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HomeMy WebLinkAbout5803 NEWTON DR; D; FPC2021-0246; PermitPR]LT REPORT (Ccity of Carlsbad Print Date: 03/24/2025 Permit No: FPC2021-0246 Job Address: 5803 NEWTON DR, # D, CARLSBAD, CA 92008-7380 Status: Closed - Finaled Permit Type: FIRE-Construction Commercial Work Class: Fire Sprinklers Parcel #: 2121304800 Track t: Applied: 12/30/2021 Valuation: $23,885.00 Lot #: Issued: 03/01/2022 Occupancy Group: Project #: Finaled Close Out: 08/17/2022 #of Dwelling Units: Plan #: Bedrooms: Construction Type: Final Inspection: Bathrooms: Orig. Plan Check 4*: INSPECTOR: Salcedo, Felix Plan Check 4*: Project Title: Description: THERMO FISHER -INSTALL 2 LEVELS OF FIRE SPRINKLERS IN WAREHOUSE RACKS (56 HEADS) FPContractor: MIKE L H UANTE JR 2610 5 HACIENDA BLVD HACIENDA HEIGHTS, CA 91745-5321 (323) 864-3238 FEE AMOUNT FIRE NFPA 13 or 13R System 7-100 heads $607.00 FIRE Plan Resub (3rd&Subsequerit Submittal/hr) $372.50 Total Fees: $979.50 Total Payments To Date: $979.50 Balance Due: $0.00 Fire Department Page 1 of 1 1635 Faraday Avenue, Carlsbad CA 92008-7314 1442-339-2665 1 Inspections: 442-339-2660 1 www.carlsbadca.gov HYDRAULIC CALCULATIONS FOR 5803 NEWTON DRIVE CARLSBAD,CA, 92008 ADDED IN-RACK BALANCED TO CEILING SYSTEM CALCULATION DRAWING NUMBER:FS-1 THRU FS-4 DATE: DEC 27, 2021 -DESIGN DATA- REMOTE AREA NUMBER:RACK STORAGE AREA,.. REMOTE AREA LOCATION:TENANT OCCUPANCY CLASSIFICATION: SINGLE AND DOUBLE ROW RACK STORAGE OF GROUP-A UNEXPANDED PLASTIC UP TO 25' HEIGHT WITH 2 LEVELS OF IN-RACK SPRINKLERS. 14 IN RACK HEADS (7 EACH ROW) CALCULATED SIMULTANEOUSLY AND BALANCED TO CELING SYSTEM ABOVE RACK STORAGE AREA. PER 2019 NFPA-13 FIGURE 25.9.3.1 (d) WITH MORE THAN 15 psi PRESS. AT IN-RACK HEADS AND MINIMUM 0.3 gpm/sq.ft. EXISTING CEILING SYSTEM DENSITY OVER AN AREA EXCEEDING 2000 sq. ft. DENSITY: 0.3 gpm/sq. ft. (CEILING SYSTEM), 15.0 psi/A.S IN RACK AREA OF APPLICATION: 2104 sq. ft. (CEILIND SYSTEM) PLUS 14 IN RACK COVERAGE PER SPRINKLER: 100 sq. ft. (EXISTING CEILING SYSTEM) TYPE OF SPRINKLERS CALCULATED: STORAGE (EX. CEILING), INTERMEDIATE IN-RACK NUMBER OF SPRINKLERS CALCULATED: &NUMBER& EXISTING CEILING = 14 IN-RACK *INRACK SPRINKLER DEMAND: gpm HOSE-STREAM DEMAND:500 gpm TOTAL WATER REQUIRED (INCLUDING HOSE) : 1867.9 gpm FLOW AND PRESSURE (AT BASE OF RISER) : gpm @ psi TYPE OF SYSTEM: WET WATER SUPPLY Source:8"SITE U. G., Test Date:11-22-2021 Test By:CARSLBAD FIRE DEP. Location: HYDRANT # H61404 Static: &129& psi Residual: &88& psi Flow: &4675& gpm Source Elevation Relative to Finished Flow Level:32.5 ft. INSTALLING CONTRACTOR Name:MIKE HUANTEMJR. INC. FIRE PROTECTION Address:2610 S. HACIENDA BLVD., HACIENDA HEIGHTS, CA.,91745 Phone:323-864 3238, Certification number:676834, C16 NAME OF DESIGNER:MIKE HUANTE, MIKE HAJILOO P.E. AUTHORITY HAVING JURISDICTION: CARLSBAD FIRE DEPARTMENT NOTES: Calculations performed by HASS under license # 38011909 granted by HRS SYSTEMS, INC. (Notes continue after pipe calculations results.) (Notes continue after pipe calculations results.) (Notes continue after pipe calculations results.) • SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 12/27/2021\MIKE HUANTE\NEWTON (THERMAL FISHER) \RACK SYSTEM PROOF.SDF JOB TITLE: 5803 NEWTON DR. (RACK STORAGE AREA PROOF CALC.) WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. 8 PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) 1 116.0 79.2 4675.0 109.3 1867.9 75.3 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 1867.9 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 500.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 1367.9 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 -3.0 SOURCE 75.3 1367.9 2 0.0 - - - - 73.3 - - - DC1 2.5 - - - - 71.8 - - - DC2 2.5 - - - - 64.8 - - - 3 0.0 - - - - 65.6 - - - 4 2.0 - - - - 62.7 - - - POC 2.5 - - - - 60.5 - - - BOR 3.0 - - - - 60.1 - - - 5 29.5 - - - - 47.8 - - - 6 29.5 - - - - 42.0 - - - 7 29.5 - - - - 41.8 - - - 8 29.5 - - - - 41.8 - - - 9 29.5 - - - - 41.8 - - - 10 29.5 - - - - 41.8 - - - 11 29.5 - - - - 41.8 - - - 12 29.5 - - - - 41.8 - - - 13 29.5 - - - - 41.8 - - - 14 29.5 - - - - 38.8 - - - 15 29.5 - - - - 38.7 - - - 16 29.5 - - - - 38.7 - - - 17 29.5 - - - - 38.7 - - - 18 29.5 - - - - 38.6 - - - 19 29.5 - - - - 38.5 - - - 20 29.5 - - - - 38.3 - - - 21 29.5 - - - - 38.0 - - - 22 29.5 - - - - 37.7 - - - 23 29.5 - - - - 37.3 - - - 24 29.5 - - - - 36.9 - - - 25 29.5 - - - - 36.6 - - - 26 29.5 - - - - 36.4 - - - 27 29.5 - - - - 36.4 - - - 28 29.5 - - - - 36.4 - - - 29 29.5 - - - - 36.4 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 12/27/2021\MIKE HUANTE\NEWTON (THERMAL FISHER) \RACK SYSTEM PROOF.SDF JOB TITLE: 5803 NEWTON DR. (RACK STORAGE AREA PROOF CALC.) NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 30 29.5 - - - - 40.9 - - - 31 29.5 - - - - 40.9 - - - 32 29.5 - - - - 40.9 - - - 33 29.5 - - - - 40.9 - - - 34 29.5 - - - - 41.0 - - - 35 29.5 - - - - 41.0 - - - 36 29.5 - - - - 41.1 - - - 37 29.5 - - - - 41.2 - - - 38 29.5 - - - - 41.4 - - - 51 29.5 K= 8.20 29.8 44.8 S2 29.5 K= 8.20 29.3 44.4 S3 29.5 K= 8.20 29.2 44.3 S4 29.5 K= 8.20 29.4 44.4 S5 29.5 K= 8.20 29.9 44.9 S6 29.5 K= 8.20 30.2 45.1 S7 29.5 K= 8.20 29.8 44.8 S8 29.5 K= 8.20 29.7 44.7 S9 29.5 K= 8.20 29.7 44.7 sio 29.5 K= 8.20 30.0 44.9 S11 29.5 K= 8.20 30.9 45.6 S12 29.5 K= 8.20 33.8 47.7 S13 29.5 K= 8.20 33.6 47.5 S14 29.5 K= 8.20 29.2 44.3 S15 29.5 K= 8.20 29.2 44.3 S16 29.5 K= 8.20 29.5 44.5 S17 29.5 K= 8.20 30.3 45.2 S18 29.5 K= 8.20 30.6 45.3 S19 29.5 K= 8.20 30.2 45.0 S20 29.5 K= 8.20 30.1 45.0 S21 29.5 K= 8.20 30.1 45.0 S22 29.5 K= 8.20 30.5 45.3 S23 29.5 K= 8.20 31.4 45.9 A 29.0 - - - - 47.2 - - - B 29.0 - - - - 40.8 - - - C 29.0 - - - - 36.0 - - - D 29.0 - - - - 34.3 - - - E 29.0 - - - - 23.0 - - - F 20.0 - - - - 20.1 - - - G 10.0 - - - - 22.4 - - - Ri 20.0 K= 5.60 18.6 24.2 R2 20.0 K= 5.60 18.1 23.8 R3 20.0 K= 5.60 17.9 23.7 R4 20.0 K= 5.60 16.6 22.8 R5 20.0 K= 5.60 15.6 22.1 R6 20.0 K= 5.60 15.1 21.8 R7 20.0 K= 5.60 15.0 21.7 R8 10.0 K= 5.60 20.1 25.1 R9 10.0 K= 5.60 19.5 24.8 RiO 10.0 K= 5.60 19.4 24.6 Rib 10.0 K= 5.60 19.4 24.6 R12 10.0 K= 5.60 18.2 23.9 R13 10.0 K= 5.60 17.7 23.6 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 12/27/2021\MIKE HUANTE\NEWTON(THERMAL FISHER) \RACK SYSTEM PROOF.SDF JOB TITLE: 5803 NEWTON DR. (RACK STORAGE AREA PROOF CALC.) NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) R14 10.0 K= 5.60 17.6 23.5 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 12/27/2021\MIKE HUANTE\NEWTON(THERMAL FISHER) \RACK SYSTEM PROOF.SDF JOB TITLE: 5803 NEWTON DR. (RACK STORAGE AREA PROOF 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 1367.9 8.390 PL 13.00 PF 0.8 1 -3.0 SRCE 75.3 (N/A) 7.9 140 FTG TG PE -1.3 2 0.0 0.0 73.3 0.0 0.010 TL 79.00 PV Pipe: 2 1367.8 8.390 PL 4.00 PF 0.3 2 0.0 0.0 73.3 0.0 7.9 140 FTG E PE -1.1 DC1 2.5 0.0 71.8 0.0 0.010 TL 35.00 PV Pipe: DCDA FIXED PRESSURE LOSS DEVICE DC1 2.5 0.0 71.8 0.0 7.0 psi, 1367.8 gpm DC2 2.5 0.0 64.8 0.0 Pipe: SUP 1367.8 8.390 PL 4.00 PF 0.3 DC2 2.5 0.0 64.8 0.0 7.9 140 FTG H PE 1.1 3 0.0 0.0 65.6 0.0 0.010 TL 35.00 PV Pipe: 3 1367.8 8.390 PL 115.00 PF 2.0 3 0.0 0.0 65.6 0.0 7.9 140 FTG 3E PE -0.9 4 2.0 0.0 62.7 0.0 0.010 TL 208.00 PV Pipe: CON 1367.8 6.357 PL 2.00 PF 2.0 4 2.0 0.0 62.7 0.0 13.8 120 FTG T PE -0.2 POC 2.5 0.0 60.5 0.0 0.050 TL 40.00 PV Pipe: EXRIS 1037.7 6.357 PL 2.00 PF 0.2 POC 2.5 0.0 60.5 0.0 10.5 120 FTG G PE -0.2 BOR 3.0 0.0 60.1 0.0 0.030 TL 6.00 PV Pipe: 4 1037.7 6.357 PL 27.00 PF 0.8 BOR 3.0 0.0 60.1 0.0 10.5 120 FTG ---- PE -11.5 5 29.5 0.0 47.8 0.0 0.030 TL 27.00 PV Pipe: 5 1037.7 6.357 PL 175.00 PF 5.8 5 29.5 0.0 47.8 0.0 10.5 120 FTG E PE 0.0 6 29.5 0.0 42.0 0.0 0.030 TL 193.00 PV Pipe: 6 325.9 6.357 PL 6.50 PF 0.2 6 29.5 0.0 42.0 0.0 3.3 120 FTG T PE 0.0 7 29.5 0.0 41.8 0.0 0.004 TL 44.50 PV Pipe: 7 276.5 6.357 PL 10.00 PF 0.0 7 29.5 0.0 41.8 0.0 2.8 120 FTG ---- PE 0.0 8 29.5 0.0 41.8 0.0 0.003 TL 10.00 PV Pipe: 7A 49.4 2.157 PL 148.00 PF 3.6 7 29.5 0.0 41.8 0.0 4.3 120 FTG 2T PE 0.0 20 29.5 0.0 38.3 0.0 0.021 TL 172.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 12/27/2021\MIKE HUANTE\NEWTON(THERMAL FISHER) \RACK SYSTEM PROOF.SDF JOB TITLE: 5803 NEWTON DR. (RACK STORAGE AREA PROOF 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: 8 228.7 6.357 PL 10.00 PF 0.0 8 29.5 0.0 41.8 0.0 2.3 120 FTG PE 0.0 9 29.5 0.0 41.8 0.0 0.002 TL 10.00 PV Pipe: 8A 47.8 2.157 PL 148.00 PF 3.4 8 29.5 0.0 41.8 0.0 4.2 120 FTG 2T FE 0.0 19 29.5 0.0 38.5 0.0 0.020 TL 172.00 PV Pipe: 9 182.0 6.357 FL 10.00 PF 0.0 9 29.5 0.0 41.8 0.0 1.8 120 FTG ---- PE 0.0 10 29.5 0.0 41.8 0.0 0.001 TL 10.00 PV Pipe: 9A 46.7 2.157 FL 148.00 PF 3.2 9 29.5 0.0 41.8 0.0 4.1 120 FTG 2T PE 0.0 18 29.5 0.0 38.6 0.0 0.019 TL 172.00 PV Pipe: 10 136.0 6.357 PL 10.00 PF 0.0 10 29.5 0.0 41.8 0.0 1.4 120 FTG ---- FE 0.0 11 29.5 0.0 41.8 0.0 0.001 TL 10.00 PV Pipe: bA 45.9 2.157 PL 148.00 PF 3.1 10 29.5 0.0 41.8 0.0 4.0 120 FTG 2T FE 0.0 17 29.5 0.0 38.7 0.0 0.018 TL 172.00 PV Pipe: 11 90.5 6.357 PL 10.00 PF 0.0 11 29.5 0.0 41.8 0.0 0.9 120 FTG ---- FE 0.0 12 29.5 0.0 41.8 0.0 0.000 TL 10.00 PV Pipe: hA 45.5 2.157 PL 148.00 PF 3.1 11 29.5 0.0 41.8 0.0 4.0 120 FTG 2T FE 0.0 16 29.5 0.0 38.7 0.0 0.018 TL 172.00 PV Pipe: 12 45.2 6.357 FL 10.00 PF 0.0 12 29.5 0.0 41.8 0.0 0.5 120 FTG ---- PE 0.0 13 29.5 0.0 41.8 0.0 0.000 TL 10.00 PV Pipe: 12A 45.3 2.157 FL 148.00 PF 3.0 12 29.5 0.0 41.8 0.0 4.0 120 FTG 2T PE 0.0 15 29.5 0.0 38.7 0.0 0.018 TL 172.00 PV Pipe: 13 45.2 2.157 PL 148.00 PF 3.0 13 29.5 0.0 41.8 0.0 4.0 120 FTG 2T PE 0.0 14 29.5 0.0 38.8 0.0 0.018 TL 172.00 PV Pipe: 14 45.2 4.260 PL 10.00 PF 0.0 14 29.5 0.0 38.8 0.0 1.0 120 FTG ---- PE 0.0 15 29.5 0.0 38.7 0.0 0.001 TL 10.00 PV Pipe: 15 90.5 4.260 PL 10.00 PF 0.0 15 29.5 0.0 38.7 0.0 2.0 120 FTG ---- PE 0.0 16 29.5 0.0 38.7 0.0 0.002 TL 10.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 12/27/2021\MIKE HUANTE\NEWTON (THERMAL FISHER) \RACK SYSTEM PROOF.SDF JOB TITLE: 5803 NEWTON DR. (RACK STORAGE AREA PROOF 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: 16 136.0 4.260 PL 10.00 PF 0.0 16 29.5 0.0 38.7 0.0 3.1 120 FTG ---- PE 0.0 17 29.5 0.0 38.7 0.0 0.005 TL 10.00 PV Pipe: 17 182.0 4.260 PL 10.00 PF 0.1 17 29.5 0.0 38.7 0.0 4.1 120 FTG ---- PE 0.0 18 29.5 0.0 38.6 0.0 0.008 TL 10.00 PV Pipe: 18 228.7 4.260 PL 10.00 PF 0.1 18 29.5 0.0 38.6 0.0 5.1 120 FTG ---- PE 0.0 19 29.5 0.0 38.5 0.0 0.013 TL 10.00 PV Pipe: 19 276.5 4.260 PL 10.00 PF 0.2 19 29.5 0.0 38.5 0.0 6.2 120 FTG ---- PE 0.0 20 29.5 0.0 38.3 0.0 0.018 TL 10.00 PV Pipe: 20 325.9 4.260 PL 10.00 PF 0.2 20 29.5 0.0 38.3 0.0 7.3 120 FTG ---- PE 0.0 21 29.5 0.0 38.0 0.0 0.025 TL 10.00 PV Pipe: 21 370.4 4.260 PL 10.00 PF 0.3 21 29.5 0.0 38.0 0.0 8.3 120 FTG ---- PE 0.0 22 29.5 0.0 37.7 0.0 0.031 TL 10.00 PV Pipe: 22 416.2 4.260 PL 10.00 PF 0.4 22 29.5 0.0 37.7 0.0 9.4 120 FTG ---- PE 0.0 23 29.5 0.0 37.3 0.0 0.039 TL 10.00 PV Pipe: 23 463.8 4.260 PL 10.00 PF 0.5 23 29.5 0.0 37.3 0.0 10.4 120 FTG ---- PE 0.0 24 29.5 0.0 36.9 0.0 0.047 TL 10.00 PV Pipe: 24 335.1 4.260 PL 10.00 PF 0.3 24 29.5 0.0 36.9 0.0 7.5 120 FTG ---- PE 0.0 25 29.5 0.0 36.6 0.0 0.026 TL 10.00 PV Pipe: 24A 128.7 2.157 PL 33.00 PF 6.9 24 29.5 0.0 36.9 0.0 11.3 120 FTG 2T PH 0.0 S5 29.5 8.2 29.9 44.9 0.122 TL 57.00 PV Pipe: 25 184.3 4.260 PL 14.00 PF 0.2 25 29.5 0.0 36.6 0.0 4.1 120 FTG E PE 0.0 26 29.5 0.0 36.4 0.0 0.009 TL 27.00 PV Pipe: 25A 150.9 2.157 PL 23.00 PF 5.7 25 29.5 0.0 36.6 0.0 13.2 120 FTG T PE 0.0 Sli 29.5 8.2 30.9 45.6 0.163 TL 35.00 PV Pipe: 26 33.7 4.260 PL 14.00 PF 0.0 26 29.5 0.0 36.4 0.0 0.8 120 FTG ---- PE 0.0 27 29.5 0.0 36.4 0.0 0.000 TL 14.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 12/27/2021\MIKE HUANTE\NEWTON (THERMAL FISHER) \RACK SYSTEM PROOF.SDF JOB TITLE: 5803 NEWTON DR. (RACK STORAGE AREA PROOF CALC.) PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) I-iW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 26A 150.6 2.157 PL 13.00 PF 6.0 26 29.5 0.0 36.4 0.0 13.2 120 FTG 2T PE 0.0 S17 29.5 8.2 30.3 45.2 0.163 TL 37.00 PV Pipe: 27 -121.4 4.260 PL 14.00 PF 0.1 27 29.5 0.0 36.4 0.0 2.7 120 FTG ---- PE 0.0 28 29.5 0.0 36.4 0.0 0.004 TL 14.00 PV Pipe: 27A 155.1 2.157 PL 5.00 PF 5.0 27 29.5 0.0 36.4 0.0 13.6 120 FTG 2T PE 0.0 S23 29.5 8.2 31.4 45.9 0.172 TL 29.00 PV Pipe: 28 -64.4 4.260 PL 14.00 PF 0.0 28 29.5 0.0 36.4 0.0 1.4 120 FTG ---- PE 0.0 29 29.5 0.0 36.4 0.0 0.001 TL 14.00 PV Pipe: 29 -64.4 2.157 PL 108.00 PF 4.5 29 29.5 0.0 36.4 0.0 5.7 120 FTG 2T PE 0.0 30 29.5 0.0 40.9 0.0 0.034 TL 132.00 PV Pipe: 30 -64.4 6.357 PL 10.00 PF 0.0 30 29.5 0.0 40.9 0.0 0.7 120 FTG ---- PE 0.0 31 29.5 0.0 40.9 0.0 0.000 TL 10.00 PV Pipe: 31 -121.4 6.357 PL 10.00 PF 0.0 31 29.5 0.0 40.9 0.0 1.2 120 FTG ---- PE 0.0 32 29.5 0.0 40.9 0.0 0.001 TL 10.00 PV Pipe: 31A 57.0 2.157 PL 118.00 PF 4.5 31 29.5 0.0 40.9 0.0 5.0 120 FTG 4T PE 0.0 28 29.5 0.0 36.4 0.0 0.027 TL 166.00 PV Pipe: 32 -237.9 6.357 PL 10.00 PF 0.0 32 29.5 0.0 40.9 0.0 2.4 120 FTG ---- PE 0.0 33 29.5 0.0 40.9 0.0 0.002 TL 10.00 PV Pipe: 33 -333.2 6.357 PL 10.00 PF 0.0 33 29.5 0.0 40.9 0.0 3.4 120 FTG ---- PE 0.0 34 29.5 0.0 41.0 0.0 0.004 TL 10.00 PV Pipe: 34 -452.1 6.357 PL 10.00 PF 0.1 34 29.5 0.0 41.0 0.0 4.6 120 FTG ---- PE 0.0 35 29.5 0.0 41.0 0.0 0.006 TL 10.00 PV Pipe: 35 -573.9 6.357 PL 10.00 PF 0.1 35 29.5 0.0 41.0 0.0 5.8 120 FTG ---- PE 0.0 36 29.5 0.0 41.1 0.0 0.010 TL 10.00 PV Pipe: 36 -621.6 6.357 PL 10.00 PF 0.1 36 29.5 0.0 41.1 0.0 6.3 120 FTG ---- PE 0.0 37 29.5 0.0 41.2 0.0 0.012 TL 10.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 12/27/2021\MIKE HUANTE\NEWTON(THERMAL FISHER) \RACK SYSTEM PROOF.SDF JOB TITLE: 5803 NEWTON DR. (RACK STORAGE AREA PROOF 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: 36A 47.6 2.157 PL 148.00 PF 3.8 36 29.5 0.0 41.1 0.0 4.2 120 FTG 4T PE 0.0 23 29.5 0.0 37.3 0.0 0.019 TL 196.00 PV Pipe: 37 -667.3 6.357 PL 10.00 PF 0.1 37 29.5 0.0 41.2 0.0 6.7 120 FTG ---- PE 0.0 38 29.5 0.0 41.4 0.0 0.013 TL 10.00 PV Pipe: 37A 45.8 2.157 PL 148.00 PP 3.5 37 29.5 0.0 41.2 0.0 4.0 120 FTG 4T PE 0.0 22 29.5 0.0 37.7 0.0 0.018 TL 196.00 PV Pipe: 38 711.8 6.357 PL 4.00 PP 0.6 6 29.5 0.0 42.0 0.0 7.2 120 FTG T PE 0.0 38 29.5 0.0 41.4 0.0 0.015 TL 42.00 PV Pipe: 38A 44.5 2.157 PL 148.00 PF 3.3 38 29.5 0.0 41.4 0.0 3.9 120 FTG 4T PE 0.0 21 29.5 0.0 38.0 0.0 0.017 TL 196.00 PV Pipe: 51 121.8 2.157 PL 78.00 PF 11.2 35 29.5 0.0 41.0 0.0 10.7 120 FTG 2T PE 0.0 51 29.5 8.2 29.8 44.8 0.110 TL 102.00 PV Pipe: S2 77.1 2.157 PL 10.00 PF 0.5 51 29.5 8.2 29.8 44.8 6.8 120 FTG ---- PE 0.0 S2 29.5 8.2 29.3 44.4 0.047 TL 10.00 PV Pipe: S3 32.7 2.157 PL 10.00 PF 0.1 S2 29.5 8.2 29.3 44.4 2.9 120 FTG ---- PE 0.0 S3 29.5 8.2 29.2 44.3 0.010 TL 10.00 PV Pipe: S4 -39.4 2.157 PL 10.00 PF 0.1 S3 29.5 8.2 29.2 44.3 3.5 120 FTG ---- PE 0.0 S4 29.5 8.2 29.4 44.4 0.014 TL 10.00 PV Pipe: S5 -83.8 2.157 PL 10.00 PF 0.6 S4 29.5 8.2 29.4 44.4 7.4 120 FTG ---- PE 0.0 S5 29.5 8.2 29.9 44.9 0.055 TL 10.00 PV Pipe: S6 118.9 2.157 PL 78.00 PF 10.7 34 29.5 0.0 41.0 0.0 10.4 120 FTG 2T PR 0.0 S6 29.5 8.2 30.2 45.1 0.105 TL 102.00 PV Pipe: S7 73.8 2.157 PL 10.00 PF 0.4 S6 29.5 8.2 30.2 45.1 6.5 120 FTG ---- PE 0.0 S7 29.5 8.2 29.8 44.8 0.044 TL 10.00 PV Pipe: S8 29.1 2.157 FL 10.00 PF 0.1 S7 29.5 8.2 29.8 44.8 2.6 120 FTG ---- PE 0.0 S8 29.5 8.2 29.7 44.7 0.008 TL 10.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 12/27/2021\MIKE HUANTE\NEWTON(THERMAL FISHER) \RACK SYSTEM PROOF.SDF JOB TITLE: 5803 NEWTON DR. (RACK STORAGE AREA PROOF 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: S9 -15.6 2.157 FL 10.00 PF 0.0 S8 29.5 8.2 29.7 44.7 1.4 120 FTG ---- FE 0.0 S9 29.5 8.2 29.7 44.7 0.002 TL 10.00 FV Pipe: Sb -60.3 2.157 FL 10.00 PF 0.3 S9 29.5 8.2 29.7 44.7 5.3 120 FTG ---- FE 0.0 S1O 29.5 8.2 30.0 44.9 0.030 TL 10.00 PV Pipe: Sli -105.3 2.157 FL 10.00 PF 0.8 Slo 29.5 8.2 30.0 44.9 9.2 120 FTG ---- PE 0.0 S11 29.5 8.2 30.9 45.6 0.084 TL 10.00 PV Pipe: S12 95.2 2.157 FL 78.00 PF 7.1 33 29.5 0.0 40.9 0.0 8.4 120 FTG 2T FE 0.0 S12 29.5 8.2 33.8 47.7 0.070 TL 102.00 PV Pipe: S13 47.5 2.157 PL 10.00 PF 0.2 S12 29.5 8.2 33.8 47.7 4.2 120 FTG ---- FE 0.0 S13 29.5 8.2 33.6 47.5 0.019 TL 10.00 PV Pipe: S14 27.7 2.157 PL 10.00 PF 0.1 S3 29.5 8.2 29.2 44.3 2.4 120 FTG ---- PE 0.0 S14 29.5 8.2 29.2 44.3 0.007 TL 10.00 PV Pipe: S15 -16.6 2.157 FL 10.00 PF 0.0 S14 29.5 8.2 29.2 44.3 1.5 120 FTG ---- PE 0.0 S15 29.5 8.2 29.2 44.3 0.003 TL 10.00 PV Pipe: S16 -60.9 2.157 PL 10.00 PF 0.3 S15 29.5 8.2 29.2 44.3 5.3 120 FTG ---- FE 0.0 S16 29.5 8.2 29.5 44.5 0.031 TL 10.00 PV Pipe: S17 -105.4 2.157 FL 10.00 PF 0.8 S16 29.5 8.2 29.5 44.5 9.3 120 FTG ---- FE 0.0 S17 29.5 8.2 30.3 45.2 0.084 TL 10.00 PV Pipe: S18 116.5 2.157 FL 78.00 PF 10.3 32 29.5 0.0 40.9 0.0 10.2 120 FTG 2T PE 0.0 S18 29.5 8.2 30.6 45.3 0.101 TL 102.00 PV Pipe: S19 71.2 2.157 FL 10.00 PF 0.4 S18 29.5 8.2 30.6 45.3 6.2 120 FTG ---- FE 0.0 S19 29.5 8.2 30.2 45.0 0.041 TL 10.00 FV Pipe: S20 26.1 2.157 PL 10.00 PF 0.1 S19 29.5 8.2 30.2 45.0 2.3 120 FTG ---- PE 0.0 S20 29.5 8.2 30.1 45.0 0.006 TL 10.00 FV Pipe: S21 -18.9 2.157 FL 10.00 PF 0.0 S20 29.5 8.2 30.1 45.0 1.7 120 FTG ---- FE 0.0 S21 29.5 8.2 30.1 45.0 0.003 TL 10.00 FV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page ii DATE: 12/27/2021\MIKE HUANTE\NEWTON (THERMAL FISHER) \RACK SYSTEM PROOF.SDF JOB TITLE: 5803 NEWTON DR. (RACK STORAGE AREA PROOF 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: S22 -63.9 2.157 PL 10.00 PF 0.3 S21 29.5 8.2 30.1 45.0 5.6 120 FTG ---- PE 0.0 S22 29.5 8.2 30.5 45.3 0.033 TL 10.00 PV Pipe: S23 -109.2 2.157 PL 10.00 PF 0.9 S22 29.5 8.2 30.5 45.3 9.6 120 FTG ---- PE 0.0 S23 29.5 8.2 31.4 45.9 0.090 TL 10.00 PV Pipe: A 330.1 4.260 PL 27.00 PF 1.7 FOC 2.5 0.0 60.5 0.0 7.4 120 FTG ETG FE -11.5 A 29.0 0.0 47.2 0.0 0.025 TL 69.00 FV Pipe: B 330.1 4.260 FL 214.00 PF 6.4 A 29.0 0.0 47.2 0.0 7.4 120 FTG 3E PE 0.0 B 29.0 0.0 40.8 0.0 0.025 TL 253.00 PV Pipe: C 330.1 4.260 PL 180.00 PF 4.9 B 29.0 0.0 40.8 0.0 7.4 120 FTG E PE 0.0 C 29.0 0.0 36.0 0.0 0.025 TL 193.00 PV Pipe: D 330.1 4.260 FL 52.00 PF 1.6 C 29.0 0.0 36.0 0.0 7.4 120 FTG E FE 0.0 D 29.0 0.0 34.3 0.0 0.025 TL 65.00 PV Pipe: K 330.1 2.635 FL 26.00 PF 11.3 D 29.0 0.0 34.3 0.0 19.4 120 FTG T FE 0.0 E 29.0 0.0 23.0 0.0 0.262 TL 43.00 PV Pipe: F 330.1 2.635 FL 9.00 PF 6.8 E 29.0 0.0 23.0 0.0 19.4 120 FTG T FE 3.9 F 20.0 0.0 20.1 0.0 0.262 TL 26.00 PV Pipe: G 170.1 2.157 FL 10.00 PF 2.0 F 20.0 0.0 20.1 0.0 14.9 120 FTG ---- FE 4.3 G 10.0 0.0 22.4 0.0 0.204 TL 10.00 FV Pipe: Ri 71.7 1.682 FL 1.00 PF 1.5 F 20.0 0.0 20.1 0.0 10.3 120 FTG T PE 0.0 Ri 20.0 5.6 18.6 24.2 0.138 TL 11.00 FV Pipe: R2 47.5 1.682 FL 8.30 PF 0.5 Ri 20.0 5.6 18.6 24.2 6.9 120 FTG ---- FE 0.0 R2 20.0 5.6 18.1 23.8 0.065 TL 8.30 PV Pipe: R3 23.7 1.682 FL 8.30 PF 0.1 R2 20.0 5.6 18.1 23.8 3.4 120 FTG ---- PE 0.0 R3 20.0 5.6 17.9 23.7 0.018 TL 8.30 PV Pipe: R4 88.4 1.682 FL 7.50 PF 3.6 F 20.0 0.0 20.1 0.0 12.8 120 FTG T FE 0.0 R4 20.0 5.6 16.6 22.8 0.204 TL 17.50 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 DATE: 12/27/2021\MIKE HUANTE\NEWTON (THERMAL FISHER) \RACK SYSTEM PROOF.SDF JOB TITLE: 5803 NEWTON DR. (RACK STORAGE AREA PROOF 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: R5 65.6 1.682 PL 8.30 PF 1.0 R4 20.0 5.6 16.6 22.8 9.5 120 FTG ---- PE 0.0 R5 20.0 5.6 15.6 22.1 0.117 TL 8.30 PV Pipe: R6 43.5 1.682 PL 8.30 PF 0.5 R5 20.0 5.6 15.6 22.1 6.3 120 FTG ---- PE 0.0 R6 20.0 5.6 15.1 21.8 0.055 TL 8.30 PV Pipe: R7 21.7 1.682 PL 8.30 PF 0.1 R6 20.0 5.6 15.1 21.8 3.1 120 FTG ---- PE 0.0 R7 20.0 5.6 15.0 21.7 0.015 TL 8.30 PV Pipe: R8 74.5 1.682 PL 5.50 PF 2.3 G 10.0 0.0 22.4 0.0 10.8 120 FTG T PE 0.0 R8 10.0 5.6 20.1 25.1 0.149 TL 15.50 PV Pipe: R9 49.4 1.682 PL 8.30 PF 0.6 R8 10.0 5.6 20.1 25.1 7.1 120 FTG ---- PE 0.0 R9 10.0 5.6 19.5 24.8 0.070 TL 8.30 PV Pipe: RiO 24.6 1.682 PL 8.30 PF 0.2 R9 10.0 5.6 19.5 24.8 3.6 120 FTG ---- PE 0.0 RiO 10.0 5.6 19.4 24.6 0.019 TL 8.30 PV Pipe: Rll 95.6 1.682 PL 3.00 PF 3.1 G 10.0 0.0 22.4 0.0 13.8 120 FTG T PE 0.0 Rll 10.0 5.6 19.4 24.6 0.236 TL 13.00 PV Pipe: R12 70.9 1.682 PL 8.30 PF 1.1 Rll 10.0 5.6 19.4 24.6 10.2 120 FTG ---- PE 0.0 R12 10.0 5.6 18.2 23.9 0.136 TL 8.30 PV Pipe: R13 47.0 1.682 PL 8.30 PF 0.5 R12 10.0 5.6 18.2 23.9 6.8 120 FTG PE 0.0 R13 10.0 5.6 17.7 23.6 0.063 TL 8.30 PV Pipe: R14 23.5 1.682 PL 8.30 PF 0.1 R13 10.0 5.6 17.7 23.6 3.4 120 FTG ---- PE 0.0 R14 10.0 5.6 17.6 23.5 0.018 TL 8.30 PV NOTES (HASS) (1) Calculations were performed by the HASS 8.8 D computer program in accordance with NFPA13 (2016) under license no. 38011909 granted by HRS Systems, Inc. 208 Southside Square Petersburg, TN 37144 (931) 659-9760 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 13 DATE: 12/27/2021\MIKE HUANTE\NEWTON(THERMAL FISHER) \RACK SYSTEM PROOF.SDF JOB TITLE: 5803 NEWTON DR. (RACK STORAGE AREA PROOF CALC.) 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 0.196 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 19.4 ft/sec at pipe F. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. Available pressure at source node 1 under full flow conditions is 106.68 psi with a flow of 2225.43 gpm. PIPE FITTINGS TABLE HASS Pipe Table Name: standard.pip PAGE: B MATERIAL: THNWL HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngE11 ChkVlv BfyViv GatViv AlmChk DPViv NPTee -------------------------------------------------------- F45E11 1.682 5.00 10.00 3.00 11.00 8.00 1.00 12.00 12.00 10.00 2.50 2.157 6.00 12.00 3.00 14.00 8.00 1.00 12.00 12.00 12.00 3.00 2.635 8.00 17.00 6.00 19.00 10.00 1.00 14.00 14.00 17.00 4.00 4.260 13.00 26.00 8.00 29.00 16.00 3.00 26.00 26.00 26.00 6.50 6.357 18.00 38.00 11.00 40.00 13.00 4.00 35.00 35.00 38.00 9.00 PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N F Eli Tee LngEii ChkVlv BfyViv GatViv NPTee F45E11 8.390 31.00 59.00 22.00 76.00 20.00 7.00 59.00 15.50 140.0 C 112.0 G A U G 84.0 E P R 56.0 E S S U 28.0 R E 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 14 DATE: 12/27/2021\MIKE HUANTE\NEWTON(THERMAL FISHER) \RACK SYSTEM PROOF.SDF JOB TITLE: 5803 NEWTON DR. (RACK STORAGE AREA PROOF CALC.) WATER SUPPLY ANALYSIS Static: 116.00 psi Resid: 79.20 psi Flow: 4675.0 gpm LEGEND Available pressure 109.26 psi @ 1867.9 gpm I Required pressure 75.32 psi 8 1867.9 gpm Avail. OnSite Demand Press. 109.26 psi 8 1367.9 gpm a Req. OnSite Demand Press. 75.32 psi 8 1367.9 gpm Source Supply Curve System Demand Curve Available at Source p -14.7 I I I I I I I 10015002000 2500 3000 3500 4000 4500 5000 1 FLOW (GPM) Note: (1) Dashed Lines indicate extrapolated values from Test Results (2) On Site pressures are based on hose stream deduction at the source SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 15 ,,'DATE: 12/27/2021\MIKE HUANTE\NEWTON(THERMAL FISHER) \RACK SYSTEM PROOF.SDF JOB TITLE: 5803 NEWTON DR. (RACK STORAGE AREA PROOF CALC.) WATER SUPPLY CURVE 120+ *\ I \\ 110+ 0\ I \ \\ \\ 100+ \ \\ I \\ I \\ 90+ \ I \\ \\ \ P 80+ * <-79.2 psi 8 4675 gpm R I Flow Test Point E I X S I S 70+ U R I E I 60+ P S I I 50+ 40+ 30+ 20+ LEGEND I, I X = Required Water Supply I 75.32 psi @ 1867.9 gpm 10+ I 0 = Available Water Supply I 109.26 psi @ 1867.9 gpm 'V 0++-+---+----+-----+------+--------+--------+---------+-----------+ 16002400 3200 4000 4800 5600 6400 7200 8000 FLOW (GPM) KCJ Engineering Inc. 25431 Cabot, Suite 109 Client: JR Construction 44 Laguna Hills, Ca. 92653 Project: 5803 Newton Tel (949) 380-8186 Date: qr Fax (949) 5ö-14 sheet / of 121 (A & V7) r opoi -r 19 -q'57 JLL- /OLD/' 1og.7 C0,49 49a Gi4 c) g imz 7TIL/5S 76/7 CrO506- KCJ Engineering Inc. sheet / of 25431 Cabot, Suite 109 Client: JR Construction Laguna Hills, Ca. 92653 Project: 5803 Newton Tel (949) 380-8186 Date: t-ax (4) -104 Ft I€& (A / )0G PPO1CT' J-J"/5 1p tc CO/t7 Pci QY F1'S /P9f(r )4t\j JL- O/ rO37 ,,4 C,,'0 ::,- ~')') /' " (' c c I r im To1-7 HYCp TALJSS TW37 ciof/ Fig. 61T - Bar Joist Hanger Size Range - 3/8" thru 1/2' rod sizes Material - Carbon Steel Function - Designed to hook on top chord of metal bar joist. Hanger rod is threaded into product and secured with a wash- er and nut. Approvals - Underwriters' Laboratories Listed in the USA (UL) and Canada (cUL) for up to 4" pipe with 3/8" rod, up to 6" pipe with 1/2" rod. Finish - Plain Note - Available in Electro-Galvanized and HOG finish or Stainless Steel materials. Order By - Figure number, rod size, width and thickness of bar joist. Threaded hole will be center of that width. Dimensions Pipe Rod Max. Rec. Size Size Load Lbs. Upto4 3/8 300 C®US LISTED OFFICE/MANUFACTURING FACILITY.. 1375 SAMPSON AVE. • CORONA, CA 92879 • PH: 951.737.5599 • FAX: 951.737.0330 CUSTOMER SERVICE .800.786.5266 www.tolco.com Y 1E3 PULL MOOSM' 1UBE APPROVALS AND SPECIFICATIONS ASTMA135, Grade A ASTM A795, Type E, Grade A Pressure rated to 300 psi Underwriters Laboratories— United States of America Underwriters Laboratories—Canada EDDY FLOW SPRINKLER PIPE SUBMITTAL DATA SHEET FINISHES AND COATINGS Eddy Flow Sprinkler Pipe receives an 00 mill coating of water-based paint which has corrosion protection expected with a painted carbon steel product, i.e. it would be expected to resist corrosion for an extended and indefinite period in a clean and dry environment and, as environmental conditions deteriorate, the corrosion protection would also diminish. Factory Mutual • Eddy Flow Sprinkler Pipe (black) receives an ID mill coating of Eddy NFPA-13 Guard II MIC preventative coating. EG2 has been tested at NFPA-1 3R independent laboratories to resist bacterial growth and maintain NFPA-14 minimal bacterial count after multiple flushes (25) of the pipe. CIVIL DEFENSE APPROVAL— United Arab Emirates Made in the United States of America UL, ULC & FM listed for roll-groove, plain-end and welded joints for wet, dry, preaction and deluge sprinkler systems. LEED v4 Certified Eddy Flow Sprinkler Pipe when Hot Dip Galvanized by ASTM A123 and supplied by Bull Moose Tube is UL listed and FM approved. PRODUCT IDENTIFICATION Every length of Bull Moose fire sprinkler pipe features large, easy-to- read, continuous stenciling, clearly identifying the manufacturer, type of pipe, size, and length. 0.0. (In) ID. (In) Empty Weight (lb/ft) 1.660 1.900 2.315 2.875 3.500 4.500 1.530 1.728 2.203 2.105 3.334 4.310 1.222 1.844 2.330 2.809 3.361 4.968 Water Filled Welght(Ib/ft) 2.019 2.860 3.982 5.299 1.144 11.290 C.RJL* 1.98 3.44 2.78 1.66 1.00 1.00 Pieces per Lift 61 61 37 30 19 19 *calculated using Standard UL ERR formula, UL Fire Protection Directory, category VIZY (~D C (& <.~~> SUBMITTAL INFORMATION Project [ Contractor[ Engineer L Specification Reference Date L j System Type Locations Comments Eddy Flow - Black () Eddy Flow - Hot Dip Galvanized US80032!4467 I I1BOOT882i666