R C S G 45 El BrT RunT Cplg SwCk Gate 1.101 1.00 7.00 5.00 1.00 1.00 8.00 2.00 2.003 2.00 9.00 10.00 1.00 1.00 17.00 3.00 1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B13 SENJU 4HD.SDF I. JOB TITLE: D5379 OCEAN STREET BLDG 13 W MTPRTlT.. P\T 900rT,A W7C• 150 Diameter (in) 4.070 I I I I [1 U I I I I I I I 1 I 11 Equivalent Fitting Lengths in Feet E T L C B G N Ell Tee Long Check Butter Gate NPTee 17.00 34.00 10.00 37.00 20.00 3.00 34.00 0 0 0 0 C N SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B13 SENJU 4HD.SDF JOB TITLE: D5379 OCEAN STREET BLDG 13 N 0 0 0 0 0 0 • • • 0 0 • 0 • 0 0 0 0 00 N —p4W-H---- I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 I DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B13 SENJU 4HD.SDF . JOB TITLE: D5379 OCEAN STREET BLDG 13 WATER SUPPLY CURVE I 84*\0\\\\\\ \\\\\\\\ I \\\\\\\\ I I \\\\\\\\ 77+ \\\\\\\\ I 74.2 psi @ 859 gpm-> * I I Flow Test Point 70+ 63+ x P 56+ RI El SI 5 49+ UI RI E 1 42+ P I SI I 35+ 28+ 21+ 14+ LEGEND I X = Required Water Supply I 59.06 psi 8 154.4 gpm 7+ I 0 = Available Water Supply I 83.30 psi 8 154.4 gpm 0++-+---+----+-----+ ------+ --------+ --------+ ---------+ -----------+ 200' 300 400 500 600 700 800 900 1000 FLOW (GPM) I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B13 SENJU 1HD.SDF I, JOB TITLE: D5379 OCEAN STREET BLDG 13 WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D I NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SR2 83.7 74.2 859.0 83.5 120.0 43.7 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 120.0 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 20.0 GPM NODE ANALYSIS DATA NODE TAG ELEVATION I (FT) I SR2 R2 0.0 2.5 P2 2.5 UG2 0.0 I UG3 0.0 B13 1.5 BOR 2.5 6.5 I TOR 1A 10.0 1A1 10.0 lB 10.0 I 1C 10.0 2A 20.0 2B 20.0 • 2C 20.0 2D 20.0 2E 20.0 2F 20.0 1 201 19.0 202 19.0 203 19.0 19.0 I 204 205 19.0 I I I I NODE TYPE PRESSURE DISCHARGE (PSI) (GPM) SOURCE 43.7 20.0 - - - - 42.6 - - - - - - - 31.6 - - - - - - - 32.7 - - - - - - - 32.6 - - - - - - - 31.8 - - - - - - - 31.2 - - - - - - - 29.4 - - - - - - - 25.7 - - - - - - - 27.8 - - - - - - - 25.0 - - - - - - - 25.5 - - - - - - - 19.7 - - - - - - - 19.4 - - - - - - - 18.9 - - - - - - - 18.8 - - - - - - - 18.7 - - - - - - - 18.5 - - - - - - - 19.8 - - - - - - - 19.4 - - - - - - - 19.2 - - - - - - - 19.1 - - - K= 4.90 16.7 20.0 I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B13 SENJU 1HD.SDF Is JOB TITLE: D5379 OCEAN STREET BLDG 13 PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. I END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) - I Pipe: 1 20.0 4.070 PL 17.00 PF 0.0 SR2 0.0 SRCE 43.7 (N/A) 0.5 150 FTG ETG PE -1.1 R2 2.5 0.0 42.6 0.0 0.000 TL 71.00 PV I Pipe: 2 FIXED PRESSURE LOSS DEVICE R2 2.5 0.0 42.6 0.0 11.0 psi, 20.0 gpm I P2 2.5 0.0 31.6 0.0 Pipe: 3 20.0 4.070 PL 29.00 PF 0.0 P2 2.5 0.0 31.6 0.0 0.5 150 FTG 2ETL PE 1.1 UG2 0.0 0.0 32.7 0.0 0.000 TL 107.00 PV Pipe: 4 20.0 4.070 PL 125.00 PF 0.0 0.0 0.0 32.7 0.0 0.5 150 FTG E2TL PE 0.0 I UG2 UG3 0.0 0.0 32.6 0.0 0.000 TL 220.00 PV • Pipe: 5 20.0 2.445 PL 115.00 PF 0.2 I UG3 0.0 0.0 32.6 0.0 1.4 150 FTG T3EL PE -0.6 B13 1.5 0.0 31.8 0.0 0.001 TL 166.00 PV I Pipe: 6 20.0 2.003 PL 3.00 PF 0.1 I B13 1.5 0.0 31.8 0.0 2.0 150 FTG 2E PE -0.4 BOR 2.5 0.0 31.2 0.0 0.004 TL 21.00 PV I Pipe: 7 20.0 2.067 PL .4.00 PF 0.1 BOR 2.5 0.0 31.2 0.0 1.9 120 FTG BC PE -1.7 TOR 6.5 0.0 29.4 0.0 0.005 TL 21.00 PV I Pipe: 8 20-.0 2.003 PL 7.00 PF 0.1 TOR 6.5 0.0 29.4 0.0 2.0 150 FTG E PE -1.5 I 1A1 10.0 0.0 27.8 0.0 0.004 TL 16.00 PV Pipe: 9 20.0 1.101 PL 16.00 PF 2.2 1A1 10.0 0.0 27.8 0.0 6.7 150 FTG 2E2R PE 0.0 1A 10.0 0.0 25.7 0.0 0.068 TL 32.00 PV Pipe: 10 14.2 1.101 PL 12.00 PF 0.6 10.0 0.0 25.7 0.0 4.8 150 FTG BR PE 0.0 I 1A lB 10.0 0.0 25.0 0.0 0.036 TL 18.00 PV • Pipe: 11 -5.8 1.101 PL 54.00 PF 0.5 I lB 10.0 0.0 25.0 0.0 2.0 150 FTG EB9R PE 0.0 1C 10.0 0.0 25.5 0.0 0.007 TL 75.00 PV I Pipe: 12 -5.8 1.101 PL 13.00 PF 0.1 • 1C 10.0 0.0 25.5 0.0 2.0 150 FTG B PE 0.0 1A 10.0 0.0 25.7 0.0 0.007 TL 18.00 PV 1 I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B13 SENJU 1HD.SDF I JOB TITLE: D5379 OCEAN STREET BLDG 13 PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 13 20.0 1.101 PL 10.00 PF 1.0 10.0 0.0 25.0 0.0 6.7 150 FTG B PE -4.3 I lB 2A 20.0 0.0 19.7 0.0 0.068 TL 15.00 PV Pipe: 14 11.5 1.101 PL 7.00 PF 0.3 I 2A 20.0 0.0 19.7 0.0 3.9 150 FTG B PE 0.0 2B 20.0 0.0 19.4 0.0 0.024 TL 12.00 PV I Pipe: 15 0.0 1.101 PL 3.00 PF 0.0 • 2B 20.0 0.0 19.4 0.0 0.0 150 FTG EBR PE 0.4 201 19.0 0.0 19.8 0.0 0.000 TL 16.00 PV Pipe: 16 11.5 1.101 PL 11.00 PF 0.4 • 2B 20.0 0.0 19.4 0.0 3.9 150 FTG E PE 0.0 2C 20.0 0.0 18.9 0.0 0.024 TL 18.00 PV Pipe: 17 0.0 1.101 FL 6.00 PF 0.0 2C 20.0 0.0 18.9 0.0 0.0 150 FTG EBR FE 0.4 I 202 19.0 0.0 19.4 0.0 0.000 TL 19.00 PV Pipe: 18 11.5 1.101 PL 7.00 PF 0.2 2C 20.0 0.0 18.9 0.0 3.9 150 FTG ---- FE 0.0 2D 20.0 0.0 18.8 0.0 0.024 TL 7.00 PV Pipe: 19 0.0 1.101 FL 1.00 PF 0.0 20.0 0.0 18.8 0.0 0.0 150 FTG BR FE 0.4 I 2D 203 19.0 0.0 19.2 0.0 0.000 TL 7.00 PV Pipe: 20 11.5 1.101 FL 4.00 PF 0.1 I 2D 20.0 0.0 18.8 0.0 3.9 150 FTG ---- FE 0.0 2E 20.0 0.0 18.7 0.0 0.024 TL 4.00 PV I Pipe: 21 0.0 1.101 FL 6.00 PF 0.0 2E 20.0 0.0 18.7 0.0 0.0 150 FTG 2EBR FE 0.4 204 19.0 0.0 19.1 0.0 0.000 TL 26.00 PV I Pipe: 22 11.5 1.101 FL 5.00 PF 0.1 • 2E 20.0 0.0 18.7 0.0 3.9 150 FTG ---- FE 0.0 2F 20.0 0.0 18.5 0.0 0.024 TL 5.00 PV I Pipe: 23 20.0 1.101 FL 16.00 PF 2.3 2F 20.0 0.0 18.5 0.0 6.7 150 FTG E2BR FE 0.4 I 205 19.0 4.9 16.7 20.0 0.068 TL 34.00 PV Pipe: 24 -8.5 1.101 FL 62.00 PF 1.1 2F 20.0 0.0 18.5 0.0 2.9 150 FTG 2B7R FE 0.0 2A 20.0 0.0 19.7 0.0 0.014 TL 79.00 PV I I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 I DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B13 SENJU 1HD.SDF s JOB TITLE: D5379 OCEAN STREET BLDG 13 NOTES (HASS): I (1) Calculations were performed by the HASS 8.4 computer program under license no. 16080621 granted by HRS Systems, Inc. I 208 Southside Square Petersburg, TN 37144 (931) 659-9760 I (2) The system has been calculated to provide an average imbalance at each node of 0.008 gpm and a maximum imbalance at any node of 0.179 gpm. I (3) Total pressure at each node is used -in balancing the system. Maximum water velocity is 6.7 ft/sec at pipe 13. (4) Items listed in bold print on the cover sheet are automatically transferred from the calculation report. I Available pressure at source node SR2 under full flow conditions is 83.40 psi compared to the minimum required pressure of 20.00 psi. I I (6) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPVlv NPTee 2.067 5.00 10.00 3.00 11.00 6.00 1.00 10.00 10.00 10.00 PAGE: E MATERIAL: PVC150 HWC: 150 I Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Ell Tee LngEll ChkVlv BfyVlv GatVlv NPTee U 2.445 10.00 15.00 6.00 23.00 9.00 3.50 17.00 PAGE: F MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet I (in) L E B R C S G 45 El BrT RunT Cplg SwCk Gate 1.101 1.00 7.00 5.00 1.00 1.00 8.00 2.00 2.003 2.00 9.00 10.00 1.00 1.00 17.00 3.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 6/4/2014 C:\HA5583\D5379 OCEAN ST DA B13 SENJU 1HD.SDF JOB TITLE: D5379 OCEAN STREET BLDG 13 P1X1• 1-1 MATERIAL: PVC 200rr,s T-HJr. ifl Diameter (in) 4.070 I I 1-1 I I I I I I I I I I I I Equivalent Fitting Lengths in Feet E T L C B G N Eli Tee Long Check Butter Gate NPTee 17.00 34.00 10.00 37.00 20.00 3.00 34.00 11) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B13 SENJU 1HD.SDF JOB TITLE: D5379 OCEAN STREET BLDG 13 p I I I-fl 00 0 0 0 oia) Cl) Cl) ci) 00 O 11)0 . 1)10 0r-1fl (ON U)Nfll w-1 -1Q fl 04 H(O Id(000) 4 04 1j))J (t -1 (O II r1Lfl -1O>i (l H1 ¼OU)U) (• O'• w 1U) -1 N I I N I 0 0 0 0 0 000 '.0 1 N (c_I U)Cfl çx U)-H-- I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 6/4/2014 C:\HASS83\D5379 OCEAN ST DA B13 SENJU 1HD.SDF I JOB TITLE: D5379 OCEAN STREET BLDG 13 L ! WATER SUPPLY CURVE I 84*0\\\\\\\ I \\\\\\\\ I H \\\\\\\\ 77+ \\\\\\\\ I \\\\\\\\ I 74.2 psi @ 859 gpm-> * I Flow Test Point 70+ I 63+ P 56+ RI El SI S 49+ U RI E Ix 42+ I I I I 28+ 21+ I I I I I 14+ LEGEND I X = Required Water Supply I 43.68 psi @ 120.0 gpm 7+ I 0 = Available Water Supply 83.45 psi @ 120.0 gpm 0++-+---+----+-----+ ------+ --------+ --------+ ---------+ -----------+ 200 300 400 500 600 700 800 900 1000 FLOW (GPM) I I I I