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HomeMy WebLinkAbout1991-10-01 Sprinkler System Design Report-79 CITY OF ORONO APPLICATION FOR FIRE SPRINKLER SYSTEM PERMIT COMMERCIAL GENERAL INFORMATION (NOV i 4 1. You may apply for sprinkler system permits by mail (P.O. Box 66, Crystal Bay, MN 55323) or in person at the City offices (1335 South Brown Road). Submit plans for review with this application. Plan review will require a minimum of seven days for staff review. 2. PERMITS ARE NOT VALID UNTIL YOU RECEIVE A PERMIT. WORK MUST NOT BEGIN UNTIL THE PERMIT CARD IS POSTED ON THE JOB SITE. 3. When any new construction or remodeling is involved, a separate building permit must be obtained. 4. All work must be done in accordance with State Building Code requirements and NFPA 13. 5. Three (3) sets of working plans shall be submitted for approval to the authority having jurisdiction before any equipment is installed or remodeled. Deviation from approved plans will require permission of the authority having jursdiction. 6. You shall have the plans approved and stamped and the letter of recommendation from either the I.S.O., Factory Mutual, or Industrial Risk Insured before a permit is issued. 7. All work must be inspected (rough -in and final). Call 473-7357. 24-Hour Notice Required INSTRUCTIONS Complete all items on this application. Sign and date the credential certification. INCOMPLETE APPLICATIONS WILL NOT BE PROCESSED. If you have questions, cell 473-7357. You will be notified by phone when the permit review is complete. Permit will be issued to contractors at the City offices (1335 South Brown Road - Cty. Rd 146). *s•s*f�f::*lf:�w�►*�e�*::�*�r:•��e�***ors+►#s�*:*:•*:�**•f*s:*��:sue:+rfs**:s**tta: Please check one: New Addition Remodel Replace JOB SITE Owner's Name l"tgUl.l'1 CAtmomog Telephone Number Mailing Address 4M 19D k 6o. Sprinkler Contractor's Name(5�L flif Telephone Number g • Contact Person TCINDW[� t���D T Mailing Address Wiky 0. V-0 �_ i CLASSIFICATION OF OCCUPANCIES Light Hazard_X Ordinary Hazard (Group 1) Ordinary Hazard (Group II) Ordinary Hazard (Group III) High -Piled Storage High Rise Building Extra Hazard �t*s�*i�tf�:•�*+rf�*e+rf*�*��*�**:�:#*�**��r�f*w�*�,�:*+r*w***s***s*�f****:swt** WATER SUPPLY Static PSI Residual ICD PSI Hydrant Flow Test Tank:_ Size SCCO Well: Size Other: :*f::*swf*:f:sist***faf:*#f*fa*�:��****•:��:�•:*���f:*���****s**s*:��*::•ws SYSTEM TYPE Wet Dry_ Deluge Preaction Year of Orifice Temperature Make Model Manufacture Size quantity Rating TOTAL Alarm Device Max. Time to Overate Thru Test Pine Type F Make Model I Min. Sec. Alarm Valve Flow Indicato HYDRAULIC CALCULATIONS Design Data: Density GPM/Sq. Ft. Area of Application: Sq. Ft. Coverage per Sprinkler: Sq. Ft. No. of Sprinklers Calcu 9: ak P11 I Total Water Required: PM. INCLUDING HOSE STREAMS. *fs*f:��**s*�*w•�s��t:*��*ff•**ft**t*t:��s�*l��i:::**�**!f*:!�*!��*�*•w:fps SPRINKLER SYSTEM Valuation: $ &a©^7 $30.00 minimum per system plus 1 2 permit fee for plan review. Surcharge based on valuation. Number of Heads: No. of Risers: $2.00 per head .30 per head after initial 50 ::*!�****s*:�*:::::*ss�f:*:**•**����r*::***::a**•s**:***faff*ass*af•ff***f* PERMIT FEE CALCULATION 1. Total of above Installations or Minimum Fee ($30.00) $ 2. State Surcharge. Based on valuation. $ 3. Plan Review Fee (50 % permit fee) _ 4?1. 00_ 4. TOTAL PERMIT FEE add lines 1-3 above L—W�� — The undersigned hereby applies to the City of issuance of a Sprinkler System Permit, agrees to do all work in strict accordance with the ordinances of the City and the r gulations of NFPA 13, and certifies that all statements made on this ap cation are complete, true and correct. Applicant Date b q1 GRINNE LL HYDRAULIC DESIGN INFORMATION SHEET LOCATION 11 BUILDING SYSTEM NO. CONTRACTOR CONTRACT NO. Im-24 o�s•OR CALCULATED BY DRAWING NO. , CONSTRUCTION: COMBUSTIBLE ❑NON.COMBUSTIBLE CEILING HEIGHT" FT. OCCUPANCY APPROVING AUTHORITIES Cr XNFPA. 13: ❑ NFPA 231 ❑OTHER (Specify) _ LT. HAZ. ORD. HAZ GP. 131 ❑2 CD NFPA 231C: FIGURE ; CURVE Z C7 ❑SPECIFIC RULING N W G AREA OF SPRINKLER OPERATION �� DENSITY •1 lbo- r AREA PER SPRINKLER (n HOSE ALLOWANCE GPM: INSIDE HOSE ALLOWANCE GPM: OUTSIDE RACK SPRINKLER ALLOWANCE MADE BY DATE SYSTEM TYPE ❑ EX. HAZ. ❑ WET $(DRY ❑DELUGE ❑PRE•ACTION SPRINKLER OR NOZZLE MAKE MODEL SIZE K•FACTOR �• TEMPERATURE RATING CALCULATION GPM REQUIRED PSI REOUIREDO-A a 36" Is"ciW uKadm", SUMMARY MM "C" FACTOR USED: OVERHEAD lW UNDERGROUND WATER FLOW TEST >- DATE & TIME a STATIC PSI - RESIDUALPSI N GPM FLOWING cr H ELEVATION49 3 LOCATION A SOURCE OF INFORMATION COMMODITY STORAGE HEIGHT W STORAGE METHOD: SOLID PILED C7 PUMP DATA RATED CAPACITY AT PSI ELEVATION CLASS AREA % PALLETIZED O Cl SINGLE ROW ❑CONVENTIONAL PALLET N ❑ DOUBLE ROW ❑SLAVE PALLET / } ❑ MULTIPLE ROW f- O O Y a FLUE SPA LONGITUDIN TANK OR RESERVOIR CAPACITY t= ELEVATION 951.0 WELL PROOF FLOW LOCATION AISLE WID GPM E:JAUTOMATICSTORAGE []ENCAPSULATED ❑SOLIOSHELVING ❑NON- ❑OPEN ENCAPSULATED N INCHES CLEARANCE FROM TOP OF STORAGETO CEILING TRANSVERSE FT. IN. IZONTAL BARRIERS PROVIDED GRINNELLG4322 Re. 447 PRINTED IN U 5 A. 7�EzfiITLEl`F1�CMILLANSPRINKLER YcIS PageMiCC TENNISSYSTEM COURT,HSQUASHICOJRTLADOITION/.10 WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REO'D NODE PRESS. PRESS. pp @ PRES-S. C DEMAND PRESS. TAG (PSI) (PSI) ( GPM ) (PSI) (GPM) (PSI) 23 (N/A) 100.0 (N/A) 100.0 347 .4 90.4 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 347.4 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 247.4 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 23 957.0 SOURCE 90.4 247.4 1D 978.0 - - - - 18.0 - - - 1 980.2 - - - - 17.0 - - - 2S 986.3 K= 5.55 14.3 --1.0 2 980.2 - - - - 18.4 - - - 3D 978.0 - - - - 21.2 - - - 3 980.0 - - - - 20.3 - - - 4S 986.3 K= 5.55 19.7 24.6 4 980.0 - - - - 24.4 - - - 5D 978.0 - - - - 27.2 - - - 5 980.0 - - - - 26.4 - - - 6S 986.3 K= 5.55 23.1 26.7 6 980.0 - - - - 28.2 - - - 7D 974.3 - - - - 32.3 - - - 7 980.0 - - - - 29.9 - - - 8 980.0 - - - - 36.1 - - - 9S 965.5 - - - - 42.4 - - - 9D 965.5 - - - - 42.4 - - - 9 965.5 - - - - 42.4 - - -- 10 972.7 - - - - 39.3 - - - 11D 970.1 - - - - 40.4 - -• - 11 980.0 - - - - 36.1 - - - 12D 978.0 - - - - 14.5 - - - 12 980.2 - - - - 13.5 - - - 13U 986.3 K= 5.55 8.8 16.4 135 986.3 K= 5.55 10.3 17.8 13 980.2 - - - - 16.6 - - - 14D 978.0 - - - - 21.8 - - - 14 980.1 - - - - 20.9 - - is 980.1 980.1 - - - - 23.4 - - - 15U '�86.3 K= 5.55 13.1 20.1 156 986.3 K= 5.55 15.3 21.7 1SD 978.0 - - - - 29.0 - - - 16 980.0 - - - - 28.1 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 JOB TITLE: MACMILLAN TENNIS COURT, SQUASH COURT ADDITION/.10 PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. ENO ELEV . NOZ . PT DISC. VEL( FPS ) HW(C ) (FT) SUM. NODES (FT) ( K ) ( PSI) (GPM) F.L./FT (PSI) Pipe: 1 -20.1 1.104 PL 6.06 PF 1.1 loos 986.3 5.6 13.1 20.1 6.7 100 FTG E PE 2.6 100 980.2 0.0 16.9 0.0 0.144 TL 7.49 PV 0.3 Pipe: 2 -20.1 1.104 PL 1.06 PF 0.2 100 980.2 0.0 16.9 0.0 6.7 100 FTG ---- PE 0.0 1 980.2 0.0 17.0 0.0 0.144 TL 1.06 PV 0.3 Pipe: 3 -0.0 1.iO4 PL 3.31 PF 0.0 1D 978.0 0.0 18.0 0.0 0.0 100 FTG 2ET PE 1.0 1 980.2 0.0 17.0 0.0 0.000 TL 9.73 PV 0.0 Pipe: 4 -20.1 1.104 PL 9.94 PF 1.4 1 980.2 0.0 17.0 0.0 6.7 100 FTG ---- PE 0.0 2 980.2 0.0 18.4 0.0 0.144 TL 9.94 PV 0.3 Pipe: 5 -21.0 1.104 PL 6.06 PF 1.5 2S 986.3 5.6 14.3 21.0 7.0 100 FTG T PE 2.6 2 980.2 0.0 18.4 0.0 0.155 TL 9.63 PV 0.3 Pipe: 6 -41.1 1.104 PL 3.35 PF 1.8 2 980.2 0.0 18.4 0.0 13.8 100 FTG ---- PE 0.1 3 980.0 0.0 20.3 0.0 0.539 TL 3.35 PV 1.3 Pipe: 7 -0.0 1.104 PL 3.25 PF 0.0 3D 978.0 0.0 21.2 0.0 0.0 100 FTG 2ET PE 0.9 3 980.0 0.0 20.3 0.0 0.000 TL 9.67 PV 0.0 Pipe: 8 -41.1 1.104 PL 7.65 PF 4.1 3 980.0 0.0 20.3 0.0 13.8 100 FTG ---- PE 0.0 4 980.0 0.0 24.4 0.0 0.539 TL ".65 PV 1.3 Pipe: 9 -24.6 1.104 PL 6.12 PF 2.0 4S 986.3 5.6 19.7 24.6 8.3 100 FTG T PE 2.7 4 980.0 0.0 24.4 0.0 0.209 TL 9.69 PV 0.5 Pipe: 10 -65.7 1.452 PL 5.64 PF 1.9 4 980.0 0.0 24.4 0.0 12.7 100 FTG ---- PE 0.0 5 980.0 0.0 26.4 0.0 0.338 TL 5.64 PV 1.1 Pipe: it -0.0 1.104 PL 3.23 PF 0.0 5D 978.0 0.0 27.2 0.0 0.0 100 FTG 2ET PE 0.9 5 980.0 0.0 26.4 0.0 0.000 TL 9.65 PV 0.0 Pipe: 12 -65.7 1.452 PL 5.35 PF 1.8 5 980.0 0.0 26.4 0.0 12.7 100 FTG ---- PE 0.0 6 980.0 0.0 28.2 0.0 0.338 TL 5.35 PV 1.1 Pipe: 13 -26.7 1.104 PL 6.17 PF 2.4 6S 986.3 5.6 23.1 26.7 8.9 100 FTG T PE 2.7 6 980.0 0.0 28.2 0.0 0.242 TL 9.74 PV 0.5 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 JOB TITLE: MACMILLAN TENNIS COURT, SQUASH COURT ADDITION/.10 NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 17U 986.3 K= 5.55 17.5 23.2 17S 986.3 K= 5.55 20.4 25.1 17 980.0 - - - - 30.3 - - - 18D 966.0 - - - - 38.5 - - - 18 980.0 - - - - 32.4 - - - 19 980.0 - - - - 37.4 - - - 20 983.0 - - - - 71.6 - - - 21 957.5 - - - - 87.9 - - - 22 956.5 - - - - 89.9 - - - 1005 986.3 K= 5.55 13.1 20.1 100 980.2 - - - - 16.9 - - - 101U 986.3 K= 5.55 7.0 14.7 101S 986.3 K= 5.55 8.2 15.9 101 980.2 - - - - 13.2 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 JOB TITLE: MACMILLAN TENNIS COURT, SQUASH COURT ADDITION/.10 PIPE DATA ( cont 'd ) PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV . NOZ . PT DISC. VEL(FPS) HW(C ) (FT) sum. NODES (FT) (K) (PSI) (GPM) F.L./FT (PSI) Pipe: 14 -92.4 1.452 PL 2.69 PF 1.7 6 980.0 0.0 28.2 0.0 17.9 100 FTG ---- PE 0.0 7 980.0 0.0 29.9 0.0 0.635 TL 2.69 PV 2.2 Pipe: 15 0.0 1.104 PL 6.96 PF 0.0 7D 974.3 0.0 32.3 0.0 0.0 100 FTG 2ET PE 2.5 7 980.0 0.0 29.9 0.0 0.000 TL 13.38 PV 0.0 Pipe: 16 -92.4 1.452 PL 7.00 PF 6.3 7 980.0 0.0 29.9 0.0 17.9 100 FTG E PE 0.0 8 980.0 0.0 36.1 0.0 0.635 TL 9.85 PV 2.2 Pipe: 17 0.0 1.104 PL 0.75 PF 0.0 9D 965.5 0.0 42.4 0.0 0.0 100 FTG T PE 0.0 9 965.5 0.0 42.4 0.0 0.000 TL 4.32 PV 0.0 Pipe: 18 0.0 1.104 PL 4.00 PF 0.0 9S 965.5 0.0 42.4 0.0 0.0 100 FTG T PE 0.0 9 965.5 0.0 42.4 0.0 0.000 TL 7.57 PV 0.0 Pipe: 19 0.0 1.104 PL 19.58 PF 0.0 9 965.5 0.0 42.4 0.0 0.0 100 FTG 6E PE 6.3 11 980.0 0.0 36.1 0.0 0.000 TL 28.14 PV 0.0 Pipe: 20 0.0 1.104 PL 1.00 PF 0.0 11 980.0 0.0 36.1 0.0 0.0 100 FTG T PE 3.2 10 972.7 0.0 39.3 0.0 0.000 TL 4.57 PV 0.0 Pipe: 21 -0.0 1.687 PL 7.19 PF 0.0 10 972.7 0.0 39.3 0.0 0.0 100 FTG T PE 3.2 8 980.0 0.0 36.1 0.0 0.000 TL 12.90 PV 0.0 Pipe: 22 0.0 1.104 PL 11.06 PF 0.0 11D 970.1 0.0 40.4 0.0 0.0 100 FTG 4ET PE 4.3 11 980.0 0.0 36.1 0.0 0.000 TL 20.34 PV 0.0 Pipe: 23 -92.4 1.687 PL 4.00 PF 1.2 8 980.0 0.0 36.1 0.0 13.3 100 FTG ---- PE 0.0 19 980.0 0.0 37.4 0.0 0.306 TL 4.00 PV 1.2 Pipe: 24 -14.7 1.104 PL 11.75 PF 1.2 101U 986.3 5.6 7.0 14.7 4.9 1C) FTG T PE 0.0 101S 986.3 5.6 8.2 15.9 0.080 TL 15.32 PV 0.2 Pipe: 25 -30.6 1.104 PL 6.06 PF 2.3 1015 986.3 5.6 8.2 15.9 10.3 100 FTG E PE 2.6 101 980.2 0.0 13.2 0.0 0.312 TL 7.49 PV 0.7 Pipe: 26 -30.6 1.104 PL 1.06 PF 0.3 101 980.2 0.0 13.2 0.0 10.3 100 FTG ---- PE 0.0 12 980.2 0.0 13.5 0.0 0.312 TL 1.06 PV 0.7 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 JOB TITLE: MACMILLAN TENNIS COURT, SQUASH COURT ADDITION/.10 PIPE DATA ( cont'd ) PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV . NOZ . PT DISC. VEL(FPS) HW(C ) (FT) SUM. NODES (FT) ( K ) ( PSI) (GPM) F.L./FT (PSI) Pipe: 27 -0.0 1.104 PL 3.33 PF 0.0 12D 978.0 0.0 14.5 0.0 0.0 100 FTG 2ET PE 1.0 12 980.2 0.0 13.5 0.0 0.000 TL 9.75 PV 0.0 Pipt. 28 -30.6 1.104 PL 9.94 PF 3.1 12 980.2 0.0 13.5 0.0 10.3 100 FTG ---- PE 0.0 13 980.2 0.0 16.6 0.0 0.312 TL 9.94 PV 0.7 Pipe: 29 -16.4 l.104 PL 12.00 PF 1.5 13U 986.3 5.6 8.8 16.4 5.5 100 FTG T PE 0.0 13S 986.3 5.6 10.3 17.8 0.099 TL 15.57 PV 0.2 Pipe: 30 -34.3 1.104 PL 6.04 PF 3.7 13S 986.3 5.6 10.3 17.8 11.5 100 FTG T PE 2.6 13 980.2 0.0 16.6 0.0 0.385 TL 9.61 PV 0.9 Pipe: 31 -64.9 1.104 PL 3.35 PF 4.2 13 980.2 0.0 16.6 0.0 21.7 100 FTG ---- PE 0.0 14 980.1 0.0 20.9 0.0 1.253 TL 3.35 PV 3.2 Pipe: 32 -0.0 1.104 PL 3.27 PF 0.0 14D 978.0 0.0 21.8 0.0 0.0 100 FTG 2ET PE 0.9 14 980.1 0.0 20.9 0.0 0.000 TL 9.69 PV 0.0 Pipe: 33 -64.9 1.452 PL 7.65 PF 2.5 14 980.1 0.0 20.9 0.0 12.6 100 FTG ---- PE 0.0 15 980.1 0.0 23.4 0.0 0.330 TL 7.65 PV 1.1 Pipe: 34 -20.1 1.104 PL 12.00 PF 2.2 15U 986.3 5.6 13.1 20.1 6.7 100 FTG T PE 0.0 15S 986.3 5.6 15.3 21.7 0.143 TL 15.57 PV 0.3 Pipe: 35 -41.8 1.104 PL 6.10 PF 5.4 15S 986.3 5.6 15.3 21.7 14.0 100 FTG T PE 2.7 15 980.1 0.0 23.4 0.0 0.557 TL 9.67 PV 1.3 Pipe: 36 -106.7 1.452 PL 5.64 PF 4.7 15 980.1 0.0 23.4 0.0 20.7 100 FTG ---- PE 0.0 16 980.0 0.0 28.1 0.0 0.829 TL 5.64 PV 2.9 Pipe: 37 0.0 1.104 PL 3.21 PF 0.0 16D 978.0 0.0 29.0 0.0 0.0 100 FTG 2ET PE 0.9 16 980.0 0.0 28.1 0.0 0.000 TL 9.63 PV 0.0 Pipe: 38 -106.7 1.687 PL 5.35 PF 2.1 16 980.0 0.0 28.1 0.0 15.3 100 FTG ---- PE 0.0 17 980.0 0.0 30.3 0.0 0.399 TL 5.35 PV 1.6 Pipe: 39 -23.2 1.104 PL 12.00 PF 2.9 17U 986.3 3.6 17.5 23.2 7.8 100 FTG T PE 0.0 175 986.3 5.6 20.4 2.5.1 0.187 TL 15.57 PV 0.4 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 J08 TITLE: MACMILLAN TENNIS COURT, SQUASH COURT ADDITION/.10 PIPE DATA ( cont'd ) PIPE TAG G(GPM) DIA( IN) LENGTH PRESS. END ELEV . NO,:. PT DISC. VEL( FPS ) HW(C ) (FT) sum. NODES ( r T ) ( K ) ( PSI) (GPM) F.L./FT (PSI) Pipe: 40 -48.3 1.104 PL 6.19 PF 7.1 175 986.3 5.0 '�0.4 25.1 16.2 100 FTG T PE 2.7 17 980.0 0.0 30.3 0.0 0.727 TL 9.76 PV 1.8 Pipe: 41 -153.0 1.087 PL 2.69 PF 2.1 17 980.0 O.c, 30.3 0.0 22.2 100 FTG ---- PE 0.0 18 960.0 0.0 32.4 0.0 0.1797 TL 2.69 PV 3.3 Pipe: 42 0.0 1.104 PL 17.17 PF 0.0 18D 966.0 0.0 38.5 0.0 0.0 100 FTG 2ET PE 6.1 18 980.0 0.0 32.4 0.0 0.000 TL 23.59 PV 0.0 Pipe: 43 -155.0 1.687 PL 0.50 PF 4.9 18 980.0 0.0 32.4 0.0 22.2 100 FTG T PE 0.0 19 980.0 0.0 37.4 0.0 0.797 TL 6.21 PV 3.3 Pipe: 44 -247.4 2.154 PL 47.42 PF 35.5 19 980.0 0.0 37.4 0.0 21.8 100 FTG 2ET PE 1.3 20 983.0 0.0 71.6 0.0 0.575 TL 61.69 PV 3.2 Pipe: 45 -247.4 3.260 PL 32.33 PF 5.3 20 983.0 0.0 71.6 0.0 9.5 100 FTG 3ETD PE 11.0 21 957.5 0.0 87.9 0.0 0.076 TL 68.73 PV 0.6 Pipe: 46 -247.4 4.260 PL 38.00 PF 1 6 21 957.5 0.0 87.9 0.0 5.6 120 FTG SETG PE 0.4 22 956.5 0.0 89.9 0.0 0.015 TL 110.00 PV 0.2 Pipe: 47 -247.4 4.026 PL 1.00 PF 0.7 22 956.5 0.0 89.9 0.0 6.2 120 FTG ECG PE 0.2 23 957.0 SRCE 90.4 (N/A) 0.020 TL 35.00 PV 0.3 NOTES: (1) Calculations were performed by the HASS 5.5.0 computer program under license no. 422C1326D granted by HRS Systems, Inc. 2193 Ranchwood Dr., N.E. Atlanta, GA 30345 (2) The system has been balanced to provide an average imbalance at each node of 0.004 gpm and a maximum imbalance at any node of 0.179 gpm. (3) Velocity pressures are printed for information only, and are not used in balancing the system. Maximum water velocity in any pipe is 22.2 ft/sec. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 JOB TITLE: MACMILLAN TENNIS COURT, SQUASH COURT ADDITION/.10 !4) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: A MATERIAL: 540 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D Ell Tee LngEli ChkViv BfyVly GatVly AlmChk DPVly 4.026 10.00 i0.00 6.00 22.00 12.00 2.00 20.00 10.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 JOB TITLE: MACMILLAN TENNIS COURT, SQUASH COURT ADDITION/.10 WATER SUPPLY CURVE 120+ r r r r 110+ r r r i r r r r 90+ X r r P 80+ R ' E ' S S 70+ U ; R E 60+ c ' P ' S I 50+ r r 40+ r r 30+ r r r r 20+ LEGEND " X = Required Water Supply " 90.39 psi @ 347.4 gpm " 10+ 0 = Available Water Supply " 100.00 psi @ 347.4 gpm " 0++-+---+----+-----+------+--------+--------+---------+-----------+ 200 300 400 500 600 700 800 900 1000 FLOW (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 Date: 11/12/91 MSc. J08 TITLE= MACMILLAN TENNIS COURT, SQUASH COURT ADDITION/.10 WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS=. Uo PRES!i. @ DEMAND PRESS. TAG (PSI) ( PSI ) ( GPM ) ( PSI ) (GPM) (PSI) 23 (N/A) 100.0 (N/A) 100.0 309.6 61.0 AGGREGATE FLOW ANALYSIS= TOTAL FLOW AT SOURCE 309.6 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 209.6 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 23 957.0 SOURCE 61.0 209.6 1D 978.0 K= 5.55 7.6 15.3 1 980.2 - - - - 7.5 - - - 2S 986.3 - - - - 5.7 - - - 2 980.2 - - - - 8.3 - - - 3D 978.0 K= 5.55 8.6 16.3 3 980.0 - - - - 8.7 - - - 4S 986.3 - - - - 8.5 - - - 4 980.0 - - - - 11.2 - - - 5D 978.0 K= 5.55 11.4 18.7 5 980.0 - - - - 11.7 - - - 6S 98b.3 - - - - 10.1 - - - 6 980.0 - - - - 12.8 - - - 7D 974.3 K= 5.55 13.8 20.7 7 980.0 - - - - 13.4 - - - 8 980.0 - - - - 17.2 - - - 9S 965.5 K= 5.55 8.1 15.8 90 965.5 K= 5.55 8.4 16.1 9 965.5 - - - - 8.8 - - - 10 972.7 - - - 19.0 - - - 110 970.1 K= 5.55 13.4 .20.3 11 980.0 - - - - 12.0 - - - 12D 978.0 K= 5.55 12.4 19.5 12 980.2 - - - - 12.7 - - - 13U 986.3 - - - - 11.5 - - - 13S 986.3 - - - - 11.5 - - - 13 980.2 - - - - 14.1 - - - 14D 978.0 K= 5.55 14.0 20.8 14 980.1 - - - - 14.6 - - - 15 980.1 - - - - 15.6 - - - 15U 986.3 - - - - 13.0 - - - 15S 986.3 - - - - 13.0 - - - 16D 978.0 K= 5.55 15.7 Z22.0 16 '980.0 - - - - 16.5 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 JOB TITLE= MACMILLAN TENNIS COURT, SVUA1-1 COURT ADDITION/.10 NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 17U '986.3 - - - - 14.5 - - - 17S 986.3 - - - - 14.5 - - - 17 980.0 - - - - 17.2 - - - 180 966.0 K= 5.55 19.0 24.2 18 980.0 - - - - 17.6 - - - 19 980.0 - - - - 19.3 - - - 20 983.0 - - - - 44.2 - - - 21 957.5 - - - - 59.1 - - - 22 956.5 - - - - 60.7 - - - 1005 996.3 - - - - 4.8 - - - 100 980.2 - - - - 7.5 - - - 101U 986.3 - - - - 10.1 - - - 1015 986.3 - - - - 10.1 - - - 101 980.2 - - - - 12.7 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 J08 TITLE: MACMILLAN TENNIS COURT, SQUASH COURT AUDITION/.10 PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV . NOZ . PT DISC. VEL(FPS) HW(C ) (FT) SUM. NODES (FT) ( K ) ( PSI) (GPM) F.L./FT (PSI) Pipe: 1 0.0 1.104 PL 6.06 PF 0.0 loos 986.3 0.0 4.8 0.0 0.0 100 FTG E PE 2.6 100 980.2 0.0 7.5 0.0 0.000 TL 7.49 PV 0.0 Pipe: :: 0.0 1.104 PL 1.06 PF 0.0 100 980.21 0.0 7.5 0.0 0.0 100 FTG ---- PE 0.0 1 980.2 0.0 7.5 0.0 0.000 TL 1.06 PV 0.0 Pipe: 3 -15.3 1.104 PL 3.31 PF 0.8 1D '978.0 5.6 7.6 15.3 5.1 100 FTG 2ET PE 1.0 1 980.2 0.0 7.5 0.0 0.086 TL 9.73 PV 0.2 Pipe: 4 -15.3 1.104 PL 9.94 PF 0.9 1 980.2 0.0 7.5 0.0 5.1 100 FTG ---- PE 0.0 2 980.2 0.0 8.3 0.0 0.086 TL 9.94 PV 0.2 Pipe: 5 -0.0 1.104 PL 6.06 PF 0.0 2S 986.3 0.0 5.7 0.0 0.0 100 FTG T PE 2.6 2 980.2 0.0 8.3 0.0 0.000 TL 9.63 PV 0.0 Pipe: 6 -15.3 1.104 PL 3.35 PF 0.3 2 980.2 0.0 8.3 0.0 5.1 100 FTG ---- PE 0.1 3 980.0 0.0 8.7 0.0 0.086 TL 3.35 PV 0.2 Pipe: 7 -16.3 1.104 PL 3.25 PF 0.9 3D 978.0 5.6 8.6 16.3 5.5 100 FTG 2ET PE 0.9 3 980.0 0.0 8.7 0.0 0.097 TL 9.67 PV 0.2 Pipe: 8 -31.6 1.104 PL 7.65 PF 2.5 3 980.0 0.0 8.7 0.0 10.6 100 FTG ---- PE 0.0 4 980.0 0.0 11.2 0.0 0.331 TL 7.65 PV 0.8 Pipe: 9 0.0 1.104 PL 6.12 PF 0.0 4S 986.3 0.0 8.5 0.0 0.0 100 FTG T PE 2.7 4 980.0 0.0 11.2 0.0 0.000 TL 9.69 PV 0.0 Pipe: 10 -31.6 1.452 PL 5.64 PF 0.5 4 980.0 0.0 11.2 0.0 6.1 100 FTG ---- PE 0.0 5 980.0 0.0 11.7 0.0 0.087 TL 5.64 PV 0.3 Pipe: 13 -18.7 1.104 PL 3.23 PF 1.2 5D 978.0 5.6 11.4 18.7 6.3 100 FTG 2ET PE 0.9 S 980.0 0.0 11.7 0.0 0.126 TL 9.65 PV 0.3 Pipe: 12, -50.3 1.452 PL 5.35 PF 1.1 5 980.0 0.0 11.7 0.0 9.8 100 FTG ---- PE 0.0 6 980.0 0.0 12.8 0.0 0.206 TL 5.35 PV O.b Pipe: 13 0.0 1.104 PL 6.17 PF 0.0 6S '986.3 0.0 10.1 0.0 0.0 100 FTG T PE 2.7 6 980.0 0.0 121.8 0.0 0.000 TL 9.74 PV 0.0 -.FS;INKLER SYSTEM HYDRAULIC ANALYSIS Page 4 JOB TITLE: MACMILLAN TENNIS COURT, SQUASH COURT ADDITION/.10 PIPE DATA ( cont 'd ) PIPE TAG Q( GPM ) DIA( IN ) LENGTH PRESS. END ELEV . NOZ . PT DISC. VEL( FPS ) HW(C ) (FT) sum. NODES (FT) ( K ) ( PSI) (GPM) F.L./FT (PSI) Pipe: 14 -50.3 1.452 PL 2.69 PF 0.6 6 980.0 0.0 12.8 0.0 9.8 100 FTG ---- PE 0.0 7 980.0 0.0 13.4 0.0 0.206 TL 2.69 PV 0.6 Pipe: 15 -20.7 1.104 PL 6.96 PF 2.0 7D 974.3 5.6 13.8 20.7 6.9 100 FTG, 2ET PE 2.5 7 980.0 0.0 13.4 0.0 0.151 TL 13.38 PV 0.3 Pipe: 16 -71.0 1.452 PL 7.00 PF 3.8 7 980.0 0.0 13.4 0.0 13.8 100 FTG E PE 0.0 8 980.0 0.0 17.2 0.0 0.390 TL 9.85 PV 1.3 Pipe: 17 -16.1 1.104 PL 0.75 PF 0.4 9D 965.5 5.6 8.4 16.1 5.4 100 FTG T PE 0.0 9 965.5 0.0 8.8 0.0 0.095 TL 4.32 PV 0.2 Pipe: 18 -15.8 1.104 PL 4.00 PF 0.7 9S 965.5 5.6 8.1 15.8 5.3 100 FTG T PE 0.0 9 965.5 0.0 8.8 0.0 0.092 TL 7.57 PV 0.2 Pipe: 19 -31.9 1.104 PL 19.58 PF 9.5 9 965.5 0.0 8.8 0.0 10.7 100 FTG 6E PE 6.3 11 980.0 0.0 12.0 0.0 0.337 TL 28.14 PV 0.8 Pipe: 20 -52.2 1.104 PL 1.00 PF 3.8 1: 980.0 0.0 12.0 0.0 17.5 100 FTG T PE 3.2 10 972.7 0.0 19.0 0.0 0.839 TL 4.57 PV 2.1 Pipe: 21 -52.2 1.687 PL 7.19 PF 1.4 10 972.7 0.0 19.0 0.0 7.5 100 FTG T PE 3.2 8 980.0 0.0 17.2 0.0 0.106 TL -2.90 PV 0.4 Pipe: 22 -20.3 1.104 PL 11.06 PF 3.0 11D 970.1 5.6 13.4 20.3 6.8 100 FTG 4ET PE 4.3 11 980.0 0.0 12.0 0.0 0.146 TL 20.34 PV 0.3 Pipe: 23 -123.2 1.687 PL 4.00 PF 2.1 8 980.0 0.0 17.2 0.0 17.7 100 FTG, ---- PE 0.0 19 980.0 0.0 19.3 0.0 0.521 TL 4.00 PV 2.1 Pipe: 24 0.0 1.104 PL 11.75 PF 0.0 101U 986.3 0.0 10.1 0.0 0.0 100 FTG T PE 0.0 1015 986.3 0.0 10.1 0.0 0.000 TL 15.32 PV 0.0 Pipe: 25 -0.0 1.104 PL 6.06 PF 0.0 lO1S 986.3 0.0 10.1 0.0 0.0 100 FTG E PE 2.6 101 980.2 0.0 12.7 0.0 0.000 TL 7.49 PV 0.0 Pipe: 26 0.0 1.104 PL 1.06 PF 0.0 101 980.2 0.0 12.7 0.0 0.0 100 FTG ---- PE 0.0 12 900.2 0.0 12.7 0.0 0.000 TL 1.06 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 JOB TITLE: MACMILLAN TENNIS COURT, SQUASH COURT ADDITION/.10 PIPE DATA (cont'd ) PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV . NUZ . PT DISC. VEL(FPS) HW(C ) (FT) sum. NODES (FT) ( K ) ( F15I ) GF•M ) F.L./FT (PSI) Pipe: 27 -19.5 1.104 PL 3.3�; PF 1.3 12-D '978.0 5.4:, 12.4 19.5 6.5 100 FTG 2ET PE 1.0 12 980.2 0.0 12.7 0.0 0.136 TL 9.75 PV 0.3 Pipe: 28 -19.5 1.104 PL 9.94 PF 1.4 1� 980.2 0.0 12.7 0.0 6.5 100 FTG ---- PE 0.0 13 980.2 0.0 14.1 0.0 0.136 TL 9.94 PV 0.3 Pipe: 29 0.0 1.104 PL 12.00 PF 0.0 13U 986.3 0.0 11.5 0.0 0.0 100 FTG T PE 0.0 13S 986.3 0.0 11.5 0.0 0.000 TL 15.57 PV 0.0 Pipe: 30 0.0 1.104 PL 6.04 PF 0.0 13S 986.3 0.0 11.5 0.0 0.0 100 FTG T PE 2.6 13 980.2 0.0 14.1 0.0 0.000 TL 9.61 PV 0.0 Pipe: 31 -19.5 1.104 PL 3.35 PF 0.5 13 980.2 0.0 14.1 0.0 6.5 100 FTG ---- PE 0.0 14 980.1 0.0 14.6 0.0 0.136 TL 3.35 PV 0.3 Pipe: 32 -20.8 1.104 PL 3.27 PF 1.5 14D 978.0 5.6 14.0 20.8 7.0 100 FTG 2ET PE 0.9 14 980.1 0.0 14.6 0.0 0.153 TL 9.69 PV 0.3 Pipe: 33 -40.3 1.452 PL 7.65 PF 1.0 14 980.1 0.0 14.6 0.0 7.8 100 FTG ---- PE 0.0 15 980.1 0.0 15.6 0.0 0.137 TL 7.65 PV 0.4 Pipe: 34 0.0 1.104 PL 12.00 PF 0.0 15U 986.3 0.0 13.0 0.0 0.0 100 FTG T PE 0.0 155 986.3 0.0 13.0 0.0 0.000 TL 15.57 PV 0.0 Pipe: 35 -0.0 1.104 PL 6.10 PF 0.0 15S 986.3 0.0 13.0 0.0 0.0 100 FTG T PE 2.7 15 980.1 0.0 15.6 0.0 0.000 TL 9.67 PV 0.0 Pipe: 36 -40.3 1.452 PL 5.64 PF 0.8 15 980.1 0.0 15.6 0.0 7.8 100 FTG ---- PE 0.0 16 980.0 0.0 16.5 0.0 0.137 TL 5.64 PV 0.4 Pipe: 37 -22.0 1.104 PL 3.21 PF 1.6 16D 978.0 5.6 15.7 22.0 7.4 100 FTG 2ET PE 0.9 16 980.0 0.0 16.5 0.0 0.169 TL 9.63 PV 0.4 Pipe: 38 -62.3 1.687 PL 5.35 PF 0.8 16 980.0 0.0 16.5 0.0 8.9 100 FTG ---- PE 0.0 17 980.0 0.0 17.2 0.0 0.147 TL 5.35 PV 0.5 Pipe. 39 0.0 1.104 PL 12.00 PF 0.0 17U 986.3 0.0 14.5 0.0 0.0 100 FTG T PE 0.0 175 986.3 0.0 14.5 0.0 0.000 TL 15.57 PV 0.0 SPRINKLER SYST-Ei1 t-'i DRAULI,-- Page 0 JOE TITLE NACNILL"N TENNIS COURT, SQUASH COURT ADDITION/.10 PIPE DATA ( cunt 'd ) PIPE rAG :( UPM) 01A(IN) LENGTH PRESS. END ELE', NOZ . PT DISC . VEL( FP.;. ) HW( C ) ( i= f ) SUM. NODES ( FT ) ( k ) ( P',I) ( GPM ) F .L FT (PSI) Pipe: 40 -0.0 1.104 PL 6.19 PF 0.0 17S 986.3 0.0 14.5 0.0 0.0 100 FTG T PE 2.7 17 0.0 17.2 0.0 0.000 TL 9.76 PV 0.0 Pipe; 41 -6Z . _ 1 . c.87 PL 2 .69 PF 0.4 17 980.0 0.0 17.2 0.0 8.19 100 FTG ---- PE 0.0 13 980.0 0.0 17.6 0.0 0.147 TL 2.69 PV 0.5 Pipe: 42 -24.2 1.104 PL 17.17 PF 4.8 18D 966.0 S.b 19.0 24.2 8.1 100 FTG 2ET PE 6.1 18 980.0 0.0 17.6 0.0 0.202 TL 23.59 PV 0.4 Pipe; 43 -86.5 1.687 PL 0.50 PF 1.7 18 980.0 0.0 17.6 0.0 12.4 100 FTG T PE 0.0 19 980.0 0.0 19.3 0.0 0.270 TL 6.21 PV 1.0 Pipe: 44 -209.6 -2.154 PL 47.42 PF 26.1 19 980.0 0.0 19.3 0.0 18.5 100 FTG 2ET PE 1.3 20 983.0 0.0 44.2 0.0 0.424 TL 61.69 PV 2.3 Pipe: 45 -209.6 3.260 PL 32.33 PF 3.9 20 983.0 0.0 44.2 0.0 8.1 100 FTG 3ETD PE 11.0 21 957.5 0.0 59.1 0.0 0.056 TL 68.73 PV 0.4 Pipe 46 -209.6 4.260 PL 38.00 PF 1.2 21 957.5 0.0 59.1 0.0 4.7 120 FTG 5ETG PE 0.4 22 956.5 0.0 60.7 0.0 0.011 TL 110.00 PV 0.1 Pipe: 47 -209.6 4.026 PL 1.00 PF 0.5 22 956.5 0.0 60.7 0.0 5.3 120 FTG ECG Pt 0.2 SRCE 61.0 (N/A) 0.014 TL 35.00 PV 0.2 NOTES. (1) Calculations were performed by the HASS S.5.0 computer program under license no. 422C1326D granted by HRS Systems, Inc. 2193 Ranchwood Dr., N.E. Atlanta, GA 30345 (2) The system has been balanced to provide an average imbalance at each node of 0.004 gpm and a maximum imbalance at any node of 0.194 gpm. (3) Velocity pressures are printed for information only, and are not used in balancing the system. Maximum water velocity in any pipe is 18.5 ft/sec. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 JOB TITLE: MACMILLAN TENNIS COURT, SQUASH COURT ADDITION/.10 (4) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIF PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D Ell Tee LngEll ChkVly BfyVly GatVly A1mChk DPVly 4.026 10.00 20.00 6.00 ZZ2.00 12.00 2.00 20.00 10.00