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7271 CALLE PLATA; ; AS070010
8/9/24, 11:40 AM AS070010 Permit Data City of Carlsbad Sprinkler Permit Job Address: 7271 CALLE PLATA Permit Type: SPRINK Parcel No: 2230320400 Lot #: 0 Reference No.: Permit No: AS0700I0 Status: ISSUED Applied 1/19/2007 Approved: 1/19/2007 Issued: 1/19/2007 PC #: Inspector: Project Title: HUNTER'S POINT THREE FIRE SPRINKLER INSPECTIONS @ $62/EA Applicant: SOUTHLAND FIRE PROTECTION, INC 4733 PT. LOMAAV SAN DIEGO, CA 92107 619-523-1400 Owner: REAL ESTATE COLLATERAL MANAGEMENT CO C/O MORROW DEV/ LIZ LAYMAN 1903 WRIGHT FL #180 CARLSBAD CA Fees ($)J Add'I Fees ($) Total ($) Balance ($) 186 0 186 0 about:blarik 1/1 13-190 . . INSTALLATION OF SPRINKLER SYSTEMS . A&)400ic) Contractor's Material and Test Certificate for Aboveground Piping PROCEDURE Upon completion of work, inspection and tests shall be made by the contractor's representative and witnessed by an owners representative. All detects shall be corrected and system left in service before contractor's personnel finally leave the job. A certificate shall be filled out and signed by both representatives. Copies shall be prepared for approving authorities, owners, and contractor. It Is understood the owners representative's signature in no way prejudices any claim against contractor for faulty material, poor workmanship, or failure to comply with approving authorlts requirements or local ordinances. Property name po Property address C/l Accepted by approving authorities (names) Address Plans Installation conforms to accepted plans [) Yes 0 No Equipment used Is approved Yes 0 No It no, explain deviations Has person in charge of fire equipment been instructed as Yes 0 No to location of control valves and care and maintenance . of this new equipment? If no, explain Instructions Have copies of the following been left on the premises? Yes 0 No System components instructions' Yes 0 No Care and maintenance Instructions Yes 0 No NFPA25 Yes 0 No Location of system Supplies buildings Year of Orifice Temperature M.eI. / M9pel manufacture 1 51ze QUantitY rating *!.x4f4'1<e1,b(e jtt. Sprinklers 0 2rp Pipe and Type of pipe CPU fittings Type of fittings Alarm C10L1C Maximum time to operate Alarm device _________________ valve or Make through test connection flow . Model Minutes Seconds indicator valve QO.D. Make 'MQck.& Serial no Make Model Serial no. Dry pipe Time to trip Time water Alarm operating through test Water Trip point reached; operated test - conp.ec110n1'2 pressure pressure -.a1rpressure test outlet"2 properly Minutes Seconds I psi psi Minutes Seconds Yes No With If no, explain . 1 Measured from time Inspector's test connection is opened 2 NFPA 13 only requires the 60-second limitation in specific sections FIGURE 16.1 Contractor's Material and Test Certificate for Aboveground Piping. 2002 Edition SYSTEMS ACCEPTANCE 13-19 Operation El Pneumatic El Electric CD Hydraulics Piping supervised Yes El No Detecting media supervised D Yes No Does valve operate from the manual trip, remote, or both Yes El No control stations? Deluge and preaction Is there an accessible facility In each circuit If no, explain for testinvalvesg? El Yes EJNo Does each circuit operate Does each circuit operate Maximum time to Make Model supervision loss alarm? valve release? operate release Yes No Yes No Minutes Seconds Location Make and Setting Static pressure Residual pressure Flow rate Pressure and floor model (flowing) reducing valve tam Inlet (psi) Outlet (psi) Inlet (psi) Outlet psi) Flow (gpm) ( Hydrostatic: tests shall be made at not less than 200 psi (13.6 bar) for hours or 50 psi (3.4 bar) above stati ressure in excess of 150 psi (10.2 bar) for 2 hours. Differential dry-pIpe valve clappers shall be left o ng the test to prevent damage. All aboveground piping leakage shall be stopped. Test description Pneumatic: Establish 40 psi (2.7 bar) air pressure and measure drop, which shall not exceed 1½ psi (0.1 bar) In 24 hours. Test pressure tanks at normal water level and air pressure and measure air pressure drop, which shall not exceed l½ psi (0.1 bar) 1n24hours. All piping hydrostatically tested at pal (__ bar) for hours If no, state mason Dry piping pneumatically tested El Yes El No Equipment operates properly (, Yes El No Do you certify as the sprinkler contractor that additives and corrosive chemicals, sodium silicate or derivatives of sodium pilcate, brine, or other corrosive chemicals were not used for testing systems or stopping leaks? Elves El No Drain Reading of gauge located,yiar water Residual pressure with 'J In test Tests test .& supply test connection: 7 psi (_bar) connection open wide: L) psi (.- bar) Underground mains and lead-In connections to system risers flushed before connection made to sprinkler piping Verified by co' of the Contractors Material and Test Yes El No Other Explain Certificate for Underground Piping. Flushed by Installer of underground sprinkler piping Yes El No If powder-driven fasteners are used in concrete, El Yes No If no, explain has representative sample testing been satisfactorily completed? Blank testing Number used Locations Number removed gaskets Welding piping El Yes No If yes. Do you certify as the sprinkler contractor that welding procedures comply El Yes El No with the requirements of at least AWS B2.1? Welding ng Do you certify that the welding was performed by welders qualified In El Yes El No compliance with the requirements of at least AWS B2.1? Do you certify that the welding was carried out In compliance with a El Yes El. No documented quality control procedure to ensure that all discs are retrieved, that openings in piping are smooth, that slag and other welding residue are - removed, and that the Internal diameters of piping are not penetrated? Cutouts Do you certify that you have a control feature to ensure that El Yes El No (discs) all cutouts (discs) are retrieved? FIGURE 16.1 Continued 2002 Edition 13-192 INSTALLATION OF SPRINKLERSYST E M S Hydraulic Nameplate provided Ii no, explain data nameplate Yes [I] No Date left in service with all control val v e s o p e n Remarks Name of sprinkler contractor Tests se Signatures Forp~j 8 tie Date Zell, For sprinkler contractor (signed) Title Date Additional explanations and notes FIGURE 16.1 Continued 16.2.1.2 Portions of systems no ç m a l l y s u b j e c t e d t o s y s t e m working pressures in excess of 15 0 p s i ( 1 0 . 4 b a r ) s h a l l b e tested as described in 16.2.2.1 at a p r e s s u r e o f p s i ( 3 . 5 b a r ) in excess of system working pressure. 16.2.1.3 Where cold weather will n o t p e r r n i t t e s t i n g w i t h w a - ter, an interim air test shall be perm i t t e d t o b e c o n d u c t e d a s described in 16.2.3. 16.2.1.4 Modifications affecting 20 o r f e w e r s p r i n k l e r s s h a h not require testing in excess of sy s t e m w o r k i n g p r e s s u r e . 16,2.1.5 Where addition or modif i c a t i o n i s m a d e t o a n e x i s t - ing system affecting more than 20 spr i n k l e r s , t h e n e w p o r t i o n shall be isolated and tested at not les s t h a n 2 0 0 p s i ( 1 3 . 8 b a r ) for 2 hours. open sprinklers after the test is c o m p l e t e d , o r t h e o p e r a t i n g elements of automatic sprinklers sh a l l b e r e m o v e d a f t e r t h e test is completed. 16.2.1.12* The trench shall he b a c k f l l l e d b e t w e e n j o i n t s b e - fore testing to prevent movement of pip e . 16.2.1.13 Where required for safety m e a s u r e s p r e s e n t e d b y the hazards of open tnn.hes, the pipe and joints shall be per-mitted to be backfilled provided the installing contractor takes the responsibility lot locatin g and correcting leakage in eXCeSS of that permitted in 16.2.1.8. 16.2.1.1.4. Provision .shall -be ..madeior..the proper disposal of water used for flushing or testiag. . .: 16.2.1.15* Test Blanks. 16.2.1.6 Modifications that cannot be isol a t e d , s u c h a s r e l o - cated drops, shall not require testin g i n e x c e s s o f s y s t e m w o r k - 16.2.1.15.1 Test blanks shall have painted lugs p r o t r u d i n g i n lug pressure. such a way as to clearly indicate t h e i r p r e s e n c e . 16.2.1.7 Lossshall be determined by a drop i n g a u g e p r e s 16.2.1.15.2 ilit. Lest blanks shall be numbere d , a n d t h e i n . - sure or visual leakage. stalling contractor shall have a recor d k e e p i n g m e t h o d e n s u r - ing their removal after work is co m p l e t e d . 16.2.1.8 The test pressure shall be r e a d f r o m a g a u g e l o c a t e d at the low elevation point of the s y s t e m o r p o r t i o n b e i n g 16.2.1.16 When subject to hydrost a t i c t e s t p r e s s u r e s , t h e c l a p - tested, per of a differential-type valve sh a l l b e h e l d o f f i t s s e a t t o p r e - vent damaging the valve. 16.2.1.9 Additives, corrosive chemicals such a s s o d i u m s i l i - cate, or derivatives of sodium silicat e , b r i n e , o r o t h e r c h e i n i - 16.2.2 Dry Pipe and Double Interlock System(s) Air Test. cats shall not be used while hydrosta t i c a l l y t e s t i n g s y s t e m s o r . 16.2.2.1 In addiuon to the standard hydrostatic test an air f leaks or stopping , pressure leakage test at 40 psi (2.8 bar) shall be conductedfor 16.2.1.10 Piping between the exterior fire department con- 24 hours. Any leakage that results in a loss of pressure in excess necrion and the check valve in the fi r e d e p a r t m e n t i n l e t p i p e of 1½ psi (0.1 bar) for the 24 hours shall be corrected. shall be hydrostatically tested in the same manner, as-the-bal- tall 16.2.2.2 Where systems are insed es in spac that are ca- ance of the system. ys . pable of being operated at temperatu r e s . . b e l o w 16.2.1.11 When deluge systems are being h y d r o s t a t i c a l l y pressure leakage tests required in 1 6 . 2 . 2 s h a l l b e c q n d u c t e d a t tested, plugs shall be installed in fitt i n g s a n d r e p l a c e d w i t h the lowest nominal temperature of t h e s p a c e . 2002 Edition 4 SOUTHLAND FIRE PROTECTION, INC. 4733 POINT LOMA AVENUE SAN DIEGO,CA 92107 HYDRAULIC CALCULATIONS FOR Hunter's Pointe Building Type 1 Cab. Family Apartments Carlsbad, CA FILE NUMBER: 06-144 DATE: JAN 2, 2007 -DESIGN DATA- OCCUPANCY CLASSIFICATION: R-1 jq APPROVED 17D O APPROVED AS NOTED O NOT PFOVED, RESUBMIT CHECKIC " F CPF0RMAN WITH RUE 1' C TiE •:. yhH THE . r D0CU.0 i;iY S f-s? FOB L S cc:. ED AND C0PEL itE JOB SiTE ANO FO 'OlATIc OF Th WURr Or I.LL DENSITY: AREA OF APPLICATION: COVERAGE PER SPRINKLER: NUMBER OF SPRINKLERS CALCULATED TOTAL SPRINKLER WATER FLOW REQUIRED TOTAL WATER REQUIRED (including hose): FLOW AND PRESSURE (@ BOR) SPRINKLER ORIFICE SIZE: NAME OF CONTRACTOR: DESIGN/LAYOUT BY: AUTHORITY HAVING JURISDICTION: CONTRACTOR CERTIFICATION NUMBER: 05 gpm/sq. ft. Remote Area 1 256 sq. ft. 4 sprinklers 56.7 gpm 56.7 gpm 56.7 gpm @ 54.4 psi 1/2 inch Southland Fire Protection, Inc. Sorida Phan Carslbad Fire Department C-16- 911956 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE # 27091255 HRS SYSTEMS, INC. TUCKER, GA 30084 APPROVED ITTED - CARLSBAD FIRE DUPARTMENT A60-rk-10('~ SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 1/2/2007 C:\HASS78\06-144SDF.SDF JOB TITLE: Hunters Point Building Type I Cab. WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) 1 94.5 89.1 1500.0 94.5 56.7 75.3 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 56.7 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 56.7 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 0.0 SOURCE 75.3 56.7 2 0.0 - - - - 75.3 3 3.0 - - - - 74.0 - - - 4 3.0 - - - - 66.0 - - - 5 0.0 - - - - 67.2 - - - 5A 0.0 - - - - 65.2 - - - 6A 4.0 - - - - 63.2 BOR 5.0 - - - - 54.4 - - - TOR 14.0 - - - - 41.6 - - - 6 14.0 - - - - 29.0 - - - 7 14.0 - - - - 26.0 - - - 8 14.0 - - - - 24.5 9 14.0 - - - - 21.7 - - - 10 14.0 - - - - 21.7 - - 11 14.0 - - - - 21.8 - - - 12 14.0 - - - - 21.8 - - - 20 24.0 - - - - 20.2 - - - 21 24.0 - - - - 19.9 - - - 22 24.0 - - - - 16.5 - - - 23 24.0 - - - - 16.3 - - - 24 24.0 - - - - 15.5 - - - 25 24.0 - - - - 14.9 - - - 26 24.0 - - - - 17.0 - - - 27 24.0 - - - - 17.1 - - - 28 24.0 - - - - 17.1 - - - 29 24.0 - - - - 17.1 - - - 30 24.0 - - - - 16.1 - - - 31 24.0 - - - - 15.9 - - - 32 24.0 - - - - 16.8 - - - 33 24.0 - - - - 16.6 - - - 40 34.0 - - - - 11.9 - - - 41 34.0 - - - - 11.6 - - - 42 34.0 - - - - 11.5 - - - 43 34.0 - - - - 11.7 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 1/2/2007 C:\HASS78\06-144SDF.SDF JOB TITLE: Hunters Point Building Type I Caic. NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 44 34.0 - - - - 8.6 - - - 45 34.0 - - - - 8.6 - - - 46 34.0 - - - - 8.8 - - - 47 34.0 - - - - 8.8 - - - 48 34.0 - - - - 9.4 - - - 49 34.0 - - - - 8.9 - - - 50 34.0 - - - - 10.6 - - - 51 34.0 - - - - 10.9 - - - Si 34.0 K= 4.90 8.4 14.2 S2 34.0 K= 4.90 8.2 14.0 S3 34.0 K= 4.90 8.5 14.3 S4 34.0 K= 4.90 8.5 14.3 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 1/2/2007 C:\HASS78\06-1445DF.SDF JOB TITLE: Hunters Point Building Type I Caic. 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 56.7 6.340 PL 22.00 PF 0.0 1 0.0 SRCE 75.3 (N/A) 0.6 140 FTG ETG PE 0.0 2 0.0 0.0 75.3 0.0 0.000 TL 99.58 PV Pipe: 2 56.7 3.068 PL 4.00 PF 0.0 2 0.0 0.0 75.3 0.0 2.5 140 FTG E PE -1.3 3 3.0 0.0 74.0 0.0 0.004 TL 13.31 PV Pipe: 3 FIXED PRESSURE LOSS DEVICE 3 3.0 0.0 74.0 0.0 8.0 psi, 56.7 gpm 4 3.0 0.0 66.0 0.0 Pipe: 4 56.7 3.068 PL 4.00 PF 0.0 4 3.0 0.0 66.0 0.0 2.5 140 FTG E PE 1.3 5 0.0 0.0 67.2 0.0 0.004 TL 13.31 PV Pipe: 5 56.7 2.067 FL 83.50 PF 2.0 5 0.0 0.0 67.2 0.0 5.4 150 FTG E FE 0.0 5A 0.0 0.0 65.2 0.0 0.022 TL 91.06 PV Pipe: 5A 56.7 1.995 FL 4.00 PF 0.3 5A 0.0 0.0 65.2 0.0 5.8 150 FTG E FE -1.7 6A 4.0 0.0 63.2 0.0 0.026 TL 10.36 PV Pipe: 5B 56.7 0.995 PL 1.00 PF 8.4 6A 4.0 0.0 63.2 0.0 23.4 150 FTG 10.0 PE -0.4 BOR 5.0 0.0 54.4 0.0 0.767 TL 11.00 PV Pipe: 6 56.7 1.101 PL 9.00 PF 8.9 BOR 5.0 0.0 54.4 0.0 19.1 150 FTG 10.0 PE -3.9 TOR 14.0 0.0 41.6 0.0 0.468 TL 19.00 PV Pipe: 7 56.7 1.101 PL 11.85 PF 12.6 TOR 14.0 0.0 41.6 0.0 19.1 150 FTG 15.0 FE 0.0 6 14.0 0.0 29.0 0.0 0.468 TL 26.85 PV Pipe: 8 42.5 1.101 FL 6.00 PF 3.0 6 14.0 0.0 29.0 0.0 14.3 150 FTG 5.0 FE 0.0 7 14.0 0.0 26.0 0.0 0.274 TL 11.00 PV Pipe: 9 18.1 1.101 FL 14.50 PF 1.4 7 14.0 0.0 26.0 0.0 6.1 150 FTG 11.0 FE 0.0 8 14.0 0.0 24.5 0.0 0.056 TL 25.50 PV Pipe: 10 8.4 1.101 FL 170.12 PF 2.8 8 14.0 0.0 24.5 0.0 2.8 150 FTG 37.0 FE 0.0 9 14.0 0.0 21.7 0.0 0.014 TL 207.12 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 1/2/2007 C:\HASS78\061445DF.SDF JOB TITLE: Hunters Point Building Type I Caic. 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: 11 -2.8 1.101 PL 0.58 PP 0.0 9 14.0 0.0 21.7 0.0 0.9 150 FTG 5.0 PE 0.0 10 14.0 0.0 21.7 0.0 0.002 TL 5.58 PV Pipe: 12 -2.8 1.101 PL 24.50 PF 0.1 10 14.0 0.0 21.7 0.0 0.9 150 FTG 7.0 PE 0.0 11 14.0 0.0 21.8 0.0 0.002 TL 31.50 PV Pipe: 13 -2.8 1.101 PL 0.58 PP 0.0 11 14.0 0.0 21.8 0.0 0.9 150 FTG 5.0 PE 0.0 12 14.0 0.0 21.8 0.0 0.002 TL 5.58 PV Pipe: 14 -14.2 1.101 PL 165.20 PF 7.2 12 14.0 0.0 21.8 0.0 4.8 150 FTG 33.0 PE 0.0 6 14.0 0.0 29.0 0.0 0.036 TL 198.20 PV Pipe: 15 24.4 1.101 PL 10.00 PF 1.5 7 14.0 0.0 26.0 0.0 8.2 150 FTG 5.0 PE -4.3 20 24.0 0.0 20.2 0.0 0.098 TL 15.00 PV Pipe: 16 9.7 1.101 PL 10.00 PF 0.3 8 14.0 0.0 24.5 0.0 3.3 150 FTG 5.0 PE -4.3 21 24.0 0.0 19.9 0.0 0.018 TL 15.00 PV Pipe: 17 11.1 1.101 PL 10.00 PF 0.3 9 14.0 0.0 21.7 0.0 3.8 150 FTG 5.0 PE -4.3 26 24.0 0.0 17.0 0.0 0.023 TL 15.00 PV Pipe: 18 11.5 1.101 PL 10.00 PF 0.4 12 14.0 0.0 21.8 0.0 3.9 150 FTG 5.0 PE -4.3 29 24.0 0.0 17.1 0.0 0.024 TL 15.00 PV Pipe: 19 7.4 1.101 PL 14.50 PP 0.2 20 24.0 0.0 20.2 0.0 2.5 150 FTG 7.0 PE 0.0 21 24.0 0.0 19.9 0.0 0.011 TL 21.50 PV Pipe: 20 17.2 1.101 PL 52.67 PP 3.5 21 24.0 0.0 19.9 0.0 5.8 150 FTG 15.0 PE 0.0 22 24.0 0.0 16.5 0.0 0.051 TL 67.67 PV Pipe: 21 10.0 1.101 PL 2.00 PP 0.1 22 24.0 0.0 16.5 0.0 3.4 150 FTG 5.0 PE 0.0 23 24.0 0.0 16.3 0.0 0.019 TL 7.00 PV Pipe: 22 7.2 1.101 PL 79.00 PP 1.0 22 24.0 0.0 16.5 0.0 2.4 150 FTG 21.0 PE 0.0 24 24.0 0.0 15.5 0.0 0.010 TL 100.00 PV Pipe: 23 20.6 1.101 PL 2.00 PP 0.5 24 24.0 0.0 15.5 0.0 6.9 150 FTG 5.0 PE 0.0 25 24.0 0.0 14.9 0.0 0.072 TL 7.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 1/2/2007 C:\HASS78\06-1445DF.SDF JOB TITLE: Hunters Point Building Type I Calc. 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: 24 -13.4 1.101 PL 38.92 RE' 1.6 24 24.0 0.0 15.5 0.0 4.5 150 FTG 10.0 PE 0.0 26 24.0 0.0 17.0 0.0 0.033 TL 48.92 PV Pipe: 25 -2.3 1.101 PL 0.58 PF 0.0 26 24.0 0.0 17.0 0.0 0.8 150 FTG 5.0 PE 0.0 27 24.0 0.0 17.1 0.0 0.001 TL 5.58 PV Pipe: 26 -2.3 1.101 PL 24.50 PF 0.0 27 24.0 0.0 17.1 0.0 0.8 150 FTG 7.0 PE 0.0 28 24.0 0.0 17.1 0.0 0.001 TL 31.50 PV Pipe: 27 -2.3 1.101 PL 0.58 PF 0.0 28 24.0 0.0 17.1 0.0 0.8 150 FTG 5.0 PE 0.0 29 24.0 0.0 17.1 0.0 0.001 TL 5.58 PV Pipe: 28 9.2 1.101 PL 38.92 PF 1.0 29 24.0 0.0 17.1 0.0 3.1 150 FTG 21.0 PE 0.0 30 24.0 0.0 16.1 0.0 0.016 TL 59.92 PV Pipe: 29 14.8 1.101 PL 2.00 PF 0.3 30 24.0 0.0 16.1 0.0 5.0 150 FTG 5.0 PE 0.0 31 24.0 0.0 15.9 0.0 0.039 TL 7.00 PV Pipe: 30 -5.6 1.101 PL 79.00 PF 0.6 30 24.0 0.0 16.1 0.0 1.9 150 FTG 21.0 PE 0.0 32 24.0 0.0 16.8 0.0 0.006 TL 100.00 PV Pipe: 31 11.3 1.101 PL 2.00 PF 0.2 32 24.0 0.0 16.8 0.0 3.8 150 FTG 5.0 PE 0.0 33 24.0 0.0 16.6 0.0 0.024 TL 7.00 PV Pipe: 32 -17.0 1.101 PL 52.67 PF 3.4 32 24.0 0.0 16.8 0.0 5.7 150 FTG 15.0 PE 0.0 20 24.0 0.0 20.2 0.0 0.050 TL 67.67 PV Pipe: 33 10.0 1.101 PL 10.00 PF 0.3 23 24.0 0.0 16.3 0.0 3.4 150 FTG 7.0 PE -4.3 43 34.0 0.0 11.7 0.0 0.019 TL 17.00 PV Pipe: 34 11.3 1.101 PL 10.00 PF 0.4 33 24.0 0.0 16.6 0.0 3.8 150 FTG 7.0 PE -4.3 40 34.0 0.0 11.9 0.0 0.024 TL 17.00 PV Pipe: 35 20.6 1.101 PL 10.00 PF 1.2 25 24.0 0.0 14.9 0.0 6.9 150 FTG 7.0 PE -4.3 48 34.0 0.0 9.4 0.0 0.072 TL 17.00 PV Pipe: 36 14.8 1.101 PL 10.00 PF 0.7 31 24.0 0.0 15.9 0.0 5.0 150 FTG 7.0 PE -4.3 51 34.0 0.0 10.9 0.0 0.039 TL 17.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 1/2/2007 C:\HASS78\06-144SDF.SDF JOB TITLE: Hunters Point Building Type I Caic. PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FFS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 37 11.3 1.101 FL 2.75 FF 0.2 40 34.0 0.0 11.9 0.0 3.8 150 FTG 7.0 FE 0.0 41 34.0 0.0 11.6 0.0 0.024 TL 9.75 PV Pipe: 38 4.0 1.101 PL 20.25 PF 0.1 41 34.0 0.0 11.6 0.0 1.4 150 FTG 9.0 PE 0.0 42 34.0 0.0 11.5 0.0 0.004 TL 29.25 PV Pipe: 39 -10.0 1.101 FL 2.75 PP 0.1 42 34.0 0.0 11.5 0.0 3.4 150 FTG 5.0 FE 0.0 43 34.0 0.0 11.7 0.0 0.019 TL 7.75 PV Pipe: 40 14.0 1.101 FL 63.00 PP 3.0 42 34.0 0.0 11.5 0.0 4.7 150 FTG 21.0 FE 0.0 44 34.0 0.0 8.6 0.0 0.035 TL 84.00 PV Pipe: 41 14.2 1.101 FL 0.92 PP 0.2 44 34.0 0.0 8.6 0.0 4.8 150 FTG 5.0 FE 0.0 51 34.0 4.9 8.4 14.2 0.036 TL 5.92 PV Pipe: 42 -0.1 1.101 FL 12.83 PP 0.0 44 34.0 0.0 8.6 0.0 0.0 150 FTG 7.0 FE 0.0 45 34.0 0.0 8.6 0.0 0.000 TL 19.83 PV Pipe: 43 14.0 1.101 FL 6.67 PP 0.4 45 34.0 0.0 8.6 0.0 4.7 150 FTG 5.0 FE 0.0 S2 34.0 4.9 8.2 14.0 0.035 TL 11.67 PV Pipe: 44 -14.1 1.101 FL 2.25 PP 0.3 45 34.0 0.0 8.6 0.0 4.8 150 FTG 5.0 FE 0.0 46 34.0 0.0 8.8 0.0 0.036 TL 7.25 PV Pipe: 45 -20.6 1.101 FL 2.83 PP 0.6 46 34.0 0.0 8.8 0.0 6.9 150 FTG 5.0 FE 0.0 48 34.0 0.0 9.4 0.0 0.072 TL 7.83 PV Pipe: 46 6.5 1.101 FL 2.10 FP 0.1 46 34.0 0.0 8.8 0.0 2.2 150 FTG 5.0 FE 0.0 47 34.0 0.0 8.8 0.0 0.008 TL 7.10 PV Pipe: 47 14.3 1.101 FL 2.00 PP 0.3 47 34.0 0.0 8.8 0.0 4.8 150 FTG 5.0 FE 0.0 S3 34.0 4.9 8.5 14.3 0.037 TL 7.00 PV Pipe: 48 -7.8 1.101 FL 4.75 PP 0.1 47 34.0 0.0 8.8 0.0 2.6 150 FTG 5.0 FE 0.0 49 34.0 0.0 8.9 0.0 0.012 TL 9.75 PV Pipe: 49 14.3 1.101 FL 6.38 PP 0.4 49 34.0 0.0 8.9 0.0 4.8 150 FTG 5.0 FE 0.0 S4 34.0 4.9 8.5 14.3 0.036 TL 11.38 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 1/2/2007 C:\HASS78\06-144SDF.SDF JOB TITLE: Hunters Point Building Type I Calc. 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: 50 -22.1 1.101 PL 13.37 PF 1.7 49 34.0 0.0 8.9 0.0 7.4 150 FTG 7.0 PE 0.0 50 34.0 0.0 10.6 0.0 0.082 TL 20.37 PV Pipe: 51 -14.8 1.101 PL 2.75 PF 0.3 50 34.0 0.0 10.6 0.0 5.0 150 FTG 5.0 PE 0.0 51 34.0 0.0 10.9 0.0 0.039 TL 7.75 PV Pipe: 52 -7.3 1.101 PL 78.00 PF 1.1 50 34.0 0.0 10.6 0.0 2.5 150 FTG 25.0 PE 0.0 41 34.0 0.0 11.6 0.0 0.011 TL 103.00 PV NOTES: Calculations were performed by the HASS 7.8 computer program under license no. 27091255 granted by HRS Systems, Inc. 4792 LaVista Road Tucker, GA 30084 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 0.052 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 23.4 ft/sec at pipe 5B. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: * 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 1.101 2.53 6.33 2.53 6.33 7.59 1.27 12.66 12.66 6.33 1.995 4.21 8.41 2.52 9.26 5.05 0.84 8.41 8.41 8.41 6.340 17.37 37.23 11.17 39.71 12.41 3.72 34.75 34.75 37.23 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 1/2/2007 :\HAS5/\0b-5U1f.IJt JOB TITLE: Hunters Point Building Type I Cab. PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEil ChkVlv BfyVlv GatVlv AlmChk DPViv NPTee 2.067 5.00 10.00 3.00 11.00 6.00 1.00 10.00 10.00 10.00 3.068 7.00 15.00 5.00 16.00 10.00 1.00 13.00 13.00 15.00 PAGE: K MATERIAL: CT-K HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E .T F R C S G N Ell Tee 45-Ell TeeRun Coupig SwgChk GatVlv NPTee 0.995 2.00 6.00 1.00 2.00 0.50 6.00 1.00 6.00 1 G 80.0 A 2 U G E P 60.0 R E S S 40.0 p 5 i 20.0 0.0 -14.7 WATER SUPPLY ANALYSIS Static: 94.50 psi Resid: 89.10 psi Flow: 1500.0 gpm LEGEND Available pressure 94.49 psi @ 56.7 gpm -Required pressure 2 75.32 psi @ 56.7 gpm Source Supply Curve System Demand Curve U) '-C Co U) co Co C C C) z I-H CoU) U) co -1 aD aD U) UQ U) (0 C aD 400 600 800 1000 1200 1400 1600 LIIsIS FLOW (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 DATE: 1/2/2007 C:\HASS78\06-144SDF.SDF JOB TITLE: Hunters Point Building Type I Caic. WATER SUPPLY CURVE 96+ 0\\\\\\\\\\\\\\\\\\ I \\\\\\\\\\\\\\\\\\\ I * <-89.1 psi @ 1500 gpm 88+ Flow Test Point 80+ x 72+ P 64+ R I E I S I 5 56+ U I R E I 48+ P I S I I 40+ 32+ 24+ 16+ LEGEND I, I X = Required Water Supply I 75.32 psi @ 56.7 gpm 8+ I 0 = Available Water Supply I 94.49 psi @ 56.7 gpm 0++-+---+----+-----+ ------+ --------+ --------+ ---------+ -----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) SOUTHLAND FIRE PROTECTION, INC. 4733 POINT LOMA AVENUE SAN DIEGO,CA 92107 HYDRAULIC CALCULATIONS FOR Hunter's Pointe Building Type 2 Caic. Family Apartments Carlsbad, CA FILE NUMBER: 06-144 DATE: JAN 3, 2007 -DESIGN DATA- OCCUPANCY CLASSIFICATION: DENSITY: AREA OF APPLICATION: COVERAGE PER SPRINKLER: NUMBER OF SPRINKLERS CALCULATED: TOTAL SPRINKLER WATER FLOW REQUIRED: TOTAL WATER REQUIRED (including hose) FLOW AND PRESSURE (@ BOR) SPRINKLER ORIFICE SIZE: NAME OF CONTRACTOR: DESIGN/LAYOUT BY: AUTHORITY HAVING JURISDICTION: CONTRACTOR CERTIFICATION NUMBER: R-3 .05 gpm/sq. ft. Remote Area 2 256 sq. ft. 4 sprinklers 59.6 gpm 59.6 gpm 59.6 gpm @ 58.7 psi 1/2 inch Southland Fire Protection, Inc. Sorida Phan Carlsbad Fire Department C-16 611956 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE # 27091255 HRS SYSTEMS, INC. TUCKER, GA 30084 APPROVED , ftJBMITTED CBAD FIRE DEPARTMENT SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 * DATE: 1/3/2007 C:\HASS78\061442.SDF - JOB TITLE: Hunters Pointe Building Type 2 Calc. WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) 1 94.5 89.1 1500.0 94.5 59.6 76.5 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 59.6 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 59.6 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 0.0 SOURCE 76.5 59.6 2 0.0 - - - - 76.5 - - - 3 3.0 - - - - 75.1 - - - 4 3.0 - - - - 67.1 5 0.0 - - - - 68.4 - - - 5A 0.0 - - - - 66.2 - - - 6A 4.0 - - - - 64.2 BOR 5.0 - - - - 58.7 - - - TOR 14.0 - - - - 45.1 - - - 6 14.0 - - - - 30.8 7 14.0 - - - - 27.4 - - - 8 14.0 - - - - 27.1 - - - 9 14.0 - - - - 26.4 - - - 10 14.0 - - - - 26.3 - - - 11 14.0 - - - - 25.7 - - - 12 14.0 - - - - 26.3 - - - 20 24.0 - - - - 22.3 21 24.0 - - - - 22.0 - - - 22 24.0 - - - - 21.8 - - - 23 24.0 - - - - 21.9 - - - 24 24.0 - - - - 21.2 - - - 25 24.0 - - - - 20.9 - - - 26 24.0 - - - - 21.2 - - - 27 24.0 - - - - 21.5 28 24.0 - - - - 21.5 - - - 29 24.0 - - - - 21.4 - - - 40 34.0 - - - - 16.9 - - - 41 34.0 - - - - 16.8 - - - 42 34.0 - - - - 16.1 - - - 43 34.0 - - - - 16.3 - - - 44 34.0 - - - - 10.0 - - - 45 34.0 - - - - 8.8 - - - 46 34.0 - - - - 11.2 - - - 47 34.0 - - - - 16.6 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 1/3/2007 C:\HASS78\06-144-2.SDF JOB TITLE: Hunters Pointe Building Type 2 Caic. NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 48 34.0 - - - - 17.1 - - - Si 34.0 K= 4.90 9.5 15.1 S2 34.0 K= 4.90 8.5 14.3 S3 34.0 K= 4.90 8.2 14.0 S4 34.0 K= 4.90 10.9 16.2 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 1/3/2007 C:\HASS78\06-144-2.SDF JOB TITLE: Hunters Pointe Building Type 2 Calc. 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 59.6 6.340 PL 22.50 PF 0.0 1 0.0 SRCE 76.5 (N/A) 0.6 140 FTG ETG PE 0.0 2 0.0 0.0 76.5 0.0 0.000 TL 100.08 PV Pipe: 2 59.6 3.068 PL 4.00 PF 0.1 2 0.0 0.0 76.5 0.0 2.6 140 FTG E PE -1.3 3 3.0 0.0 75.1 0.0 0.004 TL 13.31 PV Pipe: 3 FIXED PRESSURE LOSS DEVICE 3 3.0 0.0 75.1 0.0 8.0 psi, 59.6 gpm 4 3.0 0.0 67.1 0.0 Pipe: 4 59.6 3.068 PL 4.00 PF 0.1 4 3.0 0.0 67.1 0.0 2.6 140 FTG E PE 1.3 5 0.0 0.0 68.4 0.0 0.004 TL 13.31 PV Pipe: 5 59.6 2.067 PL 83.50 PF 2.2 5 0.0 0.0 68.4 0.0 5.7 150 FTG E PE 0.0 5A 0.0 0.0 66.2 0.0 0.024 TL 91.06 PV Pipe: 5A 59.6 1.995 PL 4.00 PF 0.3 5A 0.0 0.0 66.2 0.0 6.1 150 FTG E PE -1.7 6A 4.0 0.0 64.2 0.0 0.028 TL 10.36 PV Pipe: 6 59.6 0.995 PL 4.00 PF 5.0 6A 4.0 0.0 64.2 0.0 24.6 150 FTG E PE -0.4 BOR 5.0 0.0 58.7 0.0 0.839 TL 6.00 PV Pipe: 6A 59.6 1.101 PL 9.00 PF 9.7 BOR 5.0 0.0 58.7 0.0 20.1 150 FTG 10.0 PE -3.9 TOR 14.0 0.0 45.1 0.0 0.512 TL 19.00 PV Pipe: 7 59.6 1.101 PL 12.83 PF 14.3 TOR 14.0 0.0 45.1 0.0 20.1 150 FTG 15.0 PE 0.0 6 14.0 0.0 30.8 0.0 0.512 TL 27.83 PV Pipe: 8 24.4 1.101 PL 25.20 PF 3.5 6 14.0 0.0 30.8 0.0 8.2 150 FTG 10.0 PE 0.0 7 14.0 0.0 27.4 0.0 0.098 TL 35.20 PV Pipe: 9 17.6 1.101 PL 66.30 PF 4.5 6 14.0 0.0 30.8 0.0 5.9 150 FTG 18.0 PE 0.0 12 14.0 0.0 26.3 0.0 0.054 TL 84.30 PV Pipe: 10 13.2 1.101 PL 2.67 PF 0.2 7 14.0 0.0 27.4 0.0 4.4 150 FTG 5.0 PE 0.0 8 14.0 0.0 27.1 0.0 0.031 TL 7.67 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 1/3/2007 C:\HASS78\06-144-2.SDF JOB TITLE: Hunters Pointe Building Type 2 Caic. 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: 11 11.2 1.101 PL 29.15 PF 1.0 7 14.0 0.0 27.4 0.0 3.8 150 FTG 12.0 PE 0.0 9 14.0 0.0 26.4 0.0 0.023 TL 41.15 PV Pipe: 12 5.8 1.101 PL 2.67 PF 0.1 9 14.0 0.0 26.4 0.0 2.0 150 FTG 5.0 PE 0.0 10 14.0 0.0 26.3 0.0 0.007 TL 7.67 PV Pipe: 13 5.4 1.101 PL 93.50 PF 0.7 9 14.0 0.0 26.4 0.0 1.8 150 FTG 23.0 PE 0.0 11 14.0 0.0 25.7 0.0 0.006 TL 116.50 PV Pipe: 14 -11.9 1.101 PL 14.50 PF 0.6 11 14.0 0.0 25.7 0.0 4.0 150 FTG 8.0 PE 0.0 12 14.0 0.0 26.3 0.0 0.026 TL 22.50 PV Pipe: 15 -17.6 1.101 PL 66.25 PF 4.5 12 14.0 0.0 26.3 0.0 5.9 150 FTG 18.0 PE 0.0 6 14.0 0.0 30.8 0.0 0.054 TL 84.25 PV Pipe: 16 13.2 1.101 PL 10.00 PF 0.5 8 14.0 0.0 27.1 0.0 4.4 150 FTG 7.0 PE -4.3 20 24.0 0.0 22.3 0.0 0.031 TL 17.00 PV Pipe: 17 5.8 1.101 PL 10.00 PF 0.1 10 14.0 0.0 26.3 0.0 2.0 150 FTG 7.0 PE -4.3 23 24.0 0.0 21.9 0.0 0.007 TL 17.00 PV Pipe: 18 8.3 1.101 PL 10.00 PF 0.2 11 14.0 0.0 25.7 0.0 2.8 150 FTG 5.0 PE -4.3 26 24.0 0.0 21.2 0.0 0.013 TL 15.00 PV Pipe: 19 13.2 1.101 PL 10.00 PF 0.5 12 14.0 0.0 26.3 0.0 4.4 150 FTG 5.0 FE -4.3 27 24.0 0.0 21.5 0.0 0.032 TL 15.00 PV Pipe: 20 13.2 1.101 PL 2.20 PF 0.3 20 24.0 0.0 22.3 0.0 4.4 150 FTG 7.0 FE 0.0 21 24.0 0.0 22.0 0.0 0.031 TL 9.20 PV Pipe: 21 4.7 1.101 PL 19.30 PF 0.1 21 24.0 0.0 22.0 0.0 1.6 150 FTG 6.0 PE 0.0 22 24.0 0.0 21.8 0.0 0.005 TL 25.30 PV Pipe: 22 5.8 1.101 PL 2.20 PF 0.1 23 24.0 0.0 21.9 0.0 2.0 150 FTG 5.0 FE 0.0 22 24.0 0.0 21.8 0.0 0.007 TL 7.20 PV Pipe: 23 10.5 1.101 PL 21.00 PF 0.7 22 24.0 0.0 21.8 0.0 3.5 150 FTG 12.0 PE 0.0 24 24.0 0.0 21.2 0.0 0.021 TL 33.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 1/3/2007 C:\HASS78\06-144-2.SDF JOB TITLE: Hunters Pointe Building Type 2 Calc. 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: 24 11.1 1.101 PL 5.00 PF 0.2 24 24.0 0.0 21.2 0.0 3.7 150 FTG 5.0 PE 0.0 25 24.0 0.0 20.9 0.0 0.023 TL 10.00 PV Pipe: 25 -0.6 1.101 FL 77.30 PF 0.0 24 24.0 0.0 21.2 0.0 0.2 150 FTG 20.0 PE 0.0 26 24.0 0.0 21.2 0.0 0.000 TL 97.30 PV Pipe: 26 -8.8 1.101 PL 14.50 PF 0.3 26 24.0 0.0 21.2 0.0 2.9 150 FTG 7.0 PE 0.0 27 24.0 0.0 21.5 0.0 0.015 TL 21.50 PV Pipe: 27 -0.7 1.101 PL 77.30 PF 0.0 27 24.0 0.0 21.5 0.0 0.2 150 FTG 20.0 PE 0.0 28 24.0 0.0 21.5 0.0 0.000 TL 97.30 PV Pipe: 28 7.8 1.101 PL 5.00 PF 0.1 28 24.0 0.0 21.5 0.0 2.6 150 FTG 5.0 PE 0.0 29 24.0 0.0 21.4 0.0 0.012 TL 10.00 PV Pipe: 29 -8.5 1.101 FL 21.00 PF 0.5 28 24.0 0.0 21.5 0.0 2.9 150 FTG 12.0 FE 0.0 21 24.0 0.0 22.0 0.0 0.014 TL 33.00 PV Pipe: 30 7.8 1.101 PL 10.00 PF 0.2 29 24.0 0.0 21.4 0.0 2.6 150 FTG 5.0 FE -4.3 40 34.0 0.0 16.9 0.0 0.012 TL 15.00 PV Pipe: 31 11.1 1.101 PL 10.00 FE' 0.3 25 24.0 0.0 20.9 0.0 3.7 150 FTG 5.0 FE -4.3 43 34.0 0.0 16.3 0.0 0.023 TL 15.00 PV Pipe: 32 8.2 1.101 FL 10.00 FE' 0.2 26 24.0 0.0 21.2 0.0 2.8 150 FTG 5.0 FE -4.3 47 34.0 0.0 16.6 0.0 0.013 TL 15.00 FV Pipe: 32A 2.6 1.101 FL 10.00 PF 0.0 27 24.0 0.0 21.5 0.0 0.9 150 FTG 5.0 FE -4.3 48 34.0 0.0 17.1 0.0 0.002 TL 15.00 PV Pipe: 33 7.8 1.101 FL 1.83 PF 0.1 40 34.0 0.0 16.9 0.0 2.6 150 FTG 7.0 FE 0.0 41 34.0 0.0 16.8 0.0 0.012 TL 8.83 PV Pipe: 34 11.9 1.101 FL 18.50 FE' 0.7 41 34.0 0.0 16.8 0.0 4.0 150 FTG 7.0 FE 0.0 42 34.0 0.0 16.1 0.0 0.026 TL 25.50 PV Pipe: 35 11.1 1.101 FL 1.83 FE' 0.2 43 34.0 0.0 16.3 0.0 3.7 150 FTG 5.0 FE 0.0 42 34.0 0.0 16.1 0.0 0.023 TL 6.83 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 1/3/2007 C:\HASS78\06-144-2.SDF JOB TITLE: Hunters Pointe Building Type 2 Cab. 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: 36 23.0 1.101 PL 53.50 PF 6.1 42 34.0 0.0 16.1 0.0 7.8 150 FTG 16.0 PE 0.0 44 34.0 0.0 10.0 0.0 0.088 TL 69.50 PV Pipe: 37 15.1 1.101 PL 6.67 PF 0.5 44 34.0 0.0 10.0 0.0 5.1 150 FTG 5.0 PE 0.0 51 34.0 4.9 9.5 15.1 0.040 TL 11.67 PV Pipe: 38 28.3 1.101 PL 4.30 PF 1.2 44 34.0 0.0 10.0 0.0 9.5 150 FTG 5.0 PE 0.0 45 34.0 0.0 8.8 0.0 0.129 TL 9.30 PV Pipe: 39 14.3 1.101 PL 1.58 PF 0.2 45 34.0 0.0 8.8 0.0 4.8 150 FTG 5.0 PE 0.0 S2 34.0 4.9 8.5 14.3 0.037 TL 6.58 PV Pipe: 40 14.0 1.101 PL 4.83 PF 0.6 45 34.0 0.0 8.8 0.0 4.7 150 FTG 12.0 PE 0.0 S3 34.0 4.9 8.2 14.0 0.035 TL 16.83 PV Pipe: 41 -20.4 1.101 PL 11.50 PF 1.2 44 34.0 0.0 10.0 0.0 6.9 150 FTG 6.0 PE 0.0 46 34.0 0.0 11.2 0.0 0.070 TL 17.50 PV Pipe: 42 16.2 1.101 FL 1.00 PF 0.3 46 34.0 0.0 11.2 0.0 5.5 150 FTG 5.0 PE 0.0 S4 34.0 4.9 10.9 16.2 0.046 TL 6.00 PV Pipe: 43 -36.5 1.101 PL 15.30 PF 5.5 46 34.0 0.0 11.2 0.0 12.3 150 FTG 11.0 PE 0.0 47 34.0 0.0 16.6 0.0 0.207 TL 26.30 PV Pipe: 44 -11.1 1.101 PL 14.50 PF 0.5 47 34.0 0.0 16.6 0.0 3.7 150 FTG 7.0 FE 0.0 48 34.0 0.0 17.1 0.0 0.023 TL 21.50 PV Pipe: 45 4.1 1.101 FL 80.30 PF 0.4 48 34.0 0.0 17.1 0.0 1.4 150 FTG 22.0 FE 0.0 41 34.0 0.0 16.8 0.0 0.004 TL 102.30 PV Pipe: 46 -8.2 1.101 FL 10.00 PF 0.2 47 34.0 0.0 16.6 0.0 2.8 150 FTG 5.0 FE 4.3 26 24.0 0.0 21.2 0.0 0.013 TL 15.00 PV Pipe: 47 -9.0 1.101 FL 20.00 PF 0.4 47 34.0 0.0 16.6 0.0 3.0 150 FTG 6.0 FE 8.7 11 14.0 0.0 25.7 0.0 0.015 TL 26.00 PV Pipe: 48 -2.6 1.101 FL 10.00 FE' 0.0 48 34.0 0.0 17.1 0.0 0.9 150 FTG 5.0 FE 4.3 27 24.0 0.0 21.5 0.0 0.002 TL 15.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 1/3/2007 C:\HASS78\06-144-2.SDF JOB TITLE: Hunters Pointe Building Type 2 Caic. 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: 49 -10.1 1.101 PL 20.00 PF 0.5 48 34.0 0.0 17.1 0.0 3.4 150 FTG 6.0 PE 8.7 12 14.0 0.0 26.3 0.0 0.019 TL 26.00 PV NOTES: Calculations were performed by the HASS 7.8 computer program under license no. 27091255 granted by HRS Systems, Inc. 4792 LaVista Road Tucker, GA 30084 The system has been calculated to provide an average imbalance at each node of 0.002 gpm and a maximum imbalance at any node of 0.091 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 24.6 ft/sec at pipe 6. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: * MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngE1l ChkVlv BfyVlv GatVlv AlmChk DPVlv NPTee 1.101 2.53 6.33 2.53 6.33 7.59 1.27 12.66 12.66 6.33 1.995 4.21 8.41 2.52 9.26 5.05 0.84 8.41 8.41 8.41 6.340 17.37 37.23 11.17 39.71 12.41 3.72 34.75 34.75 37.23 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 DPViv NPTee 2.067 5.00 10.00 3.00 11.00 6.00 1.00 10.00 10.00 10.00 3.068 7.00 15.00 5.00 16.00 10.00 1.00 13.00 13.00 15.00 PAGE: K MATERIAL: CT-K HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R C S G N Ell Tee 45-Eli TeeRun Coupig SwgChk GatVlv NPTee 0.995 2.00 6.00 1.00 2.00 0.50 6.00 1.00 6.00 100.0 1 G 80.0 A 2 U G E WATER SUPPLY ANALYSIS Static: 94.50 psi Resid: 89.10 psi Flow: 1500.0 qpm LEGEND Available pressure 94.49 psi @ 59.6 gpm -Required pressure 2 76.50 psi @ 59.6 gpm Source Supply curve System Demand Curve 60.0 R E S S 40.0 p S i 20.0 0.0 -14.7 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 1/3/2007 C:\HASS78\06-144-2.SDF JOB TITLE: Hunters Pointe Building Type 2 Calc. WATER SUPPLY CURVE 96+ 0\\\\\\\\\\\\\\\\\\ I \\\\\\\\\\\\\\\\\\\ I * <-89.1 psi @ 1500 gpm 88+ Flow Test Point 80+ x 72+ P 64+ R I E I S S 56+ U I R I E I 48+ P S I I 40+ ) I 32+ 24+ 16+ LEGEND I X = Required Water Supply 76.50 psi @ 59.6 gpm 8+ I 0 = Available Water Supply I 94.49 psi @ 59.6 gpm 0++-+---+----+-----+ ------+ --------+ --------+ ---------+ -----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) SOUTHLAND FIRE PROTECTION, INC. 4733 POINT LOMA AVENUE SAN DIEGO,CA 92107 HYDRAULIC CALCULATIONS FOR Hunter's Pointe Building Type 3 Parking Garage Calc Carlsbad, Ca. FILE NUMBER: 06-144 DATE: JAN 3, 2007 -DESIGN DATA- OCCUPANCY CLASSIFICATION: S-3 DENSITY: .15 gpm/sq. ft. AREA OF APPLICATION: Remote Area 4 COVERAGE PER SPRINKLER: 324 sq. ft. NUMBER OF SPRINKLERS CALCULATED: 6 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 298.2 gpm TOTAL WATER REQUIRED (including hose): 548.2 gpm FLOW AND PRESSURE (@ BOR) : 298.2 gpm @ 64.9 psi SPRINKLER ORIFICE SIZE: 3/4 inch NAME OF CONTRACTOR: Southland Fire Protection, Inc. DESIGN/LAYOUT BY: Sorida Phan AUTHORITY HAVING JURISDICTION Carlsbad Fire Department CONTRACTOR CERTIFICATION NUMBER: C-16 611956 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE # 27091255 HRS SYSTEMS, INC. TUCKER, GA 30084 APPROVED AWSAIWITTED CARLSBAD FIR D PARTMENT SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 1/3/2007 C:\HASS78\06-144-P.SDF JOB TITLE: Hunter's Pointe Garage Parking WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQD NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) 1 94.5 89.1 1500.0 93.7 548.2 72.5 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 548.2 GPM TOTAL'HOSE STREAM ALLOWANCE AT SOURCE 250.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 298.2 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 0.0 SOURCE 72.5 298.2 2 0.0 - - - - 72.3 3 3.0 - - - - 70.7 - - - 4 3.0 - - - - 67.7 - - - 5 3.0 - - - - 67.4 - - - 5A -6.0 - - - - 70.9 - - - 6A -7.0 - - - - 68.7 BOR -4.0 - - - - 64.9 - - - TOR 3.0 - - - - 55.9 - - - 6 3.0 - - - - 44.2 - - - 7 3.0 - - - - 42.1 - - - 10 3.0 - - - - 40.7 - - - 13 3.0 - - - - 40.4 - - - 14 3.0 - - - - 24.4 - - - 15 3.0 - - - - 24.2 - - - 16 3.0 - - - - 23.6 - - - 17 3.0 - - - - 23.4 - - - Si 3.0 K=11.20 20.7 50.9 S2 3.0 K=11.20 19.3 49.2 S3 3.0 K=11.20 19.3 49.3 S4 3.0 K=11.20 20.5 50.7 S5 3.0 K=11.20 19.1 49.0 S6 3.0 K=11.20 19.2 49.1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 1/3/2007 C:\HASS78\06-144-P.SDF JOB TITLE: Hunter's Pointe Garage Parking PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (PT) SUM. NODES (PT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 1 298.2 6.340 PL 11.20 PF 0.2 1 0.0 SRCE 72.5 (N/A) 3.0 140 FTG ETG PE 0.0 2 0.0 0.0 72.3 0.0 0.002 TL 88.78 PV Pipe: 2 298.2 4.280 PL 4.00 PP 0.3 2 0.0 0.0 72.3 0.0 6.6 140 FTG E PE -1.3 3 3.0 0.0 70.7 0.0 0.015 TL 21.92 PV Pipe: 3 FIXED PRESSURE LOSS DEVICE 3 3.0 0.0 70.7 0.0 3.0 psi, 298.2 gpm 4 3.0 0.0 67.7 0.0 Pipe: 4 298.2 4.280 PL 4.00 PF 0.3 4 3.0 0.0 67.7 0.0 6.6 140 FTG E PE 0.0 5 3.0 0.0 67.4 0.0 0.015 TL 21.92 PV Pipe: 5 298.2 4.280 PL 9.00 PP 0.4 5 3.0 0.0 67.4 0.0 6.6 140 FTG E PE 3.9 5A -6.0 0.0 70.9 0.0 0.015 TL 26.92 PV Pipe: 5A 298.2 2.703 PL 4.00 PP 2.6 5A -6.0 0.0 70.9 0.0 16.7 120 FTG E PE 0.4 6A -7.0 0.0 68.7 0.0 0.192 TL 13.33 PV Pipe: SB 298.2 2.703 PL 4.00 PP 2.6 6A -7.0 0.0 68.7 0.0 16.7 120 FTG E PE -1.3 BOR -4.0 0.0 64.9 0.0 0.192 TL 13.33 PV Pipe: 6 298.2 2.703 PL 9.00 PF 6.0 BOR -4.0 0.0 64.9 0.0 16.7 120 FTG 22.0 PE -3.0 TOR 3.0 0.0 55.9 0.0 0.192 TL 31.00 PV Pipe: 7 298.2 2.703 PL 39.83 PP 11.7 TOR 3.0 0.0 55.9 0.0 16.7 120 FTG 21.0 PE 0.0 6 3.0 0.0 44.2 0.0 0.192 TL 60.83 PV Pipe: 8 239.8 2.703 PL 16.00 PF 2.1 6 3.0 0.0 44.2 0.0 13.4 120 FTG ---- PE 0.0 7 3.0 0.0 42.1 0.0 0.128 TL 16.00 PV Pipe: 9 184.3 2.703 PL 17.75 PF 1.4 7 3.0 0.0 42.1 0.0 10.3 120 FTG ---- PE 0.0 10 3.0 0.0 40.7 0.0 0.079 TL 17.75 PV Pipe: 10 91.9 2.703 PL 16.00 PP 0.3 10 3.0 0.0 40.7 0.0 5.1 120 FTG ---- PE 0.0 13 3.0 0.0 40.4 0.0 0.022 TL 16.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 1/3/2007 C:\HASS78\06-144-P.SDF JOB TITLE: Hunter's Pointe Garage Parking 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: 11 58.4 1.536 PL 114.30 PF 19.8 6 3.0 0.0 44.2 0.0 10.1 120 FTG 20.0 PE 0.0 14 3.0 0.0 24.4 0.0 0.148 TL 134.30 PV Pipe: 12 58.4 2.703 PL 16.00 PF 0.2 14 3.0 0.0 24.4 0.0 3.3 120 FTG 6.0 PE 0.0 15 3.0 0.0 24.2 0.0 0.009 TL 22.00 PV Pipe: 13 113.9 2.703 PL 17.75 PF 0.6 15 3.0 0.0 24.2 0.0 6.4 120 FTG ---- PE 0.0 16 3.0 0.0 23.6 0.0 0.032 TL 17.75 PV Pipe: 14 56.9 2.703 PL 16.00 PF 0.1 16 3.0 0.0 23.6 0.0 3.2 120 FTG ---- PE 0.0 17 3.0 0.0 23.4 0.0 0.009 TL 16.00 PV Pipe: 15 55.4 1.536 PL 114.30 PF 18.0 7 3.0 0.0 42.1 0.0 9.6 120 FTG 20.0 PE 0.0 15 3.0 0.0 24.2 0.0 0.134 TL 134.30 PV Pipe: 16 92.4 1.536 PL 48.20 PF 20.1 10 3.0 0.0 40.7 0.0 16.0 120 FTG 10.0 PE 0.0 Si 3.0 11.2 20.7 50.9 0.345 TL 58.20 PV Pipe: 17 41.5 1.536 PL 18.00 PF 1.4 Si 3.0 11.2 20.7 50.9 7.2 120 FTG ---- PE 0.0 S2 3.0 11.2 19.3 49.2 0.078 TL 18.00 PV Pipe: 18 -7.7 1.536 PL 18.00 PF 0.1 S2 3.0 11.2 19.3 49.2 1.3 120 FTG ---- PE 0.0 S3 3.0 11.2 19.3 49.3 0.003 TL 18.00 PV Pipe: 19 -57.0 1.536 PL 30.20 PF 4.3 S3 3.0 11.2 19.3 49.3 9.9 120 FTG ---- PE 0.0 16 3.0 0.0 23.6 0.0 0.141 TL 30.20 PV Pipe: 20 91.9 1.536 PL 48.20 PF 19.9 13 3.0 0.0 40.4 0.0 15.9 120 FTG 10.0 PE 0.0 S4 3.0 11.2 20.5 50.7 0.341 TL 58.20 PV Pipe: 21 41.2 1.536 PL 18.00 PF 1.4 S4 3.0 11.2 20.5 50.7 7.1 120 FTG ---- PE 0.0 S5 3.0 11.2 19.1 49.0 0.077 TL 18.00 PV Pipe: 22 -7.8 1.536 PL 18.00 PF 0.1 S5 3.0 11.2 19.1 49.0 1.4 120 FTG ---- PE 0.0 S6 3.0 11.2 19.2 49.1 0.004 TL 18.00 PV Pipe: 23 -56.9 *1.536 PL 30.20 PF 4.2 S6 3.0 11.2 19.2 49.1 9.9 120 FTG ---- PE 0.0 17 3.0 0.0 23.4 0.0 0.141 TL 30.20 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 1/3/2007 C:\HASS78\06-144-P.SDF JOB TITLE: Hunter's Pointe Garage Parking NOTES: Calculations were performed by the HASS 7.8 computer program under license no. 27091255 granted by HRS Systems, Inc. 4792 LaVista Road Tucker, GA 30084 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 0.107 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 16.7 ft/sec at pipe 5A. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: * 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 1.536 3.18 6.36 1.59 7.16 4.77 0.80 7.95 7.95 6.36 2.703 9.33 18.65 6.22 21.76 10.88 1.55 15.54 15.54 18.65 4.280 13.47 26.94 8.08 29.64 16.17 2.69 26.94 26.94 26.94 6.340 17.37 37.23 11.17 39.71 12.41 3.72 34.75 34.75 37.23 100. 0 G 80.0 A U G E WATER SUPPLY ANALYSIS Static: 94.50 psi Resid: 89.10 psi Flow: 1500.0 qpm LEGEND Available pressure 93.66 psi 8 548.2 gpm Required pressure T 72.54 psi @ 548.2 gpm Source Supply curve System Demand curve 2 60.0 R E S S 40.0 P S i 20.0 0.0 -14.71 I I I I i I i I I 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 1/3/2007 C:\HASS78\06-144-P.SDF JOB TITLE: Hunter's Pointe Garage Parking WATER SUPPLY CURVE 96+ *\\\\\Q \\\\\\\\\\\\ \\\\\\\\\\\\\\\\\\\ * <-89.1 Psi @ 1500 gpm 88+ Flow Test Point 80+ 72+ x P 64+ R E S I S 56+ U I R E I 48+ P I S I 40+ 32+ 24+ 16+ LEGEND X = Required Water Supply I 72.54 psi @ 548.2 gpm " 8+ I 0 = Available Water Supply 93.66 psi @ 548.2 gpm 0++-+---+----+-----+ ------+ --------+--------+ ---------+ -----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) b SOUTHLAND FIRE PROTECTION, INC. 4733 POINT LOMA AVENUE SAN DIEGO,CA 92107 HYDRAULIC CALCULATIONS FOR Hunter's Pointe Family Apartments Community Building Carlsbad, Ca. FILE NUMBER: 06-144 DATE: JAN 3, 2007 -DESIGN DATA- OCCUPANCY CLASSIFICATION: DENSITY: AREA OF APPLICATION: COVERAGE PER SPRINKLER: NUMBER OF SPRINKLERS CALCULATED: TOTAL SPRINKLER WATER FLOW REQUIRED: TOTAL WATER REQUIRED (including hose) FLOW AND PRESSURE (@ BOR) SPRINKLER ORIFICE SIZE: NAME OF CONTRACTOR: DESIGN/LAYOUT BY: AUTHORITY HAVING JURISDICTION CONTRACTOR CERTIFICATION NUMBER: A3/B .10 gpm/sq. ft. Remote Area 1 1350 sq. ft. 12 sprinklers 207.4 gpm 307.5 gpm 207.5 gpm @ 48.5 psi 1/2 inch Southland Fire Protection, Inc. Sorida Phan Carlsbad Fire Department C-16- 611956 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE # 27091255 HRS SYSTEMS, INC. TUCKER, GA 30084 APPROVED AR5JITTED CARLSBAD FIRE DEPARTMENT - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 1/3/2007 C:\HASS78\06-144--CB.SDF JOB TITLE: Hunter's Pointe Community Building WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GEM) (PSI) (GPM) (PSI) 1 94.5 89.1 1500.0 94.2 307.5 77.9 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 307.5 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GEM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 207.5 GEM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GEM) 1 0.0 SOURCE 77.9 207.5 2 0.0 - - - - 77.8 - - - 3 3.0 - - - - 75.9 4 3.0 - - - - 66.9 5 3.0 - - - - 66.4 - - - 5A 0.0 - - - - 56.3 6A 3.0 - - - - 52.1 BOR 4.0 - - - - 48.5 - - - TOR 13.0 - - - - 38.3 6 13.0 - - - - 30.6 7 13.0 - - - - 25.6 8 13.0 - - - - 21.3 - - - 9 13.0 - - - - 16.7 - - - 10 13.0 - - - - 16.7 11 13.0 - - - - 21.5 - - - 20 13.0 - - - - 20.7 - - - 21 13.0 - - - - 16.2 - - - 21A 13.0 - - - - 13.0 - - - 22 13.0 - - - - 14.0 23 13.5 - - - - 12.4 24 13.0 - - - - 16.2 -. - - 25 13.0 - - - - 14.4 26 13.0 - - - - 11.3 - - 27 14.0 - - - - 9.7 - - - 28 14.0 - - - - 20.3 - - - 51 16.0 K= 5.60 10.1 17.8 S2 16.0 K= 5.60 10.5 18.1 S3 16.0 K= 5.60 9.0 16.8 S4 16.0 K= 5.60 7.9 15.7 S5 16.0 K= 5.60 8.2 16.0 S6 16.0 K= 5.60 7.0 14.8 S7 14.0 K= 5.60 9.7 17.5 S8 14.0 K= 5.60 10.1 17.8 S9 14.0 K= 5.60 8.5 16.3 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 1/3/2007 C:\HASS78\06-144-CB.SDF JOB TITLE: Hunter's Pointe Community Building NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE (FT) S10 14.0 K= 5.60 Sil 14.0 K= 5.60 S12 14.0 K= 5.60 PRESSURE DISCHARGE (PSI) (GPM) 11.3 18.8 11.6 19.1 11.1 18.7 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 1/3/2007 C:\HASS78\06-144-CB.SDF JOB TITLE: Hunter's Pointe Community Building 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: 1 207.5 6.340 PL 20.00 PF 0.1 1 0.0 SRCE 77.9 (N/A) 2.1 140 FTG ETG PE 0.0 2 0.0 0.0 77.8 0.0 0.001 TL 97.58 PV Pipe: 2 207.4 3.068 PL 4.00 PF 0.5 2 0.0 0.0 77.8 0.0 9.0 140 FTG E PE -1.3 3 3.0 0.0 75.9 0.0 0.040 TL 13.31 PV Pipe: 3 FIXED PRESSURE LOSS DEVICE 3 3.0 0.0 75.9 0.0 9.0 psi, 207.4 gpm 4 3.0 0.0 66.9 0.0 Pipe: 4 207.4 3.068 PL 4.00 PF 0.5 4 3.0 0.0 66.9 0.0 9.0 140 FTG E PE 0.0 5 3.0 0.0 66.4 0.0 0.040 TL 13.31 PV Pipe: 5 207.4 2.067 PL 40.00 PF 11.4 5 3.0 0.0 66.4 0.0 19.8 150 FTG E PE 1.3 5A 0.0 0.0 56.3 0.0 0.240 TL 47.56 PV Pipe: 5A 207.4 1.995 PL 4.00 PF 3.0 5A 0.0 0.0 56.3 0.0 21.3 150 FTG E PE -1.3 6A 3.0 0.0 52.1 0.0 0.285 TL 10.36 PV Pipe: 5B 207.4 1.995 PL 1.00 PF 3.1 6A 3.0 0.0 52.1 0.0 21.3 150 FTG 10.0 PE -0.4 BOR 4.0 0.0 48.5 0.0 0.285 TL 11.00 PV Pipe: 6 207.4 2.104 PL 9.00 PF 6.3 BOR 4.0 0.0 48.5 0.0 19.1 120 FTG 10.0 PE -3.9 TOR 13.0 0.0 38.3 0.0 0.332 TL 19.00 PV Pipe: 7 207.4 2.067 PL 8.25 PF 7.7 TOR 13.0 0.0 38.3 0.0 19.8 120 FTG 13.0 PE 0.0 6 13.0 0.0 30.6 0.0 0.362 TL 21.25 PV Pipe: 8 107.0 1.639 PL' 7.00 PF 4.9 6 13.0 0.0 30.6 0.0 16.3 120 FTG 8.0 PE 0.0 7 13.0 0.0 25.6 0.0 0.330 TL 15.00 PV Pipe: 9 107.0 1.639 PL 5.00 PF 4.3 7 13.0 0.0 25.6 0.0 16.3 120 FTG 8.0 PE 0.0 8 13.0 0.0 21.3 0.0 0.330 TL 13.00 PV Pipe: 10 50.7 1.639 PL 47.10 PF 4.6 8 13.0 0.0 21.3 0.0 7.7 120 FTG 9.0 PE 0.0 9 13.0 0.0 16.7 0.0 0.083 TL 56.10 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 1/3/2007 C:\HASS78\06-144-CB.SDF JOB TITLE: Hunter's Pointe Community Building 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: 11 -0.9 1.639 FL 35.00 PF 0.0 9 13.0 0.0 16.7 0.0 0.1 120 FTG 12.0 PE 0.0 10 13.0 0.0 16.7 0.0 0.000 TL 47.00 PV Pipe: 12 -51.6 1.639 PL 47.10 PF 4.8 10 13.0 0.0 16.7 0.0 7.8 120 FTG 9.0 PE 0.0 11 13.0 0.0 21.5 0.0 0.085 TL 56.10 PV Pipe: 13 -100.4 1.639 PL 23.00 PF 9.1 11 13.0 0.0 21.5 0.0 15.3 120 FTG 8.0 PE 0.0 6 13.0 0.0 30.6 0.0 0.293 TL 31.00 PV Pipe: 14 56.4 1.639 PL 1.00 PF 0.6 8 13.0 0.0 21.3 0.0 8.6 120 FTG 5.0 PE 0.0 20 13.0 0.0 20.7 0.0 0.101 TL 6.00 PV Pipe: 15 51.6 1.639 PL 1.00 PF 0.5 9 13.0 0.0 16.7 0.0 7.8 120 FTG 5.0 PE 0.0 21 13.0 0.0 16.2 0.0 0.085 TL 6.00 PV Pipe: 16 50.7 1.639 PL 1.00 PF 0.5 10 13.0 0.0 16.7 0.0 7.7 120 FTG 5.0 PE 0.0 24 13.0 0.0 16.2 0.0 0.083 TL 6.00 PV Pipe: 17 48.8 1.639 FL 1.00 PF 0.8 11 13.0 0.0 21.5 0.0 7.4 120 FTG 9.0 PE -0.4 28 14.0 0.0 20.3 0.0 0.077 TL 10.00 PV Pipe: 18 55.1 1.639 PL 47.10 PF 4.5 20 13.0 0.0 20.7 0.0 8.4 120 FTG ---- PE 0.0 21 13.0 0.0 16.2 0.0 0.096 TL 47.10 PV Pipe: 19 109.3 1.639 PL 1.00 PF 2.2 21 13.0 0.0 16.2 0.0 16.6 120 FTG 5.5 PE 0.0 22 13.0 0.0 14.0 0.0 0.343 TL 6.50 PV Pipe: 20 52.7 1.639 FL 6.15 PF 1.3 22 13.0 0.0 14.0 0.0 8.0 120 FTG 8.7 FE -0.2 23 13.5 0.0 12.4 0.0 0.089 TL 14.85 PV Pipe: 21 -2.6 1.639 FL 35.00 PF 0.0 21 13.0 0.0 16.2 0.0 0.4 120 FTG 18.0 PE 0.0 24 13.0 0.0 16.2 0.0 0.000 TL 53.00 PV Pipe: 22 17.8 1.080 FL 8.30 PF 1.2 23 13.5 0.0 12.4 0.0 6.2 120 FTG 5.2 FE -1.1 Si 16.0 5.6 10.1 17.8 0.091 TL 13.50 PV Pipe: 23 34.9 1.408 FL 4.67 PF 0.9 23 13.5 0.0 12.4 0.0 7.2 120 FTG 5.2 PE -1.1 S2 16.0 5.6 10.5 18.1 0.087 TL 9.87 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 1/3/2007 C:\HASS78\06-144-CB.SDF JOB TITLE: Hunter's Pointe Community Building PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. FT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 24 16.8 1.080 PL 13.00 PF 1.5 S2 16.0 5.6 10.5 18.1 5.9 120 FTG 5.2 PE 0.0 S3 16.0 5.6 9.0 16.8 0.082 TL 18.20 PV Pipe: 25 98.1 1.639 PL 1.00 PF 1.8 24 13.0 0.0 16.2 0.0 14.9 120 FTG 5.5 PE 0.0 25 13.0 0.0 14.4 0.0 0.281 TL 6.50 PV Pipe: 26 98.1 1.639 PL 2.15 PF 3.0 25 13.0 0.0 14.4 0.0 14.9 120 FTG 8.7 PE 0.0 26 13.0 0.0 11.3 0.0 0.281 TL 10.85 PV Pipe: 27 46.6 1.639 PL 7.88 PF 1.2 26 13.0 0.0 11.3 0.0 7.1 120 FTG 8.7 PE -0.4 27 14.0 0.0 9.7 0.0 0.071 TL 16.58 PV Pipe: 28 15.7 1.080 PL 8.30 PF 1.0 27 14.0 0.0 9.7 0.0 5.5 120 FTG 5.2 PE -0.9 S4 16.0 5.6 7.9 15.7 0.072 TL 13.50 PV Pipe: 29 30.8 1.408 PL 4.67 PF 0.7 27 14.0 0.0 9.7 0.0 6.4 120 FTG 5.2 PE -0.9 S5 16.0 5.6 8.2 16.0 0.069 TL 9.87 PV Pipe: 30 14.8 1.080 PL 13.00 PF 1.2 S5 16.0 5.6 8.2 16.0 5.2 120 FTG 5.2 FE 0.0 S6 16.0 5.6 7.0 14.8 0.065 TL 18.20 PV Pipe: 31 17.5 1.080 PL 8.30 PF 1.2 26 13.0 0.0 11.3 0.0 6.1 120 FTG 5.2 PE -0.4 S7 14.0 5.6 9.7 17.5 0.088 TL 13.50 PV Pipe: 32 34.1 1.408 PL 4.67 PF 0.8 26 13.0 0.0 11.3 0.0 7.0 120 FTG 5.2 PE -0.4 S8 14.0 5.6 10.1 17.8 0.083 TL 9.87 PV Pipe: 33 16.3 1.408 FL 13.00 PF 1.6 S8 14.0 5.6 10.1 17.8 3.4 120 FTG 61.0 FE 0.0 S9 14.0 5.6 8.5 16.3 0.021 TL 74.00 PV Pipe: 34 -50.1 1.639 FL 47.10 PF 4.5 24 13.0 0.0 16.2 0.0 7.6 120 FTG 8.7 FE -0.4 28 14.0 0.0 20.3 0.0 0.081 TL 55.80 PV Pipe: 35 -1.3 1.639 FL 35.00 PF 0.0 28 14.0 0.0 20.3 0.0 0.2 120 FTG 18.0 FE 0.4 20 13.0 0.0 20.7 0.0 0.000 TL 53.00 PV Pipe: 36 56.5 1.639 FL 3.92 PF 0.9 22 13.0 0.0 14.0 0.0 8.6 120 FTG 5.2 PE 0.0 21A 13.0 0.0 13.0 0.0 0.101 TL 9.12 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 1/3/2007 C:\HASS78\06-144-CB.SDF JOB TITLE: Hunter's Pointe Community Building 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: 37 18.8 1.080 PL 8.30 PF 1.4 21A 13.0 0.0 13.0 0.0 6.6 120 FTG 5.2 PE -0.4 S10 14.0 5.6 11.3 18.8 0.101 TL 13.50 PV Pipe: 38 37.7 1.408 PL 4.67 PF 1.0 21A 13.0 0.0 13.0 0.0 7.8 120 FTG 5.2 PE -0.4 S11 14.0 5.6 11.6 19.1 0.100 TL 9.87 PV Pipe: 39 18.7 1.408 PL 13.00 PF 0.5 Sil 14.0 5.6 11.6 19.1 3.8 120 FTG 6.1 PE 0.0 S12 14.0 5.6 11.1 18.7 0.027 TL 19.10 PV NOTES: Calculations were performed by the HASS 7.8 computer program under license no. 27091255 granted by HRS Systems, Inc. 4792 LaVista Road Tucker, GA 30084 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 0.167 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 21.3 ft/sec at pipe 5A. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: * MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEfl ChkViv BfyVlv GatViv AimChk DPViv NPTee 1.080 2.30 5.76 2.30 5.76 6.91 1.15 11.52 11.52 5.76 1.408 3.31 6.62 2.21 7.72 6.62 1.10 11.03 11.03 6.62 1.639 4.36 8.73 2.18 9.82 6.54 1.09 10.91 10.91 8.73 1.995 4.21 8.41 2.52 9.26 5.05 0.84 8.41 8.41 8.41 2.104 5.45 10.90 3.27 11.99 6.54 1.09 10.90 10.90 10.90 6.340 17.37 37.23 11.17 39.71 12.41 3.72 34.75 34.75 37.23 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 1/3/2007 C:\HASS78\06-144-CB.SDF JOB TITLE: Hunter's Pointe Community Building PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEil ChkVlv BfyVlv GatViv AlmChk DPViv NPTee 2.067 5.00 10.00 3.00 11.00 6.00 1.00 10.00 10.00 10.00 3.068 7.00 15.00 5.00 16.00 10.00 1.00 13.00 13.00 15.00 100. 0 G 80.0 A U G E WATER SUPPLY ANALYSIS Static: 94.50 psi Resid: 89.10 psi Flow: 1500.0 qpm LEGEND Available pressure 94.21 psi 8 307.5 gprn -Required pressure 2 77.88 psi 8 307.5 gpm Source Supply Curve System Demand Curve 60.0 R E S S U R E 40.0 p S i 20.0 0.0 -14.71 I I I i i I i I 400 600 800 1000 1200 1400 1600 1800 FLOW (GPM) SOUTHLAND FIRE PROTECTION, INC. 4733 POINT LOMA AVENUE SAN DIEGO,CA 92107 HYDRAULIC CALCULATIONS FOR Hunter's Pointe Building Type 3 Calc. Family Apartments Carlsbad, Ca. FILE NUMBER: 06-144 DATE: JAN 3, 2007 -DESIGN DATA- OCCUPANCY CLASSIFICATION: DENSITY: AREA OF APPLICATION: COVERAGE PER SPRINKLER: NUMBER OF SPRINKLERS CALCULATED: TOTAL SPRINKLER WATER FLOW REQUIRED: TOTAL WATER REQUIRED (including hose): FLOW AND PRESSURE (@ BOR) SPRINKLER ORIFICE SIZE: NAME OF CONTRACTOR: DESIGN/LAYOUT BY: AUTHORITY HAVING JURISDICTION: CONTRACTOR CERTIFICATION NUMBER: R-3 .05 gpm/sq. ft. Remote Area 5 256 sq. ft. 4 sprinklers 56.7 gpm 306.7 gpm 56.7 gpm @ 30.4 psi 1/2 inch Southland Fire Protection, Inc. Sorida Phan Carlsbad Fire Department C-16 611956 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE # 27091255 HRS SYSTEMS, INC. TUCKER, GA 30084 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 1/3/2007 C:\HASS78\06-144-5.SDF JOB TITLE: Hunter's Pointe Building Type 3 Caic. WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) 1 94.5 89.1 1500.0 94.2 306.7 31.9 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 306.7 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 250.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 56.7 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 0.0 SOURCE 31.9 56.7 2 0.0 - - - - 31.9 - - - 3 3.0 - - - - 30.6 4 3.0 - - - - 27.6 - - - 5 3.0 - - - - 27.6 5A -6.0 - - - - 31.5 6A -7.0 - - - - 31.8 BOR -4.0 - - - - 30.4 TOR 3.0 - - - - 27.0 6 3.0 - - - - 26.5 - - - 7 3.0 - - - - 26.4 - - - 8 3.0 - - - - 26.2 - - - 9 3.0 - - - - 26.1 - - - 10 3.0 - - - - 26.3 - - - 11 3.0 - - - - 26.2 12 3.0 - - - - 26.1 - - - 13 3.0 - - - - 26.3 - - - 14 3.0 - - - - 26.0 - - - 15 3.0 - - - - 26.0 - - - 16 3.0 - - - - 26.0 - - - 17 3.0 - - - - 26.0 - - - 18 3.0 - - - - 25.9 19 3.0 - - - - 25.8 20 3.0 - - - - 25.9 - - - 21 3.0 - - - - 25.8 - - - 30 12.0 - - - - 21.6 - - - 31 12.0 - - - - 21.6 32 12.0 - - - - 21.4 - - - 33 12.0 - - - - 21.4 - - - 34 12.0 - - - - 21.4 - - - 35 12.0 - - - - 21.4 - - - 36 12.0 - - - - 21.6 - - - 37 12.0 - - - - 21.6 - - - 40 21.0 - - - - 17.2 - - - I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 1/3/2007 C:\HASS78\06-144-5.SDF JOB TITLE: Hunter's Pointe Building Type 3 Caic. NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 41 21.0 - - - - 17.0 - - - 42 21.0 - - - - 16.0 - - - 43 21.0 - - - - 15.8 - - - 44 21.0 - - - - 15.7 - - - 45 21.0 - - - - 15.8 - - - 46 21.0 - - - - 15.5 - - - 47 21.0 - - - - 16.7 - - - 48 21.0 - - - - 17.0 - - - 49 21.0 - - - - 16.7 - - - 50 21.0 - - - - 17.0 - - - 51 21.0 - - - - 15.3 52 21.0 - - - - 14.7 53 21.0 - - - - 15.7 - - - 54 21.0 - - - - 15.6 55 21.0 - - - - 15.5 - - - 56 21.0 - - - - 16.9 - - - 57 21.0 - - - - 17.2 - - - 60 30.0 - - - - 11.5 - - - 61 30.0 - - - - 11.3 - - - 62 30.0 - - - - 11.2 - - - 63 30.0 - - - - 11.4 - - - 64 30.0 - - - - 8.6 65 30.0 - - - - 8.6 66 30.0 - - - - 8.9 67 30.0 - - - - 9.6 - - - 68 30.0 - - - - 8.8 - - - 69 30.0 - - - - 8.9 70 30.0 - - - - 10.5 71 30.0 - - - - 10.9 - - - Si 30.0 K= 4.90 8.4 14.2 S2 30.0 K= 4.90 8.2 14.0 S3 30.0 K= 4.90 8.5 14.3 S4 30.0 K= 4.90 8.5 14.3 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 1/3/2007 C:\HASS78\06-144-5.SDF JOB TITLE: Hunter's Pointe Building Type 3 Calc. 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 56.7 6.340 PL 11.20 PF 0.0 1 0.0 SRCE 31.9 (N/A) 0.6 140 FTG ETG PE 0.0 2 0.0 0.0 31.9 0.0 0.000 TL 86.78 PV Pipe: 2 56.7 6.340 PL 4.00 PF 0.0 2 0.0 0.0 31.9 0.0 0.6 140 FTG E FE -1.3 3 3.0 0.0 30.6 0.0 0.000 TL 27.11 PV Pipe: 3 FIXED PRESSURE LOSS DEVICE 3 3.0 0.0 30.6 0.0 3.0 psi, 56.7 gpm 4 3.0 0.0 27.6 0.0 Pipe: 4 56.7 4.280 PL 4.00 PF 0.0 4 3.0 0.0 27.6 0.0 1.3 140 FTG E PE 0.0 5 3.0 0.0 27.6 0.0 0.001 TL 21.92 PV Pipe: 5 56.7 4.280 PL 9.00 PF 0.0 5 3.0 0.0 27.6 0.0 1.3 140 FTG E PE 3.9 5A -6.0 0.0 31.5 0.0 0.001 TL 26.92 PV Pipe: 5A 56.7 2.703 FL 4.00 PF 0.1 5A -6.0 0.0 31.5 0.0 3.2 120 FTG E PE 0.4 6A -7.0 0.0 31.8 0.0 0.009 TL 13.33 PV Pipe: SB 56.7 2.703 PL 4.00 PF 0.1 6A -7.0 0.0 31.8 0.0 3.2 120 FTG E PE -1.3 BOR -4.0 0.0 30.4 0.0 0.009 TL 13.33 PV Pipe: 6 56.7 2.703 PL 9.00 PF 0.3 BOR -4.0 0.0 30.4 0.0 3.2 120 FTG 22.0 FE -3.0 TOR 3.0 0.0 27.0 0.0 0.009 TL 31.00 PV Pipe: 7 56.7 2.703 PL 39.83 PF 0.5 TOR 3.0 0.0 27.0 0.0 3.2 120 FTG 21.0 FE 0.0 6 3.0 0.0 26.5 0.0 0.009 TL 60.83 PV Pipe: 8 48.8 2.703 FL 16.00 PF 0.1 6 3.0 0.0 26.5 0.0 2.7 120 FTG 6.0 FE 0.0 7 3.0 0.0 26.4 0.0 0.007 TL 22.00 PV Pipe: 9 26.8 2.703 PL 17.75 PF 0.1 7 3.0 0.0 26.4 0.0 1.5 120 FTG 6.0 FE 0.0 10 3.0 0.0 26.3 0.0 0.002 TL 23.75 PV Pipe: 10 5.9 2.703 PL 16.00 PF 0.0 10 3.0 0.0 26.3 0.0 0.3 120 FTG 6.0 FE 0.0 13 3.0 0.0 26.3 0.0 0.000 TL 22.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 1/3/2007 C:\HASS78\06-144--5.SDF JOB TITLE: Hunter's Pointe Building Type 3 Caic. 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: 11 8.0 1.536 PL 114.30 PF 0.5 6 3.0 0.0 26.5 0.0 1.4 120 FTG 12.0 PE 0.0 14 3.0 0.0 26.0 0.0 0.004 TL 126.30 PV Pipe: 12 8.0 2.703 PL 16.00 PF 0.0 14 3.0 0.0 26.0 0.0 0.4 120 FTG 6.0 PE 0.0 15 3.0 0.0 26.0 0.0 0.000 TL 22.00 PV Pipe: 13 1.4 2.703 PL 17.75 PF 0.0 15 3.0 0.0 26.0 0.0 0.1 120 FTG 6.0 PE 0.0 16 3.0 0.0 26.0 0.0 0.000 TL 23.75 PV Pipe: 14 -5.9 2.703 PL 16.00 PF 0.0 16 3.0 0.0 26.0 0.0 0.3 120 FTG 6.0 PE 0.0 17 3.0 0.0 26.0 0.0 0.000 TL 22.00 PV Pipe: 15 6.5 1.536 PL 114.30 PF 0.3 7 3.0 0.0 26.4 0.0 1.1 120 FTG 12.0 PE 0.0 15 3.0 0.0 26.0 0.0 0.003 TL 126.30 PV Pipe: 16 15.5 1.536 PL 3.25 PF 0.1 7 3.0 0.0 26.4 0.0 2.7 120 FTG 6.0 PE 0.0 8 3.0 0.0 26.2 0.0 0.013 TL 9.25 PV Pipe: 17 15.5 1.536 PL 1.25 PF 0.1 8 3.0 0.0 26.2 0.0 2.7 120 FTG 6.0 PE 0.0 9 3.0 0.0 26.1 0.0 0.013 TL 7.25 PV Pipe: 18 13.1 1.536 PL 8.10 PF 0.1 15 3.0 0.0 26.0 0.0 2.3 120 FTG 6.0 PE 0.0 18 3.0 0.0 25.9 0.0 0.009 TL 14.10 PV Pipe: 19 13.1 1.536 PL 1.25 PF 0.1 18 3.0 0.0 25.9 0.0 2.3 120 FTG 6.0 PE 0.0 19 3.0 0.0 25.8 0.0 0.009 TL 7.25 PV Pipe: 20 5.9 1.536 PL 114.30 PF 0.3 10 3.0 0.0 26.3 0.0 1.0 120 FTG 12.0 PE 0.0 16 3.0 0.0 26.0 0.0 0.002 TL 126.30 PV Pipe: 21 15.0 1.536 PL 3.25 PF 0.1 10 3.0 0.0 26.3 0.0 2.6 120 FTG 6.0 PE 0.0 11 3.0 0.0 26.2 0.0 0.012 TL 9.25 PV Pipe: 22 15.0 1.536 PL 1.25 PF 0.1 11 3.0 0.0 26.2 0.0 2.6 120 FTG 6.0 PE 0.0 12 3.0 0.0 26.1 0.0 0.012 TL 7.25 PV Pipe: 23 13.1 1.536 PL 8.10 PF 0.1 16 3.0 0.0 26.0 0.0 2.3 120 FTG 6.0 PE 0.0 20 3.0 0.0 25.9 0.0 0.009 TL 14.10 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 1/3/2007 C:\HASS78\06-144-5.SDF JOB TITLE: Hunter's Pointe Building Type 3 Caic. 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: 24 13.1 1.536 PL 1.25 PF 0.1 20 3.0 0.0 25.9 0.0 2.3 120 FTG 6.0 PE 0.0 21 3.0 0.0 25.8 0.0 0.009 TL 7.25 PV Pipe: 25 5.9 1.536 PL 114.30 PF 0.3 13 3.0 0.0 26.3 0.0 1.0 120 FTG 12.0 PE 0.0 17 3.0 0.0 26.0 0.0 0.002 TL 126.30 PV Pipe: 26 15.5 1.101 PL 9.00 PF 0.7 9 3.0 0.0 26.1 0.0 5.2 150 FTG 7.0 PE -3.9 30 12.0 0.0 21.6 0.0 0.042 TL 16.00 PV Pipe: 27 15.0 1.101 PL 9.00 PF 0.6 12 3.0 0.0 26.1 0.0 5.1 150 FTG 7.0 PE -3.9 37 12.0 0.0 21.6 0.0 0.040 TL 16.00 PV Pipe: 28 13.1 1.101 PL 9.00 PF 0.5 19 3.0 0.0 25.8 0.0 4.4 150 FTG 7.0 PE -3.9 33 12.0 0.0 21.4 0.0 0.031 TL 16.00 PV Pipe: 29 13.1 1.101 PL 9.00 PF 0.5 21 3.0 0.0 25.8 0.0 4.4 150 FTG 7.0 PE -3.9 35 12.0 0.0 21.4 0.0 0.031 TL 16.00 PV Pipe: 30 1.8 1.101 PL 2.20 PF 0.0 30 12.0 0.0 21.6 0.0 0.6 150 FTG 7.0 PE 0.0 31 12.0 0.0 21.6 0.0 0.001 TL 9.20 PV Pipe: 31 1.8 1.101 PL 125.67 PF 0.1 31 12.0 0.0 21.6 0.0 0.6 150 FTG 28.0 PE 0.0 32 12.0 0.0 21.4 0.0 0.001 TL 153.67 PV Pipe: 32 1.6 1.101 PL 2.20 PF 0.0 32 12.0 0.0 21.4 0.0 0.5 150 FTG 5.0 PE 0.0 33 12.0 0.0 21.4 0.0 0.001 TL 7.20 PV Pipe: 33 0.2 1.101 PL 55.84 PF 0.0 32 12.0 0.0 21.4 0.0 0.1 150 FTG 16.0 PE 0.0 34 12.0 0.0 21.4 0.0 0.000 TL 71.84 PV Pipe: 34 2.0 1.101 PL 2.20 PF 0.0 34 12.0 0.0 21.4 0.0 0.7 150 FTG 5.0 PE 0.0 35 12.0 0.0 21.4 0.0 0.001 TL 7.20 PV Pipe: 35 -1.8 1.101 PL 125.67 PF 0.1 34 12.0 0.0 21.4 0.0 0.6 150 FTG 28.0 PE 0.0 36 12.0 0.0 21.6 0.0 0.001 TL 153.67 PV Pipe: 36 -1.8 1.101 PL 2.20 PF 0.0 36 12.0 0.0 21.6 0.0 0.6 150 FTG 5.0 PE 0.0 37 12.0 0.0 21.6 0.0 0.001 TL 7.20 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 1/3/2007 C:\HASS78\06-144-5.SDF JOB TITLE: Hunter's Pointe Building Type 3 Caic. PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (PT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 36A 0.0 1.101 PL 55.84 PF 0.0 36 12.0 0.0 21.6 0.0 0.0 150 FTG 16.0 PE 0.0 31 12.0 0.0 21.6 0.0 0.000 TL 71.84 PV Pipe: 37 13.7 1.101 PL 9.00 PP 0.5 30 12.0 0.0 21.6 0.0 4.6 150 FTG 5.0 PE -3.9 40 21.0 0.0 17.2 0.0 0.034 TL 14.00 PV Pipe: 38 13.2 1.101 PL 9.00 PP 0.4 37 12.0 0.0 21.6 0.0 4.4 150 FTG 5.0 PE -3.9 57 21.0 0.0 17.2 0.0 0.031 TL 14.00 PV Pipe: 39 14.7 1.101 PL 9.00 PF 0.5 33 12.0 0.0 21.4 0.0 5.0 150 FTG 5.0 PE -3.9 48 21.0 0.0 17.0 0.0 0.038 TL 14.00 PV Pipe: 40 15.1 1.101 PL 9.00 PF 0.6 35 12.0 0.0 21.4 0.0 5.1 150 FTG 5.0 PE -3.9 50 21.0 0.0 17.0 0.0 0.041 TL 14.00 PV Pipe: 41 13.7 1.101 PL 2.10 PF 0.2 40 21.0 0.0 17.2 0.0 4.6 150 FTG 5.0 PE 0.0 41 21.0 0.0 17.0 0.0 0.034 TL 7.10 PV Pipe: 42 12.7 1.101 PL 25.92 PF 1.0 41 21.0 0.0 17.0 0.0 4.3 150 FTG 8.0 PE 0.0 42 21.0 0.0 16.0 0.0 0.030 TL 33.92 PV Pipe: 43 10.2 1.101 PL 2.10 PF 0.1 42 21.0 0.0 16.0 0.0 3.4 150 FTG 5.0 PE 0.0 43 21.0 0.0 15.8 0.0 0.020 TL 7.10 PV Pipe: 44 10.2 1.101 PL 0.67 PF 0.1 43 21.0 0.0 15.8 0.0 3.4 150 FTG 5.0 PE 0.0 44 21.0 0.0 15.7 0.0 0.020 TL 5.67 PV Pipe: 45 2.5 1.101 PL 78.50 PP 0.1 42 21.0 0.0 16.0 0.0 0.8 150 FTG 20.0 PE 0.0 45 21.0 0.0 15.8 0.0 0.001 TL 98.50 PV Pipe: 46 15.6 1.101 PL 2.10 PP 0.3 45 21.0 0.0 15.8 0.0 5.3 150 FTG 5.0 PE 0.0 46 21.0 0.0 15.5 0.0 0.043 TL 7.10 PV Pipe: 47 -13.1 1.101 PL 21.25 PF 0.9 45 21.0 0.0 15.8 0.0 4.4 150 FTG 8.0 PE 0.0 47 21.0 0.0 16.7 0.0 0.031 TL 29.25 PV Pipe: 48 -14.7 1.101 PL 2.20 PF 0.3 47 21.0 0.0 16.7 0.0 5.0 150 FTG 5.0 PE 0.0 48 21.0 0.0 17.0 0.0 0.038 TL 7.20 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 1/3/2007 C:\HASS78\06-144-5.SDF JOB TITLE: Hunter's Pointe Building Type 3 Calc. PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (PT) SUM. NODES (PT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 49 1.6 1.101 FL 55.84 PF 0.0 47 21.0 0.0 16.7 0.0 0.5 150 FTG 16.0 PE 0.0 49 21.0 0.0 16.7 0.0 0.001 TL 71.84 PV Pipe: 50 -15.1 1.101 PL 2.10 PF 0.3 49 21.0 0.0 16.7 0.0 5.1 150 FTG 5.0 PE 0.0 50 21.0 0.0 17.0 0.0 0.041 TL 7.10 PV Pipe: 51 16.7 1.101 FL 21.25 PP 1.4 49 21.0 0.0 16.7 0.0 5.6 150 FTG 7.0 FE 0.0 51 21.0 0.0 15.3 0.0 0.049 TL 28.25 PV Pipe: 52 21.4 1.101 FL 2.20 PF 0.6 51 21.0 0.0 15.3 0.0 7.2 150 FTG 5.0 PE 0.0 52 21.0 0.0 14.7 0.0 0.077 TL 7.20 PV Pipe: 53 -4.7 1.101 FL 78.50 PF 0.5 51 21.0 0.0 15.3 0.0 1.6 150 FTG 20.0 FE 0.0 53 21.0 0.0 15.7 0.0 0.005 TL 98.50 PV Pipe: 54 9.5 1.101 FL 2.10 PF 0.1 53 21.0 0.0 15.7 0.0 3.2 150 FTG 5.0 FE 0.0 54 21.0 0.0 15.6 0.0 0.017 TL 7.10 PV Pipe: 55 9.5 1.101 FL 0.67 PF 0.1 54 21.0 0.0 15.6 0.0 3.2 150 FTG 5.0 FE 0.0 55 21.0 0.0 15.5 0.0 0.017 TL 5.67 PV Pipe: 56 -14.2 1.101 FL 25.92 PF 1.2 53 21.0 0.0 15.7 0.0 4.8 150 FTG 7.0 FE 0.0 56 21.0 0.0 16.9 0.0 0.036 TL 32.92 PV. Pipe: 57 -13.2 1.101 FL 2.20 PP 0.3 56 21.0 0.0 16.9 0.0 4.4 150 FTG 7.0 FE 0.0 57 21.0 0.0 17.2 0.0 0.031 TL 9.20 PV Pipe: 58 -1.0 1.101 PL 55.84 PF 0.0 56 21.0 0.0 16.9 0.0 0.3 150 FTG 16.0 FE 0.0 41 21.0 0.0 17.0 0.0 0.000 TL 71.84 PV Pipe: 59 10.2 1.101 FL 9.00 PP 0.3 44 21.0 0.0 15.7 0.0 3.4 150 FTG 7.0 FE -3.9 60 30.0 0.0 11.5 0.0 0.020 TL 16.00 PV Pipe: 60 9.5 1.101 FL 9.00 PF 0.3 55 21.0 0.0 15.5 0.0 3.2 150 FTG 7.0 FE -3.9 63 30.0 0.0 11.4 0.0 0.017 TL 16.00 PV Pipe: 61 15.6 1.101 FL 9.00 PP 0.7 46 21.0 0.0 15.5 0.0 5.3 150 FTG 7.0 FE -3.9 71 30.0 0.0 10.9 0.0 0.043 TL 16.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 1/3/2007 C:\HASS78\06-144-5.SDF JOB TITLE: Hunter's Pointe Building Type 3 Cab. 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: 62 21.4 1.101 FL 9.00 PF 1.2 52 21.0 0.0 14.7 0.0 7.2 150 FTG 7.0 PE -3.9 67 30.0 0.0 9.6 0.0 0.077 TL 16.00 PV Pipe: 63 10.2 1.101 FL 2.75 PF 0.2 60 30.0 0.0 11.5 0.0 3.4 150 FTG 7.0 PE 0.0 61 30.0 0.0 11.3 0.0 0.020 TL 9.75 PV Pipe: 64 4.0 1.101 PL 20.25 PF 0.1 61 30.0 0.0 11.3 0.0 1.3 150 FTG 9.0 FE 0.0 62 30.0 0.0 11.2 0.0 0.003 TL 29.25 PV Pipe: 65 9.5 1.101 PL 2.75 PF 0.2 63 30.0 0.0 11.4 0.0 3.2 150 FTG 7.0 PE 0.0 62 30.0 0.0 11.2 0.0 0.017 TL 9.75 PV Pipe: 66 13.5 1.101 PL 63.00 PF 2.6 62 30.0 0.0 11.2 0.0 4.5 150 FTG 17.0 PE 0.0 64 30.0 0.0 8.6 0.0 0.033 TL 80.00 PV Pipe: 67 14.2 1.101 FL 0.92 PF 0.2 64 30.0 0.0 8.6 0.0 4.8 150 FTG 5.0 PE 0.0 Sb 30.0 4.9 8.4 14.2 0.036 TL 5.92 PV Pipe: 68 -0.7 1.101 PL 12.83 PF 0.0 64 30.0 0.0 8.6 0.0 0.2 150 FTG 8.0 PE 0.0 65 30.0 0.0 8.6 0.0 0.000 TL 20.83 PV Pipe: 69 14.0 1.101 FL 6.67 PF 0.4 65 30.0 0.0 8.6 0.0 4.7 150 FTG 5.0 PE 0.0 S2 30.0 4.9 8.2 14.0 0.035 TL 11.67 PV Pipe: 70 -14.7 1.101 FL 2.20 PF 0.3 65 30.0 0.0 8.6 0.0 5.0 150 FTG 5.0 PE 0.0 66 30.0 0.0 8.9 0.0 0.038 TL 7.20 PV Pipe: 71 21.4 1.101 FL 2.75 PF 0.8 67 30.0 0.0 9.6 0.0 7.2 150 FTG 7.0 FE 0.0 66 30.0 0.0 8.9 0.0 0.077 TL 9.75 PV Pipe: 72 6.7 1.101 FL 2.20 PF 0.1 66 30.0 0.0 8.9 0.0 2.3 150 FTG 5.0 FE 0.0 68 30.0 0.0 8.8 0.0 0.009 TL 7.20 PV Pipe: 73 14.3 1.101 FL 2.00 PF 0.3 68 30.0 0.0 8.8 0.0 4.8 150 FTG 5.0 FE 0.0 S3 30.0 4.9 8.5 14.3 0.037 TL 7.00 PV Pipe: 74 -7.6 1.101 FL 4.75 PF 0.1 68 30.0 0.0 8.8 0.0 2.6 150 FTG 5.0 FE 0.0 69 30.0 0.0 8.9 0.0 0.011 TL 9.75 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 1/3/2007 C:\HASS78\06-144-5.SDF JOB TITLE: Hunter's Pointe Building Type 3 Caic. 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: 75 14.3 1.101 PL 6.50 PF 0.4 69 30.0 0.0 8.9 0.0 4.8 150 FTG 5.0 PE 0.0 S4 30.0 4.9 8.5 14.3 0.036 TL 11.50 PV Pipe: 76 -21.9 1.101 PL 13.20 PF 1.6 69 30.0 0.0 8.9 0.0 7.4 150 FTG 7.0 PE 0.0 70 30.0 0.0 10.5 0.0 0.080 TL 20.20 PV Pipe: 77 15.6 1.101 PL 2.20 PF 0.4 71 30.0 0.0 10.9 0.0 5.3 150 FTG 7.0 PE 0.0 70 30.0 0.0 10.5 0.0 0.043 TL 9.20 PV Pipe: 78 -6.2 1.101 PL 78.00 PF 0.8 70 30.0 0.0 10.5 0.0 2.1 150 FTG 21.0 PE 0.0 61 30.0 0.0 11.3 0.0 0.008 TL 99.00 PV NOTES: Calculations were performed by the HASS 7.8 computer program under license no. 27091255 granted by HRS Systems, Inc. 4792 LaVista Road Tucker, GA 30084 The system has been calculated to provide an average imbalance at each node of 0.002 gprn and a maximum imbalance at any node of 0.128 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 7.4 ft/sec at pipe 76. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: * MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPVlv NPTee 1.101 2.53 6.33 2.53 6.33 7.59 1.27 12.66 12.66 6.33 1.536 3.18 6.36 1.59 7.16 4.77 0.80 7.95 7.95 6.36 2.703 9.33 18.65 6.22 21.76 10.88 1.55 15.54 15.54 18.65 4.280 13.47 26.94 8.08 29.64 16.17 2.69 26.94 26.94 26.94 6.340 17.37 37.23 11.17 39.71 12.41 3.72 34.75 34.75 37.23 100.0 G 80.0 A U G E P 60.0 R E S S 40.0 P S ± 20.0 mm -14.7 WATER SUPPLY ANALYSIS Static: 94.50 psi Resid: 89.10 psi Fl o w : 1 5 0 0 . 0 g p m 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 DATE: 1/3/2007 C:\HASS78\06-144-5.SDF 'JOB TITLE: Hunter's Pointe Building Type 3 Cab. WATER SUPPLY CURVE 96+ *\0\\\\\\\\\\\\\\\\ \\\\\\\\\\\\\\\\\\\ I * <-89.1 psi @ 1500 gpm 88+ Flow Test Point 80+ 72+ P 64+ R I E S S 56+ U I R I E I 48+ P I S I I 40+ 32+ X 24+ 16+ LEGEND I X = Required Water Supply I 31.90 psi @ 306.7 gpm 8+ I 0 = Available Water Supply 94.21 psi @ 306.7 gpm 0++-+---+----+-----+ ------+ --------+ --------+ ---------+ -----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) Bulletin 014 Rev. J Model Fl FR Series Quick Response Standard Spray Model Fl FR56 Sprinkler Types Standard Upright Standard Pendent Conventional Vertical Sidewall Horizontal Sidewall Model Fl FR56 Recessed Sprinkler Types Standard Pendent/F1/F2/FP Horizontal Sidewall Model Fl FR56 Concealed Sprinkler Types Standard Pendent Model F1FR42, F1FRXLH & FlFR28 Sprinkler Types Standard Upright Standard Pendent Model Fl FR42, Fl FRXLH & Fl FR28 Recessed Sprinkler Types Standard Pendent Model Fl FR56LL & Fl FR42LL Low Lead Sprinkler Types* Standard Pendent Less than 0.25% Lead Content Listing & Approvals Underwriters Laboratories Inc. and Certified for Canada (cULus). Factory Mutual Approvals (FM) Loss Prevention Council (LPCB, UK) VdS SchadenverhUtung GmbH NSF Certified to NSF/ANSi Standard 61 Annex G UL Listing Category Sprinklers, Automatic & Open (VNIV) Quick Response Sprinkler Product Description Reliable Models F1FR56, F1FR56LL, F1FR42, F1FR42LL, F1FRXLH & F1FR28 Series Sprinklers are quick response sprinklers which combine the durability of a standard sprin- kler with the attractive low profile of a decorative sprinkler. The Models F1FR56, F1FR56LL, F1FR42, F1FR42LL, F1FRXLH & Fl FR28 Series Recessed automatic sprinklers utilize a 3.0 mm frangible glass bulb. These sprinklers have demonstrated response times in laboratory tests which are five to ten times faster than standard response sprinklers. This quick response enables the Model F1 FR56, F1FR56LL, F1FR42, F1FR42LL, F1FRXLH & F1FR28 Series sprinklers Upright Pendent Conventional oar Vertical Sidewall Horizontal Sidewall Recessed Pendent/Fl/F2 V. Recessed Concealed Recessed Horizontal Sidewall Pendent PendentiFP j4IWJ1a1 4I:IT&m Pendent F1/F2 to apply water to a fire much faster than standard sprinklers of the same tem- perature rating. The glass bulb consists of an accu- rately controlled amount of special fluid hermetically sealed inside a precisely manufactured glass capsule. This glass XLH Recessed bulb is specially constructed to provide PendentFP fast thermal response. At normal temperatures, the glass bulb contains the fluid in both the liquid and vapor phases. The vapor phase can be seen as a small bubble. As heat is applied, the liquid expands, forcing the bubble smaller and smaller as the liq- uid pressure increases. Continued heating forces the liquid to push out against the bulb, causing the glass to shatter, opening the waterway and allowing the deflector to distrib- ute the discharging water. The Reliable Automatic Sprinkler Co., Inc., 103 Fairview Park Drive, Elmsford, New York 10523 Application Quick response sprinklers are used in fixed fire protection systems: Wet, Dry, Deluge or Preactio n . C a r e m u s t b e exercised that the orifice size, temperature rating, deflector style and sprinkler type are in accordan c e w i t h t h e l a t e s t published standards of the National Fire Protection Association or the approving Authority Having Juris d i c t i o n . Q u i c k response sprinklers are intended for installation as specified in NFPA 13. Quick response sprinklers and st a n d a r d r e - sponse sprinklers should not be intermixed. Pin tie XLH Only Deflector Load Screw Wcsher Bulb Frame Cup O74FCO6A Model F1FR42, F1FRXLH Upright Technical data: Models Discharge Coefficient Response Thread Size Max. Working Mm. Working Temperature FinishRating Pressure Pressure F1FR56 **F1 FR56LL1t K 5.6 Quick 1/2 NPT See See F1FR42 **F1FR42LL11) K 4.2 Response (R1/2) 175 PSI 7 PSI Temperature Finish Table F1FRXLH K 2.8 Ratings Table. Fl FR28 Low Lead Sprinklers available only with Temperature Rating 200°F/93c Material Data: Frame Deflector Load Screw Pintle Cup Washer Bulb DZR Brass CDA Alloy 260, CDA Alloy 360 CDA Alloy 360 CDA Alloy 651 Nickel Alloy 440 or Alloy 360 QM Brass CDA Alloy 220 or or or coated with PTFE Adhesive Glass *Low Lead Brass or CDA Alloy 544 CDA Alloy 544 CDA _Alloy5lo CDA Alloy 693 Tape 2. Model F1FR56, Upright, Pendent & Conventional Sprinklers Model Fl FR42, Fl FRXLH & Fl FR28 Upright & Pendent Sprinklers Installation Wrench: Model D Sprinkler Wrench Installation Data: Nominal Orifice 1 Thread Nominal K Factor Sprinkler Approval Sprinkler Identification Number (SIN Size j US Metric Height Organization Upright Pendant Standard- Upright(SSU)andPendent Deflectors Marked to Indicate Position 1/2'_(15mm)i 1/2__NPT(R1/2) 5.5 80 2,25"(57mm) 1,2,3,4 RA1425 3 RA1414Xe))3) 7/16"(10mm) 1/2"NPT (R1/2) 4.2 2.25"(57mm) 1 RA1423 3/8"(10mm) 1/2" NPT (R1/2) 2.8 _60 _40 2.25"(57mm) 1 RA1421 _RA1413 RA1411 Conventional-Install In Upright or Pendent Position 15mm 1/2" NPT (A 1/2) 5.6 1 80 1 57mm 1 3,4 j RA14752 cULus listed corrosion resistant (Polyester coated) sprinkler. 2) Polyester coated FM approved sprinkler. Polyester coated LPCB & VdS approved sprinkler RA1425, RA1414 & RA1475. Upright Pendent Conventional Model Fl FR56LL & Fl FR42LL Pendent Sprinklers Installation Wrench: Model 0 Sprinkler Wrench Installation Data: Nominal Thread Nominal K Factor Sprinkler Approval Sprinkler Identification Number (SIN) Orifice Size US _Metric Height Organization .Pendent Standard-Pendent Deflectors Marked to Indicate Position 1/2"(15mm) 1/2"NPT(R1/2) 5.6 80 2.25"(57mm){ 1,5 1_RA1414 7/16"(11mm) 1/2"NPT(A 1/2) 4.2 _60 25"(57mm) 1,5 RA1413 01 cULus listed corrosion resistant (Polyester coated) sprinkler. 3. 2 £X htE h H------ Ii (.-. , ------- . [2'.'•'""J (VP ,.cE o. r'wC O '.cr OF (('LOP I MINMIUM af-cr0'•7•.sJj Model F1FR56, F1FR42, F1FRXLH & F1FR28 Quick Response Recess e d P e n d e n t S p r i n k l e r (') Installation Wrench: Mode! GFR2 Sprinkler Wrench Installation Data: Nominal Orifice Thread Size K Factor - Sprinkler Height Sprinkler Identification Number (SIN) US Metric 1/2 (15mm) 112 NPT(R½) 5.6 80 2.25" (57mm) RA 1414 7/16" (10mm) 1/2' NPT (R1/2) 4.2 60 2:25 (57mm) RA 1413 3/8' (10mm) 1/2' NPT (R1/2) 2,8 40 2.25 (57mm) RA141 1 1) Refer to escutcheon data table for approvals & dimensions Model F1FR56LL & F1FR42LL Quick Response Recessed Pende n t S p r i n k l e r (') Installation Wrench: Model GFR2 Sprinkler Wrench Installation Data: Nominal Orifice Thread Size K Factor Sprinkler Height Sprinkler Identification Number (SIN) us Metric 1/2' (15mm) 1/2" NPT(R½) 5.6 80 2.25" (57mm) RA1414 - 7/16" (10mm) 1/2" NPT (A 1/2) 4.2 60 2.25' (57mm) RA1413 Refer to escutcheon data table for approvals & dimensions Model F1FR56, F1FA56LL, F1FR42, F1FR42LL, F1FRXLH & F1FR28 Fl or F2 Model F1FR56, F1FR56LL, F1FR42, F1FR42LL, F1FRXLH & F1FR28 FP Model Fl FR56 Quick Response Vertical Sidewall Sprinkler Installation Wrench: Model 0 Sprinkler Wrench Installation Position: Upright or Pendent Approval Type: Light Hazard Occupancy Installation Data: Nominal Nominal K Factor I Sprinkler Approval Sprinkler I I US I Metric Orifice Thread Size Height Organizations Identification I Numbers (SIN) V2" (15mm) j ½" NPT (R1/2) 5.6 . 8.0 2.25" (57mm) 1,2,3,4 15mm ½" NPT (R1/2) 5.6 I 8.0 2.25" (57mm) 41') RA 1485P ' LPC Approval is for pendent position only. 01 cULus Listed corrosion resistant (Polyester coated) sprinkler. Sprinkler Type Deflector to Ceiling Distancel (Min. - Max.) Upright 4" (102mm) - 12" (305mm) Pendent 4' (102mm) - 12' (305mm) Vertical Sidewall Horizontal Sidewall LLI.aIrCJscc.a' A I ur;&rcaI wrr,7c- ,. ;,p'T,j o..,.,,,/ -' AT MINIMUM RECESS .- 2-1,/I4152.4""J I .41 4,145/MUM RECESS .41 MINiMUM RECESS [lQl.5mIr-304.5m,j CElL/NC Ti) CET'LI'CIOP Model Fl FR56 Quick Response Horizontal Sidewall Sprinkler Deflector: HSW Installation Wrench: Model D Sprinkler Wrench Installation Data: Horizontal Sidewall Nominal K Factor Sprinkler Approval Organizations Sprinkler __________________ Height and Type of Approval Nominal Orifice Thread Size Identification US Metric Light Hazard Ordinary Hazard Numbers (SIN) ½"(l5mm) /2 NPT(R1/2) 5.6 j 80' 23"(67mm) 1,2 1 RA 1435(1)(L) 10 cULus Listed corrosion resistant (Polyester coated) sprinkler. 01 Polyester coated FM approved sprinkler. .ACt: CF FlING r Ii 0'C5 AC OIMFIACIC(, E1_L I i25 4' MAXIMUM RECESS I 725. Al MINIMUM RECESS = 3/8 7.9 5's",j 2.ISCAIIC±LLQS AT 144SF/MUM RECESS 3/4 -[ 19--] AT MINIMUM RECESS 3/8 79. MA 2 /4 IqOLE' 0/4, [57.2',"1 REDUCER —r fl- I.5/1// TURN COt1,49 UNTiL ---' F/GIlT AGAINTI vpR/NA-LER WR,FNCIA ROSS. ('Ir C/I APPROVED I/Ti' 4 - 9 [101.1/4M .- 152.4MM] CEILING TO DEFLECTOR. Note: For Recessed HSW Sprinklers use installation wrench GFR2. Model Fl FR56 Quick Response Concealed Pendent Sprinklers Installation Wrench: Model RC1 Sprinkler Wrench Technical Data: Nominal Orifice "K" Factor Thread Size I Model Temp. Rating Max. Temp Ambient Bulb Color Approvals Sprinkler Identification Number(SIN) US Metric Sprinkler Cover ½" (15mm) 5.6 80 1/2" NPT F1FR 135°F/57C 135F/57°C 100F/381c Orange 1 RA 1414 ½" (15mm) 5.6 80 /2" NPT F1FR 155* 81 i35°F/57°C 1001F/381C Red 1,40) RA 1414 ½" (15mm) 5.6 80 112" NPT F1FR 175°F/79°C 165°F/74°C 1OdOF/380C Yellow 1 RA 1414 1/2"_(15mm) 5.6 80 i/A" NPT F1FR I 200°F/93°c 165°F/74°C 150°F/65°C Green 1 RA 1414 01 For VdS only = 155°F/68°c Norbulb and 1/2" [12,7mm] adjustment. Model F1FR56LL Quick Response Concealed Pendent Sprinklers Installation Wrench: Model AOl Sprinkler Wrench Technical Data: Nominal • Orifice "K" Factor I Thread I I . Size Model Temp. Rating Max. Ambient Temp Bulb Color Approvals Sprinkler . . Identification I Number(SIN) US Metric Sprinkler Cover ½15rn 5.6___.__80 "NPT F1FR5SLL ~OT~/~Y 6-5'F/74'C-,- 1501F/651C 1,5 i 5. /2' RiTiUCIrIC Tf/ CR (L&OW - ' 2 Elk 2 ' i± - j - -. - rACE or I7TONC CE/LINE 7 r - ,tTOF.4CEOFC IL 'JO 'COI'ERADJLISTMET/T '/ 1/1/16" 0EV/h' PLATE / 5/16" 2/4. GFRINIELEE Figure 1 Installation Aid A protective cap is included for use during installation. Important; The F1FR56 Sprinkler with Model COP cover plate is not an FM Approved combination. Installation Quick response sprinklers are intended for installation as specified in NFPA 13. Quick response sprinklers and stan- dard response sprinklers should not be intermixed. The Model F1FR56, F1FR56LL, F1FR42, F1FR42LL, F1FRXLH & F1FR28 Recessed Quick Response Sprin- klers are to be installed as shown. The Model Fl or F2 Es- cutcheons illustrated are the only recessed escutcheons to be used with the Model F1FR56, F1FR56LL, F1FR42, F1FR42LL, F1FRXLH & F1FR28 Sprinklers. The use of any other recessed escutcheon will void all approvals and ne- gate all warranties. When installing Model F1FR56, F1FR56LL, F1FR42, F1FR42LL, F1FRXLH & F1FR28 Sprinklers, use the Model D Sprinkler Wrench. Use the Model GFR2 Wrench for install- ing F1FR56, F1FR56LL, F1FR42, F1FR42LL, F1FRXLH & F1FR28 Recessed Pendent Sprinklers. Any other type of wrench may damage these sprinklers. NOTE: A leak tight ½" NPT (A 1/2) sprinkler joint can be obtained with a torque of 8-18 ft-lbs (10,8 - 24,4 N-m), Do not tighten sprinklers over maximum recommended torque. It may cause leakage or impairment of the sprinklers. The Models F1FR56/CCP & F1FR56LL/CCP Concealed Sprinkler use the /2" orifice, ½" NPT (R1/2), Model F1FR56 & Fl FR56LL Pendent Sprinkler with a threaded Model COP cup which is factory attached to the sprinklers. The Model F1FR56 Pndent is available in temperature rating of 135°F (57°C), 155°F (680C), 175°F (79°C) or 200°F (930C). The Model F1FR56LL Pendent is available only in a rating of 200°F (930C). The concealed sprinkler assemblies are com- pleted by the installation of the attractive low profile Model COP push on cover plate assembly, rated 135°F (57°C) or 165°F (74°C) for the Fl FR56 and 165°F (74°C) for the FIFR56 LL. The cover plate and sprinkler cup assemblies are joined using a cover plate skirt with flexible tabs for threaded en- *DuPont Registered Trade Mark 6. "7,0' RESECTYE TEE OP LIL1LIIV -- ii .- - - 2 .5/8' 0/A. 2 iUI' -- _I_ -. - rcr or INC CEILING COVER AOJUSTAI(RT -----L--------- ----- COVER I'LVTC / ASSEMBLY SPc'IM'LFR Figure 2 gagement. A choice of two cover plate assemblies provide either 1/2"(13mm) or 5/8" (8mm) of cover adjustment, Do not install these sprinklers in ceiling which have positive pressure in the space above. After a 2/8" (67mm) diameter hole is cut in the ceiling, the sprinkler is easily installed with the Model Aol Wrench. A Teflon* based thread sealant should be applied to the sprin- kler threads only. The Model R01 Wrench is then used to engage the sprinkler wrenching surfaces and to install the sprinkler in the fithng. When inserting or removing the wrench from the sprinkler/cup assembly, care should be tak- en to prevent damage to the sprinkler. DO NOT WRENCH ON ANY OTHER PART OF THE SPRINKLER. The cover plate is then pushed onto the cup. Final adjustment is made by hand turning the cover plate until the skirt flange makes full contact with the ceiling. Cover plate removal requires turning in the counter clockwise direction. After installation, inspect all sprinklers to ensure that there is a gap between the cover plate and ceiling and that the four cup slots are open and free from any air flow impedi- ment to the space above. Concealed cover plate/cup assemblies are listed only for use with specific sprinklers. The use of any other concealed cover plate/cup assembly with the Model Fl FA56 Pendent Sprinkler or the use of the Model COP Concealed cover plate assembly on any sprinkler with which it is not specifi- cally listed my prevent good fire protection and will void all guarantees, warranties, listings and approvals. Glass bulb sprinklers have orange bulb protectors to minimize bulb damage during shipping, handling and in- stallation. REMOVE THIS PROTECTION AT THE TIME THE SPRINKLER SYSTEM IS PLACED IN SERVICE FOR FIRE PROTECTION. Removal of the protectors before this time may leave the bulb vulnerable to damage. RASCO wrench- es are designed to install sprinklers when covers are in place. REMOVE PROTECTORS BY UNDOING THE CLASP BY HAND. DO NOT USE TOOLS TO REMOVE THE PRO- TECTORS. Temperature Ratings Sprinkler mbient Classification Max.+ e mp Bulb Color °C OF Ordinary 57 135 100°F (38°C) Orange Ordinary 68 155 100°F (38°C) Red Intermediate 79 175 150°F (66°C) Yellow Intermediate 93 200 150°F (66°C) Green _jli2_ _1t ? 2EJQ?c1 Btye Not available for recessed sprinklers Escutcheon Data (1) SIN RA1435 -cULus permits use with Fl, F2 or FP escutcheons for 'light hazard" only, while FM limits use for same hazard with F2 escutcheon only. Maintenance The Model F1FR56, F1FR56LL, F1FR42, F1FR42LL, F1FAXLH and Model F1FR56, F1FR56LL, F1FR42, F1FR42LL, F1FRXLH & F1FR28 Recessed Sprinklers should be inspected quarterly and the sprinkler system maintained in accordance with NFPA 25. Do not clean sprinklers with soap and water, ammonia or any other cleaning fluids. Remove dust by using a soft brush or gentle vacuuming. Remove any sprinkler which has been painted (other than factory applied) or damaged in any way. A stock of spare sprinklers should be maintained to allow quick replacement of damaged or operated sprinklers. Prior to installation, sprinklers should be maintained in the original cartons and packaging to minimize the potential for damage to sprinklers that would cause improper operation or non-operation. Sprinkler Types Standard Upright Standard Pendent Conventional Recessed Pendent Vertical Sidewall Horizontal Sidewall Recessed Horizontal sidewall Concealed pendent Maximum Working Pressure 175 psi (12 bar) 100% Factory tested hydrostatically to 500 psi (34.5 bar) Finishes (1) ndard CoverEscutcheon I Bronze Brass Chrome Plated Chrome Chrome Polyester Plated White Stecial Aoblication Finishes I Bright Brass 0) Bright Brass Bright Brass / Black Plated Black Plated Satin Black Paint ° Black Paint Off White I Off White Off White Black Paint Sa tin Chrome .LacKJ ------- Other finishes and colors are available on special order. Consult the factory for details. Custom color painted sprinklers may not retain their UL Corrosion resistance listing. Coverplate custom paint is semi-gloss, unless specified otherwise. cLiLus Listed only. ) 200°F (93°C) maximum. ° cULus listed corrosion resistance applies to SIN Numbers RA1435 (HSW), RA1485(VSW), R.11425 (Upright), RA1414 (Pendent) and lR.A1415 (Pendent) in standard black or white. Corrosion resistance in other polyester colors is available upon request. FM Approvals finish as "Polyester coated" applies to SIN Number RA1414, RA1435 and RA1425 in standard black or white. 5LPCB and VdS Approved finish applies only to RA1425, RA1414and 8A1475. Ordering Information Specify: 1 Sprinkler Model Sprinkler Type Orifice Size Deflector Type Temperature Rating Sprinkler Finish Escutcheon Type Escutcheon Finish (where applicable) 9 Cover plate Model Cover plate Thread size Cover plate Temperature Cover plate Adjustment Cover plate Finish Note: When Model F1FR56 Recessed sprinklers are ordered, the sprinklers and escutcheons are packaged separately. 7. tieliable...For . CompleteiProtection Reliable offers a wide selection of sprinkler components. Following are some of the many precision-made Reliable products that guard life and property from fire around the clock. Automatic sprinklers Flush automatic sprinklers Recessed automatic sprinklers Concealed automatic sprinklers Adjustable automatic sprinklers Dry automatic sprinklers Intermediate level sprinklers Open sprinklers Spray nozzles Alarm valves Retarding chambers Dry pipe valves Accelerators for dry pipe valves Mechanical sprinkler alarms Electrical sprinkler alarm switches Water flow detectors Deluge valves Detector check valves Check valves Electrical system Sprinkler emergency cabinets Sprinkler wrenches Sprinkler escutcheons and guards Inspectors test connections Sight drains Ball drips and drum drips Control valve seals Air maintenance devices Air compressors Pressure gauges Identification signs Fire department connection The equipment presented in this bulletin is to be instated in accordance with the latest published Standards of the National Fire Protecton Association, Factory Mutual Research Corporation, or other similar organizations and also with the provisions of governmental codes or ordinances whenever applicable. Products manufactured and distributed by Reliable have been protecting life and property for over 90 years, and are installed and serviced by the most highly qualified and reputable sprinkler contractors located throughout the United States. Canada and foreign countries. Manufactured by The Reliable Automatic Sprinkler Co., Inc. Recycled (800) 431-1588 Sales Offices Paper Heli"abl (800) 848-6051 Sales Fax Revision lines indicate updated or new data. (914) 829-2042 Corporate Offices www.reliablesprinkler.com Internet Address LG. Printed in U.S.A. 02/13 Pfttca3970Tf,