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L W O M E R & A S S O C I A T E S ARCHITECTURAL•ENGINEERING•STRUCTURAL•PLANNING A CERTIFIED MINORITY DESIGN FIRM Old City Hall Building-221 North Wall Street,Suite 600-Spokane,WA 99201 Ogg T:(509)534-4884 F:(509)534-4943 Toll-Free:(888)966-3778 Web Site:www.wwomer.com Creighton Engineering T:(509)921-9755 RECEIVED -D Larry Johnson,EIT A l►G 13 2013 Fire Protection Engineering Technician larryj@creightoneng.com August 13,2013 CITY OFTIGARD Rick Berry BUILDING DIVISION Automatic Fire protection Systems,Inc. 19435 SW 129t Avenue Tualatin,Oregon Project: Hunziker Building Addition 7940 Hunziker Road Tigard,Oregon Rick, We have reviewed the following documents for the Fire Sprinkler systems at the above referenced facility: • Fire Sprinkler Shop Drawings Sheets: FP-1 through FP-3 (PDF files provided) • Hydraulic Calculations for one remote area(PDF file provided) Protection Summary: Systems are required by building and fire codes: OFC 2010, OSSC 2010 Occupancy Classification: Storage(S-1) Square Footage: New Addition 19,752 SF(existing SF not indicated) Occupancy Hazard Classification: Class III commodities palletized to a maximum storage of 22' Available Water Supply: Static: 96 PSI-Res: 94 PSI -Flow: 1480 GPM Design Specifications: Design per NFPA 13(ed. 2010). Shop Drawings: 1. The addition is protected by a new dry pipe fire sprinkler system with a new 6"underground supply and riser supplied through the existing vault and backflow prevention. 2. The FDC is at the existing vault near Hunziker Road, and serves new and existing systems. 3. Site and underground work is described as"by others" and sufficient detail is provided for review of hydraulic calculations. 4. Alarm bell for new system is adjacent to the new riser. 5. Stated design density of 0.24 GPM/SF over 2600 SF is appropriate for Class III commodities palletized to 22' with roof level protection. Hydraulic Calculations: The remote area is calculated for 0.24 GPM/SF over 2600 SF with 22 K=8.0 upright sprinklers flowing and 500 GPM outside hose allowance. This calculation requires 1189 GPM at 78.7 PSI and is satisfied by the available water supply with a buffer of 16 PSI. Z 1 3- DO J ( (O 1c4 0 g vv t�,r- ` Hunziker Building Addition Plan Review 8/13/2013 Page 2 of 2 This review does not cover contractor compliance with project specifications.Womer&Associates/Creighton Engineering are not under agreement to provide field observations of the installation and therefore is not responsible for changes made during installation/construction. This review can be considered comprehensive only to the extent of information provided to us. Field review and acceptance of the installation is by others. Operational satisfaction of the system is the responsibility of the contractor and design engineer. The plans and calculations are found to be in significant compliance with NFPA 13 (ed. 2010) subject to the above review comments. PDF files including our review stamp will be forwarded to your office. Should there be any questions concerning this review of sprinkler system plans,please contact us. Respectfully, WOMER&ASSOCIATES/CREIGHTON ENGINEERING,INC. �� O 0:1 PROFFS Larry Johnson,EIT N l 4, cep % 11959PE �y si (p s.6)` O R E G• q`;" O, '0'4 R ' �G ' ROSS CRS\ EXPIRES: 12/31/13 Hydrant Flow Report for Asset FHOI B005O1 Work Order Number Asset ID FH01B00501 Address Comments Start Date 2009-09-23 00:00:00.0 Assigned To Inspection Number 105043 Completed By BEATTAR Completion Date 2009-09-23 00:00:00.0 jResidual Static Pressure(psi) 96 Gallons Per Minute(gpm) 1480 94 I Pressure(psi) IRating G Crew Project .,- - - - - J.-- 12291 / • ,+. 1 1 i ?t,,,•t,' .-..- , . i.J. .. (17 ,..1.3.3 .-.. it, Q 1)"C.) .,i. - — - . i ,. i / .._, i ; 1 '"... rzs [ limbos liyi ) a.,: ,5 ,.■ 4e/64 6,1 / S i ■ \Z w•Cri I..'4.° I '....1 • t HVO1B0k0iFH011300501 + ,.1/W01800502 , -------------i Flew Hy& J t ■-.,, .. , ... FHO B00601 _--- - .-- 31 1 HS° 6•Ps- W1\1002A08703 '0• VVVO1B0 WHVO1B00601 .. .. ,,•mo2A7,0-NWHDO2A08701 7.?„ • - vikuot000soi., 'YoA, VVV02A08705 - i. 4'-. ,Il'i 0'1 ,-.1. ;,-;'' ...,.., !),,,,,,,...„..t.,...N, N-„, vi? , ',,,;kt j• '''P'''',1,'?.1 ' . •,,' 8255 _ ,-..k i',',-.4::_*.•',:.. '1.11,.4p --- ' . s, ‘-...., ti- ... ',.:'2; -,-----'' ''.-- --- , ..., ;- VVV01803702WNDO1B03701 8255 •''"' - i 44A0...-"I'ri4:-• :2 5 12530 ,.. / '''''''44.7i -: ''' / , 8255 .', WN1301803703' `-• :955 ---1.4'530 '4,...- _ie FH011303701 '"•-, .NV01803701 ''..""6.,,,.... " • 8255 /, , / 41 • WND011303702 4, , ..„,................ VW-4001803302 ‘... Feet jih, wriD01603304FHO1B03301 0 125 HVO1B03307FH-01003302 *NV011303301 h■•■=.1 ::".i...).!) 71WV018133304 ---••,,,,, ,VVVO1B03305 -..... i, ' • • • ' AFP SYSTEMS, INC. 19435 S.W. 129th AVENUE TUALATIN,OR 97062 HYDRAULIC CALCULATIONS FOR Hunziker Bldg. Addition Storage Area FILE NUMBER: Storage Area DATE: AUG 8, 2013 -DESIGN DATA- OCCUPANCY CLASSIFICATION: Class III Commodities Palletized to 22 ft. High DENSITY: .24 gpm/sq.ft. AREA OF APPLICATION: 2600 sq. ft. (Dry System) COVERAGE PER SPRINKLER: 130 sq.ft. Max. NUMBER OF SPRINKLERS CALCULATED: 22 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 689.3 gpm TOTAL WATER REQUIRED (including hose) : 1189.3 gpm FLOW AND PRESSURE (@ BOR) : 689.3 gpm @ 59.7 psi SPRINKLER ORIFICE SIZE: K8.0 NAME OF CONTRACTOR: AFP Systems, Inc. DESIGN/LAYOUT BY: R. Berry AUTHORITY HAVING JURISDICTION: City of Tigard CONTRACTOR CERTIFICATION NUMBER: #67534 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE # 38040986 ) HRS SYSTEMS, INC. WOMER & ASSOCIATES INC./ CREIGHTON ENGINEERING FIRE PROTECTION CONSULTING ENGINEERS Project: Hunziker Building Addition — AFPS # 13089 000 This stamp implies that the designing agency has submitted the plans and required supporting calculations for professional review and the drawings and calculations are found to be in significant compliance with NFPA standards, specifically NFPA 13R, 2010 edition, subject to the August 13, 2013 review letter issued by this office. The review can be considered comprehensive only to the extent of the data supplied to the reviewer. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 8/8/2013:\RICKS DRAWINGS\RICKS CALC FILES\HUNZIKER\STORAGE AREA.SDF JOB TITLE: Hunziker Storage Area j WATER SUPPLY DATA ' SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SOURCE 96.0 94 .0 1480.0 94 .7 1189.3 78.7 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 1189.3 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 500.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 689.3 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 26.2 K= 8.00 15.1 31.1 2 26.5 K= 7.62 15.1 29.6 3 26.8 K= 7. 60 15.4 29. 9 4 27.1 K= 7.58 16.3 30.6 5 27.4 K= 7.56 17.8 31.9 6 25. 6 - - - - 20.6 - - - 7 26.2 K= 8.00 15.2 31.1 8 26.5 K= 7. 62 15.1 29.7 9 26.8 K= 7. 60 15.5 29. 9 10 27.1 K= 7.58 16.3 30.6 11 27.4 K= 7 .56 17. 9 32.0 12 25.6 - - - - 20.7 - - - 13 26.2 K= 8.00 15.4 31.4 14 26.5 K= 7. 62 15.4 29.9 15 26.8 K= 7. 60 15.7 30.1 16 27.1 K= 7.58 16.6 30.9 17 27.4 K= 7.56 18.1 32.2 18 25. 6 - - - - 21.0 - - - 19 26.2 K= 8.00 15.8 31.8 20 26.5 K= 7. 62 15.8 30.3 21 26.8 K= 7.60 16.2 30. 6 22 27.1 K= 7.58 17.0 31.3 23 27.4 K= 7.56 18.6 32.6 24 25.6 - - - - 21.5 - - - 25 27.1 K= 7.58 22.6 36.0 26 27.4 K= 7.56 22.6 35.9 27 25.6 - - - - 23. 9 - - - A 24.3 - - - - 22.8 - - - B 24.3 - - - - 22.9 - - - C 24.3 - - - - 23.2 - - - D 24.3 - - - - 23.8 - - - E 24 .3 - - - - 24.8 - - - F 24 .3 - - - - 44.5 - - - . SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 8/8/2013:\RICKS DRAWINGS\RICKS CALC FILES\HUNZIKER\STORAGE AREA.SDF j JOB TITLE: Hunziker Storage Area 6 NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) G 4.8 - - - - 55.4 - - - H 4.8 - - - - 57.2 - - - BOR 0.7 - - - - 59.7 - - - T 0.0 HOSE STREAM 61.8 500.0 U 0.0 - - - - 79. 9 - - - V 0.0 - - - - 80.2 - - - W 0.0 - - - - 87.7 - - - X 0.0 - - - - 88.3 - - - Y 0.0 - - - - 89.4 - - - Z 0.0 - - - - 91 . 1 - - - SOURCE 31.0 SOURCE 78.7 1189.3 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 , DATE: 8/8/2013:\RICKS DRAWINGS\RICKS CALC FILES\HUNZIKER\STORAGE AREA.SDF JOB TITLE: Hunziker Storage Area j 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 -31.1 2.203 PL 12.17 PF 0.1 1 26.2 8.0 15.1 31.1 2.6 100 FTG ---- PE -0.1 2 26.5 7. 6 15.1 29.6 0.011 TL 12.17 PV Pipe: 2 -60.7 2.203 PL 12.17 PF 0.5 2 26.5 7. 6 15.1 29.6 5.1 100 FTG ---- PE -0.1 3 26.8 7. 6 15.4 29.9 0.038 TL 12.17 PV Pipe: 3 -90.6 2.203 PL 12.17 PF 1.0 3 26.8 7.6 15.4 29. 9 7.6 100 FTG ---- PE -0.1 4 27.1 7.6 16.3 30.6 0.080 TL 12.17 PV Pipe: 4 -121.1 2.203 PL 12.17 PF 1.7 4 27.1 7. 6 16. 3 30.6 10.2 100 FTG ---- PE -0.1 5 27.4 7. 6 17. 8 31.9 0.138 TL 12.17 PV Pipe: 5 -153.0 2.203 PL 3.42 PF 2.0 5 27.4 7. 6 17.8 31.9 12.9 100 FTG T PE 0.8 6 25.6 0.0 20. 6 0.0 0.212 TL 9.49 PV Pipe: 6 -153.0 2.203 PL 1.58 PF 1.6 6 25.6 0.0 20.6 0.0 12.9 100 FTG T PE 0.5 A 24 .3 0.0 22.8 0.0 0.212 TL 7.65 PV - Pipe: 7 -153.0 4.310 PL 10.00 PF 0.1 A 24.3 0.0 22.8 0.0 3.4 100 FTG ---- PE 0.0 B 24.3 0.0 22.9 0.0 0.008 TL 10.00 PV Pipe: 8 -31.1 2.203 PL 12.17 PF 0.1 7 26.2 8.0 15.2 31.1 2.6 100 FTG ---- PE -0.1 8 26.5 7.6 15.1 29.7 0.011 TL 12.17 PV Pipe: 9 -60.8 2.203 PL 12.17 PF 0.5 8 26.5 7.6 15.1 29.7 5.1 100 FTG ---- PE -0.1 9 26.8 7.6 15.5 29.9 0.038 TL 12.17 PV Pipe: 10 -90.7 2.203 PL 12.17 PF 1.0 9 26.8 7.6 15.5 29.9 7.6 100 FTG ---- PE -0.1 10 27.1 7.6 16.3 30. 6 0.081 TL 12.17 PV Pipe: 11 -121.4 2.203 PL 12.17 PF 1.7 10 27.1 7. 6 16.3 30.6 10.2 100 FTG ---- PE -0.1 11 27.4 7. 6 17. 9 32.0 0.138 TL 12.17 PV Pipe: 12 -153.3 2.203 PL 3.42 PF 2.0 11 27.4 7.6 17.9 32.0 12.9 100 FTG T PE 0.8 12 25.6 0.0 20.7 0.0 0.213 TL 9.49 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 8/8/2013:\RICKS DRAWINGS\RICKS CALC FILES\HUNZIKER\STORAGE AREA.SDF q JOB TITLE: Hunziker Storage Area 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 -153.3 2.203 PL 1 .58 PF 1. 6 12 25. 6 0.0 20.7 0.0 12.9 100 FTG T PE 0.5 B 24.3 0.0 22. 9 0.0 0.213 TL 7. 65 PV Pipe: 14 -306.4 4 .310 PL 10.00 PF 0.3 B 24 .3 0.0 22. 9 0.0 6.7 100 FTG ---- PE 0.0 C 24.3 0.0 23.2 0.0 0.029 TL 10.00 PV Pipe: 15 -31.4 2.203 PL 12.17 PF 0.1 13 26.2 8.0 15.4 31.4 2.6 100 FTG ---- PE -0. 1 14 26.5 7.6 15.4 29.9 0.011 TL 12.17 PV Pipe: 16 -61.2 2.203 PL 12.17 PF 0.5 14 26.5 7.6 15.4 29.9 5.2 100 FTG ---- PE -0.1 15 26.8 7.6 15.7 30.1 0.039 TL 12.17 PV Pipe: 17 -91.3 2.203 PL 12.17 PF 1.0 15 26.8 7. 6 15.7 30.1 7.7 100 FTG ---- PE -0.1 16 27. 1 7. 6 16.6 30.9 0.082 TL 12.17 PV Pipe: 18 -122.2 2.203 PL 12 .17 PF 1 .7 16 27.1 7.6 16. 6 30.9 10.3 100 FTG ---- PE -0.1 17 27.4 7.6 18.1 32.2 0. 140 TL 12. 17 PV • Pipe: 19 -154.4 2.203 PL 3.42 PF 2.0 17 27.4 7.6 18.1 32.2 13.0 100 FTG T PE 0.8 18 25. 6 0.0 21.0 0.0 0.216 TL 9.49 PV Pipe: 20 -154.4 2.203 PL 1.58 PF 1.6 18 25.6 0.0 21.0 0.0 13.0 100 FTG T PE 0.5 C 24.3 0.0 23.2 0.0 0.216 TL 7.65 PV Pipe: 21 -460.8 4.310 PL 10.00 PF 0.6 C 24.3 0.0 23.2 0.0 10.1 100 FTG ---- PE 0.0 D 24.3 0.0 23.8 0.0 0.062 TL 10.00 PV Pipe: 22 -31.8 2.203 PL 12. 17 PF 0.1 19 26.2 8.0 15.8 31.8 2.7 100 FTG ---- PE -0.1 20 26.5 7.6 15.8 30.3 0.012 TL 12. 17 PV Pipe: 23 -62.1 2.203 PL 12.17 PF 0.5 20 26.5 7.6 15.8 30.3 5.2 100 FTG ---- PE -0.1 21 26.8 7.6 16.2 30.6 0.040 TL 12.17 PV Pipe: 24 -92.6 2 .203 PL 12.17 PF 1.0 21 26.8 7.6 16.2 30.6 7.8 100 FTG ---- PE -0. 1 22 27.1 7. 6 17.0 31.3 0.084 TL 12.17 PV Pipe: 25 -123.9 2.203 PL 12.17 PF 1.7 22 27.1 7. 6 17.0 31.3 10.4 100 FTG ---- PE -0.1 23 27.4 7. 6 18. 6 32.6 0.144 TL 12.17 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 . DATE: 8/8/2013:\RICKS DRAWINGS\RICKS CALC FILES\HUNZIKER\STORAGE AREA.SDF JOB TITLE: Hunziker Storage Area J 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 -156.6 2.203 PL 3.42 PF 2.1 23 27.4 7.6 18. 6 32 . 6 13.2 100 FTG T PE 0.8 24 25.6 0.0 21.5 0.0 0.221 TL 9.49 PV Pipe: 27 -156.6 2.203 PL 1.58 PF 1.7 24 25. 6 0.0 21.5 0.0 13.2 100 FTG T PE 0.5 D 24.3 0.0 23.8 0.0 0.221 TL 7. 65 PV Pipe: 28 -617.3 4 .310 PL 10.00 PF 1 . 1 D 24.3 0.0 23.8 0.0 13. 6 100 FTG ---- PE 0.0 E 24 .3 0.0 24.8 0.0 0.107 TL 10.00 PV Pipe: 29 -36.0 2.203 PL 12.17 PF 0.2 25 27.1 7.6 22.6 36.0 3.0 100 FTG ---- PE -0.1 26 27.4 7.6 22. 6 35. 9 0.015 TL 12.17 PV Pipe: 30 -72.0 2.203 PL 3.42 PF 0.5 26 27.4 7. 6 22. 6 35.9 6.1 100 FTG T PE 0.8 27 25.6 0.0 23. 9 0.0 0.052 TL 9.49 PV Pipe: 31 -72.0 2.203 PL 1.58 PF 0.4 27 25. 6 0.0 23. 9 0.0 6.1 100 FTG T PE 0.5 E 24.3 0.0 24.8 0.0 0.052 TL 7.65 PV • Pipe: 32 -689.3 4.310 PL 140.50 PF 19.6 E 24.3 0.0 24 .8 0.0 15.2 100 FTG 2E PE 0.0 F 24.3 0.0 44 .5 0.0 0.131 TL 150.21 PV Pipe: 33 -689.3 4 .310 PL 19.17 PF 2.5 F 24.3 0.0 44.5 0.0 15.2 100 FTG ---- PE 8.4 G 4.8 0.0 55.4 0.0 0.131 TL 19.17 PV Pipe: 34 FIXED PRESSURE LOSS DEVICE H 4.8 0.0 57.2 0.0 1 .8 psi, 689.3 gpm G 4.8 0.0 55.4 0.0 Pipe: 35 -689.3 4 .310 PL 2.33 PF 0.7 H 4 .8 0.0 57.2 0.0 15.2 100 FTG B PE 1.8 BOR 0.7 0.0 59.7 0.0 0.131 TL 5.54 PV Pipe: 36 -689.3 6.280 PL 92.00 PF 1.8 BOR 0.7 0.0 59.7 0.0 7.1 140 FTG ET PE 0.3 T 0.0 H.S. 61.8 500.0 0.011 TL 161.00 PV Pipe: 37 -1189.3 6.280 PL 513.00 PF 18.1 T 0.0 H.S. 61.8 500.0 12.3 140 FTG ETG PE 0.0 U 0.0 0.0 79. 9 0.0 0.031 TL 587.00 PV . Pipe: 38 -1189.3 8.390 PL 35.00 PF 0.3 U 0.0 0.0 79. 9 0.0 6. 9 140 FTG ---- PE 0.0 ✓ 0.0 0.0 80.2 0.0 0.008 TL 35.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 8/8/2013:\RICKS DRAWINGS\RICKS CALC FILES\HUNZIKER\STORAGE AREA.SDF JOB TITLE: Hunziker Storage Area 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 FIXED PRESSURE LOSS DEVICE W 0.0 0.0 87.7 0.0 7.5 psi, 1189.3 gpm ✓ 0.0 0.0 80.2 0.0 Pipe: 40 -1189.3 8.390 PL 19.00 PF 0.6 W 0.0 0.0 87.7 0.0 6.9 140 FTG TG PE 0.0 X 0.0 0.0 88.3 0.0 0.008 TL 85.00 PV Pipe: 41 -1189.3 8.390 PL 142.00 PF 1.1 X 0.0 0.0 88.3 0.0 6.9 140 FTG ---- PE 0.0 Y 0.0 0.0 89.4 0.0 0.008 TL 142.00 PV Pipe: 42 -1189.3 10.400 PL 666.00 PF 1 .8 Y 0.0 0.0 89.4 0.0 4.5 140 FTG G PE 0.0 Z 0.0 0.0 91.1 0.0 0.003 TL 674 .00 PV Pipe: 43 -1189.3 12.460 PL 872.00 PF 1 .0 Z 0.0 0.0 91.1 0.0 3.1 140 FTG G PE -13.4 SOURCE 31 .0 SRCE 78.7 (N/A) 0.001 TL 882.00 PV NOTES (HASS) : (1) Calculations were performed by the HASS 8.4 computer program under license no. 38040986 granted by HRS Systems, Inc. 208 Southside Square Petersburg, TN 37144 (931) 659-9760 (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 0.062 gpm. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 15.2 ft/sec at pipe 35. (4) Items listed in bold print on the cover sheet are automatically transferred from the calculation report. (5) Available pressure at source node SOURCE under full flow conditions is 94.48 psi compared to the minimum required pressure of 20.00 psi. • SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 8/8/2013:\RICKS DRAWINGS\RICKS CALC FILES\HUNZIKER\STORAGE AREA.SDF JOB TITLE: Hunziker Storage Area (6) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Ell Tee LngEll ChkV1v BfyVly GatVly NPTee 6.280 22.00 47.00 14 .00 51.00 16.00 5.00 47.00 8.390 31.00 59.00 22.00 76.00 20.00 7.00 59.00 10.400 35.00 80.00 26.00 88.00 30.00 8.00 80.00 12.460 44 .00 98.00 30.00 107.00 34 .00 10.00 98.00 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 ChkVly BfyVly GatVly AlmChk DPV1v NPTee 2.203 3.50 8.50 1 .80 15.00 8.18 1.36 13.64 13.64 13.64 4 .310 6.80 16.00 3.40 30. 66 4 .50 2.79 27.87 27.87 27.87 • WATER SUPPLY ANALYSIS Cm y Static : 96. 00 psi Resid: 94 . 00 psi Flow: 1480 . 0 gpm y 120 . 0 yoo �� r 1 E'M Plable pressure •• 94.67 psi @ 1189.3 gpm x o C i-� 2 B c"' Required pressure H 78.67 psi @ 1189.3 gpm Pr a) H 100 . 0 A. Source Supply Curve n n 1 B. System Demand Curve G u' v' v' rt ro A o o x) U w E x (T) H Z CI G n ccn E 80 . 0 m C a K H V) P x t R cn X E n x K ✓ d S 60 . 0 U 1-t N M n R C E x z c > z r N 1-C ( 40 . 0 mm x H p s Cl) ± o w m 20 . 0 > x Dl > ro • a CDtO o m to 1 0 . 0 -14 . 7 4c0 i 16t JO 8(110 1c00 1)00 1400 00 100 2000 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 . DATE: 8/8/2013:\RICKS DRAWINGS\RICKS CALC FILES\HUNZIKER\STORAGE AREA.SDF JOB TITLE: Hunziker Storage Area i WATER SUPPLY CURVE ' 96*\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\\ I 0 * <-94.0 psi @ 1480 gpm I Flow Test Point I 88+ I I I 80+ I x 1 I 72+ I I I P 64+ R I E I S 1 S 56+ U I R I E 1 48+ ( 1 • P I S 1 I 40+ I I I 32+ I I 1 24+ 1 I 1 16+ LEGEND " I " I X = Required Water Supply " I 78. 67 psi @ 1189.3 gpm IF 8+ II I 0 = Available Water Supply " I 94 .67 psi @ 1189.3 gpm " , I " 0++-+---+----+ + + + + + + 400 600 800 1000 1200 1400 1600 1800 2000 . FLOW (GPM)