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150 JUNIPER AVE; ; AS120058; Permit
9/14/22,10:24 AM AS120058 Permit Data City of Carlsbad Sprinkler Permit Permit No: AS120058 Job Address: 150 JUNIPER AV Permit Type: SPRINK Parcel No: 2042320700 Lot #: 0 Reference No.: Status: APPROVED Applied 6/6/2012 Approved: 6/6/2012 Issued: 6/6/2012 PC #: Inspector: Project Title: BARELMANN RESIDENCE New 13D fire sprinkler system install Applicant: INNOVATIVE FIRE PROTECTION SUITE 101 8779 COTTONWOOD AV SANTEE, CA (619) 593-8200 (619)593-9133 Owner: BARELMANN ROBERT H&MARGARET L P0 BOX 1698 CARLSBAD CA Fees ($) Add'l Fees ($) Total ($) Balance 393 ($) 1 0 393 0 about:blank 1/1 Barelman Residence Review Comments. Page 2 Review Comments Barelman Residence, 150 Juniper Avenue, Carlsbad, CA The following comments are for your information and will appear on every residential sprinkler review. The alarm bell must be capable of being heard, above background noise, with doors closed, in all living areas of the residence. This will be checked at final acceptance. Pressure required at base of riser will be verified to be available at time of final acceptance. Sprinkler heads are omitted from bathroom areas under 55 SF in area with noncombustible plumbing fixtures. Fixtures will be verified at final acceptance. Sprinkler head blockage or pattern disruption caused by beams or other obstructions will be verified to not exist at final acceptance inspection. Sprinkler heads should be located the proper distance from heat sources (stoves, kitchen ranges, fireplaces, heat diffusers, etc.) This will be checked at final acceptance inspection. Sprinkler heads located in an unconditioned space (garage, water heater closet, etc.) should be fast response type with an appropriate temperature rating, commercial heads are acceptable in these areas. All exposed piping shall be black steel or copper. Concealed piping can be CPVC plastic. il SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 5/7/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4774.SDF JOB TITLE: BARELMANN RESIDENCE TWO HEAD CALC-2nd FLOOR WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D 0 NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) 1 72.0 66.6 500.0 72.0 31.2 56.7 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 31.2 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 5.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 26.2 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 0.0 SOURCE 56.7 31.2 2 0.0 - - - - 43.8 - - - 2A 0.0 - - - - 39.8 3A 0.0 HOSE STREAM 39.6 5.0 DC 0.0 - - - - 37.5 - - - VA 0.0 - - - - 31.5 U.1 0..0 - - - - 29.8 - - - 3B 0.0 - - - - 28.1 3 3.5 - - - - 25.4 - - - 4 6.5 - - - - 22.4 5 9.5 - - - - 18.0 - - - 6 19.0 - - - - 12.8 - - - 7 19.0 - - - - 12.3 - - - 7A 18.5 - - - - 12.5 8 19.0 - - - - 11.2 - - - 9 19.0 - - - - 9.5 - - - 9A 18.5 K= 4.30 9.5 13.2 10A 18.5 K= 4.30 9.1 13.0 11 19.0 - - - - 11.7 - - - 12 9.5 - - - - 16.8 his heel revir\¼ ed ho opitci it L oiitptiiiice il ewicilt app eahir codes and it lice the ii iitetii 1he 1 1vitr Ot. colt aCil i llta\ t011/i liii ret o It slopOFt ii iii appltctttolt lot .1 ntltliitI 01111 tIC \fllCS uttdcrstil1ttt ihtt this irs i\ relics Ct the owiter 0i their pits ii hal CllCiiiCCF or whited toi sole respitttSt'1Y 5oitt1iliitttCC with said codes aitd siandarik. tictidilig hr hitdtltg code or tot itt) spoitsihittY or dettdiItL1L'. roiS. oil 01 ttegtie0 ill thesc plaits witettiri ot. at noted ill this evieW t)aie:.5f1 / Ret tew44fr" Rid )M i5th.Nl) API'ROVAt. R ItC( )MMhN1 APPRtJVAl. AS Not F-A) I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 5/7/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4774.SDF JOB TITLE: BARELMANN RESIDENCE TWO HEAD CALC-2nd FLOOR PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 1 31.2 0.995 PL 40.00 PF 12.8 1 0.0 SRCE 56.7 (N/A) 12.9 150 FTG TLG PH 0.0 2 0.0 0.0 43.8 0.0 0.254 TL 50.50 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE 2 0.0 0.0 43.8 0.0 4.0 psi, 31.2 gpm 2A 0.0 0.0 39.8 0.0 Pipe: 3 31.2 1.025 FL 1.00 PF 0.2 2A 0.0 0.0 39.8 0.0 12.1 150 FTG ---- PE 0.0 3A 0.0 H.S. 39.6 5.0 0.220 TL 1.00 PV Pipe: 4 26.2 1.025 FL 2.00 PF 2.1 3A 0.0 H.S. 39.6 5.0 10.2 150 FTG ET PE 0.0 DC 0.0 0.0 37.5 0.0 0.159 TL 13.00 PV Pipe: 5 FIXED PRESSURE LOSS DEVICE DC 0.0 0.0 37.5 0.0 6.0 psi, 26.2 gpm VA 0.0 0.0 31.5 0.0 Pipe: 6 26.2 1.360 PL 35.00 PF 1.7 VA 0.0 0.0 31.5 0.0 5.8 150 FTG 4L FE 0.0 U.1 0.0 0.0 29.8 0.0 0.040 TL 43.00 PV Pipe: 7 26.2 1.025 PL 5.00 PF 1.8 U.1 0.0 0.0 29.8 0.0 10.2 150 FTG 2E PE 0.0 3B 0.0 0.0 28.1 0.0 0.159 TL 11.00 PV Pipe: 8 26.2 1.101 FL 3.00 PF 1.1 3B 0.0 0.0 28.1 0.0 8.8 150 FTG H PE -1.5 3 3.5 0.0 25.4 0.0 0.112 TL 10.00 PV Pipe: 9 26.2 1.049 PL 3.00 FE' 1.7 3 3.5 0.0 25.4 0.0 9.7 120 FTG C PE -1.3 4 6.5 0.0 22.4 0.0 0.215 TL 8.00 PV Pipe: 10 26.2 1.101 FL 17.50 PF 3.1 4 6.5 0.0 22.4 0.0 8.8 150 FTG E3R FE -1.3 5 9.5 0.0 18.0 0.0 0.112 TL 27.50 PV Pipe: 11 15.8 1.101 FL 11.00 PF 1.1 5 9.5 0.0 18.0 0.0 5.3 150 FTG ET2R PH -4.1 6 19.0 0.0 12.8 0.0 0.044 TL 25.00 PV Pipe: 12 15.8 1.101 FL 4.50 PF 0.5 6 19.0 0.0 12.8 0.0 5.3 150 FTG TR PH 0.0 7 19.0 0.0 12.3 0.0 0.044 TL 10.50 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 5/7/2012 C:\PROGRI\N FILES\I-IRS SYSTEMS\HASS82\C4774.SDF JOB TITLE: BARELMANN RESIDENCE TWO HEAD CALC-2nd FLOOR PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 13 0.0 1.101 PL 5.00 PF 0.0 7 19.0 0.0 12.3 0.0 0.0 150 FTG ETR PE 0.2 7A 18.5 0.0 12.5 0.0 0.000 TL 18.00 PV Pipe: 14 15.8 1.101 PL 20.50 PF 1.2 7 19.0 0.0 12.3 0.0 5.3 150 FTG 6R PE 0.0 8 19.0 0.0 11.2 0.0 0.044 TL 26.50 PV Pipe: 15 26.2 1.101 PL 3.00 PF 1.7 8 19.0 0.0 11.2 0.0 8.8 150 FTG ET PE 0.0 9 19.0 0.0 9.5 0.0 0.112 TL 15.00 PV Pipe: 16 13.2 1.101 PL 0.50 PF 0.2 9 19.0 0.0 9.5 0.0 4.5 150 FTG TR PE 0.2 9A 18.5 4.3 9.5 13.2 0.032 TL 6.50 PV Pipe: 17 13.0 1.101 PL 9.75 PF 0.5 9 19.0 0.0 9.5 0.0 4.4 150 FTG ER PE 0.2 10A 18.5 4.3 9.1 13.0 0.031 TL 17.75 PV Pipe: 18 -10.4 1.101 PL 20.00 PF 0.6 8 19.0 0.0 11.2 0.0 3.5 150 FTG E2R PE 0.0 11 19.0 0.0 11.7 0.0 0.020 TL 29.00 PV Pipe: 19 -10.4 1.101 PL 16.00 PF 0.9 11 19.0 0.0 11.7 0.0 3.5 150 FTG 3ET2R PE 4.1 12 9.5 0.0 16.8 0.0 0.020 TL 44.00 PV Pipe: 20 -10.4 1.101 PL 46.00 PF 1.3 12 9.5 0.0 16.8 0.0 3.5 150 FTG 2T6R PE 0.0 5 9.5 0.0 18.0 0.0 0.020 TL 62.00 PV NOTES (HASS): Calculations were performed by the HASS 8.2 computer program under license no. 16080621 granted by HRS Systems, Inc. 208 South Public Square Petersburg, TN 37144 (931) 659-9760 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 0.009 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 12.9 ft/sec at pipe 1. Items listed in bold print on the cover sheet SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 5/7/2012 C:\PROGRPN FILES\HRS SYSTEMS\HASS82\C4774.SDF JOB TITLE: BARELMANN RESIDENCE TWO HEAD CALC-2nd FLOOR are automatically transferred from the calculation report. (5) PIPE FITTINGS TABLE Pipe Table Name: FSS.PIP PAGE: A MATERIAL: SCJ-i40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) B T L C B G A D Ell Tee 1.049 2.00 5.00 2.00 5.00 6.00 1.00 1.00 1.00 PAGE: H MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) B T R K C L B L Ell Tee TEERUN COUPLG EL45 1.101 7.00 5.00 1.00 0.00 1.00 1.00 0.00 1.00 PAGE: I MATERIAL: CPPR-L HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D Eli Tee 1.025 3.00 8.00 2.00 8.00 2.00 2.00 0.00 0.00 PAGE: J MATERIAL: S40PVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D Eli Tee 1.360 5.00 9.00 2.00 11.00 6.00 2.00 0.00 0.00 PAGE: K MATERIAL: CPPR-K HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) B T L C B G A D Ell Tee L 0.995 2.00 6.00 1.50 0.00 0.00 3.00 0.00 0.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 5/7/2012 C:\PROGRAN FILES\HRS SYSTEMS\HASS82\C4774.SDF JOB TITLE: BARELMANN RESIDENCE TWO HEAD CALC-2nd FLOOR WATER SUPPLY ANALYSIS Static: 72.00 psi Resid: 66.60 psi Flow: 500.0 gpm NO 70 1-C 60.0 G A 2 U G 50.0 E P 40.0 R E S 30.0 S U R E 20.0 LEGEND Available pressure 71.97 psi @ 31.2 gpm Required pressure 56.67 psi @ 31.2 gpm Source Supply Curve System Demand Curve p 10.0 5 1 0.0 200300 400 500 600 700 800 900 1000 FLOW (GEM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 5/7/2012 C:\PROGRPM FILES\HRS SYSTEMS\HASS82\C4774.SDF JOB TITLE: BARELMANN RESIDENCE ONE HEAD CALC-2nd FLOOR 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 72.0 66.6 500.0 72.0 26.0 61.4 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 26.0 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 5.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 21.0 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 0.0 SOURCE 61.4 26.0 2 0.0 - - - - 52.3 - - - 2A 0.0 - - - - 48.3 - - - 3A 0.0 HOSE STREAM 48.2 5.0 DC 0.0 - - - - 46.8 VA 0.0 - - - - 40.8 U.1 0.0 - - - - 39.6 - - - 3B 0.0 - - - - 38.5 3 3.5 - - - - 36.2 - - - 4 6.5 - - - - 33.8 - - - 5 9.5 - - - - 30.4 6 19.0 - - - - 25.4 - - - 7 19.0 - - - - 25.0 7A 18.5 K= 4.30 23.8 21.0 8 19.0 - - - - 25.2 9 19.0 - - - 25.2 - - - 9A 18.5 - - - - 25.4 - - - bA 18.5 - - - - 25.4 11 19.0 - - - - 25.4 12 9.5 - - - - 29.9 4 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 5/7/2012 C:\FROGRAM FILES\HRS SYSTEMS\HASS82\C4774.SDF JOB TITLE: BARELMANN RESIDENCE ONE HEAD CALC-2nd FLOOR 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 26.0 0.995 FL 40.00 PF 9.1 1 0.0 SRCE 61.4 (N/A) 10.7 150 FTG TLG FE 0.0 2 0.0 0.0 52.3 0.0 0.181 TL 50.50 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE 2 0.0 0.0 52.3 0.0 4.0 psi, 26.0 gpm 2A 0.0 0.0 48.3 0.0 Pipe: 3 26.0 1.025 PL 1.00 PF 0.2 2A 0.0 0.0 48.3 0.0 10.1 150 FTG --- PE 0.0 3A 0.0 H.S. 48.2 5.0 0.157 TL 1.00 PV Pipe: 4 21.0 1.025 FL 2.00 PF 1.4 3A 0.0 H.S. 48.2 5.0 8.2 150 FTG ET PE 0.0 DC 0.0 0.0 46.8 0.0 0.105 TL 13.00 PV Pipe: 5 FIXED PRESSURE LOSS DEVICE DC 0.0 0.0 46.8 0.0 6.0 psi, 21.0 gpm VA 0.0 0.0 40.8 0.0 Pipe: 6 21.0 1.360 FL 35.00 PF 1.1 VA 0.0 0.0 40.8 0.0 4.6 150 FTG 4L PE 0.0 U.1 0.0 0.0 39.6 0.0 0.027 TL 43.00 PV Pipe: 7 21.0 1.025 FL 5.00 PF 1.2 U.1 0.0 0.0 39.6 0.0 8.2 150 FTG 2E FE 0.0 3B 0.0 0.0 38.5 0.0 0.105 TL 11.00 PV Pipe: 8 21.0 1.101 FL 3.00 PF 0.7 3B 0.0 0.0 38.5 0.0 7.1 150 FTG E PE -1.5 3 3.5 0.0 36.2 0.0 0.074 TL 10.00 PV Pipe: 9 21.0 1.049 PL 3.00 PF 1.1 3 3.5 0.0 36.2 0.0 7.8 120 FTG C FE -1.3 4 6.5 0.0 33.8 0.0 0.142 TL 8.00 PV Pipe: 10 21.0 1.101 FL 17.50 PF 2.0 4 6.5 0.0 33.8 0.0 7.1 150 FTG E3R FE -1.3 5 9.5 0.0 30.4 0.0 0.074 TL 27.50 PV Pipe: 11 14.6 1.101 FL 11.00 PF 0.9 5 9.5 0.0 30.4 0.0 4.9 150 FTG ET2R FE -4.1 6 19.0 0.0 25.4 0.0 0.038 TL 25.00 PV Pipe: 12 14.6 1.101 FL 4.50 PF 0.4 6 19.0 0.0 25.4 0.0 4.9 150 FTG TR FE 0.0 7 19.0 0.0 25.0 0.0 0.038 TL 10.50 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 5/7/2012 C:\PROGRAN FILES\HRS SYSTEMS\HASS82\C4774.SDF JOB TITLE: BARELMANN RESIDENCE ONE HEAD CALC-2nd FLOOR PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 13 21.0 1.101 PL 5.00 PF 1.3 7 19.0 0.0 25.0 0.0 7.1 150 FTG ETR PE 0.2 7A 18.5 4.3 23.8 21.0 0.074 TL 18.00 PV Pipe: 14 -6.4 1.101 PL 20.50 PF 0.2 7 19.0 0.0 25.0 0.0 2.2 150 FTG 6R PE 0.0 8 19.0 0.0 25.2 0.0 0.008 TL 26.50 PV Pipe: 15 0.0 1.101 FL 3.00 PF 0.0 8 19.0 0.0 25.2 0.0 0.0 150 FTG ET PE 0.0 9 19.0 0.0 25.2 0.0 0.000 TL 15.00 PV Pipe: 16 0.0 1.101 PL 0.50 PF 0.0 9 19.0 0.0 25.2 0.0 0.0 150 FTG TR PE 0.2 9A 18.5 0.0 25.4 0.0 0.000 TL 6.50 PV Pipe: 17 0.0 1.101 FL 9.75 PF 0.0 9 19.0 0.0 25.2 0.0 0.0 150 FTG ER PE 0.2 bA 18.5 0.0 25.4 0.0 0.000 TL 17.75 PV Pipe: 18 -6.4 1.101 PL 20.00 PF 0.2 8 19.0 0.0 25.2 0.0 2.2 150 FTG E2R FE 0.0 11 19.0 0.0 25.4 0.0 0.008 TL 29.00 PV Pipe: 19 -6.4 1.101 FL 16.00 PF 0.4 11 19.0 0.0 25.4 0.0 2.2 150 FTG 3ET2R PE 4.1 12 9.5 0.0 29.9 0.0 0.008 TL 44.00 PV Pipe: 20 -6.4 1.101 PL 46.00 PF 0.5 12 9.5 0.0 29.9 0.0 2.2 150 FTG 2T6R PE 0.0 5 9.5 0.0 30.4 0.0 0.008 TL 62.00 PV NOTES (HASS): Calculations were performed by the HASS 8.2 computer program under license no. 16080621 granted by HRS Systems, Inc. 208 South Public Square Petersburg, TN 37144 (931) 659-9760 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 0.019 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 10.7 ft/sec at pipe 1. Items listed in bold print on the cover sheet 4 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 5/7/2012 C:\PROGRAJ4 FILES\HRS SYSTEMS\HASS82\C4774.SDF JOB TITLE; BARELMANN RESIDENCE ONE HEAD CALC--2nd FLOOR are automatically transferred from the calculation report. (5) PIPE FITTINGS TABLE Pipe Table Name: FSS.PIP PAGE: A MATERIAL: SCH40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D Eli Tee 1.049 2.00 5.00 2.00 5.00 6.00 1.00 1.00 1.00 PAGE: H MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T R K C L B L Ell Tee TEERUN COUPLG EL45 1.101 7.00 5.00 1.00 0.00 1.00 1.00 0.00 1.00 PAGE: I MATERIAL: CPPR-L HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D Ell Tee 1.025 3.00 8.00 2.00 8.00 2.00 2.00 0.00 0.00 PAGE: J MATERIAL: S40PVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D Eli Tee 1.360 5.00 9.00 2.00 11.00 6.00 2.00 0.00 0.00 PAGE: K MATERIAL: CPPR-K HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D Ell Tee L 0.995 2.00 6.00 1.50 0.00 0.00 3.00 0.00 0.00 41 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 5/7/2012 C:\PROGRAN FILES\HRS SYSTEMS\HASS82\C4774.SDF JOB TITLE: BARELMPNN RESIDENCE ONE HEAD CALC-2nd FLOOR WATER SUPPLY ANALYSIS Static: 72.00 psi Resid: 66.60 psi Flow: 500.0 gpm 7010 6020 G A U G 50.0 E P 40.0 R B 30.0 S U R E 20.0 LEGEND Available pressure 71.98 psi @ 26.0 gpm Required pressure 61.44 psi @ 26.0 gpm Source Supply Curve System Demand Curve p 10.0 5 i 0.0 -14.7 200300 400 500 600 700 800 900 1000 FLOW (GPM)