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HomeMy WebLinkAbout1808 ASTON AVE; ; AS010027; Permit8/10/22, 1 :30 PM Job Address: Permit Type: Parcel No: Lot#: Reference No.: PC#: Project Title: Applicant: Fees($) 949 AS010027 Permit Data City of Carlsbad Sprinkler Permit Permit No: AS010027 1808 ASTON AV Status: ISSUED SPRINK Applied 1/25/2001 2121200700 Approved: 3/30/2001 0 Issued: 3/30/2001 Inspector: ASTON VIEWS PLAZA - Owner: ASTON VIEWS L L C 4370 LA JOLLA VILLAGE DR #655 SAN DIEGO CA - Add'I Fees ($) Total($) Balance($) 0 949 0 1 /1 a jJ m.,f},u I)_ rto o 3; is vrrr ···-vu ~t!f5DI oaJ-7 ~---CARLSBAD FIRE PROTECTION SERVICES Permit -Submittal Form A. Check or fill in pertinent information for type of permit you are submitting. AS -Automatic Sprinklers ~ Commercial ___ ~---Residential ____ _ Number of Heads per System: System #_L Heads.22._;;;;_ System #__ Heads System# ___ Heads __ --System # Heads __ System # __ Heads __ System # Heads __ Underground included for approval Underground included for reference only ____ _ Total Fees FA -Fire Alarm 10 devices or less Over 10 devices ___ # of devices ___ _ FS -Fixed Systems (Circle One) Hood & Duct, Halon, Special Chemical Agent, Standpipe, Spray Booth, or Appliance. Total Fees __ _ There may bee an additional fee of $50.00 per ½ hour for Failed Inspections. B. Address of job site iJ/1!!;::A sTQN ,{IJEAIUF Suite# ____ _ Building Permit# _C_B_-"-(J ...::;_t _7-LJ_:,__tf_5_ C. Contractor Information Address 2-Z. Z.C E V / ~ City,State,Zip-rl/LJAl--lc/A / CrJ L 7Z-BCJ0 s/ 3s-0~ KindofLicenseandnumberC/6-C3<J-: Phone ?/£ S3S-:--_J 7G/ Certificate of Insurance on file with Fire Dept.? r N Business License on filr with City? ~ N Signature~ c~ Date 6/-/9~zoo/ Carlsbad Fire Department A Sci(:l:,2-t-003345 1635 Faraday Ave. Carlsbad, CA 92008 y (760) 602-4660 Plan Review Requirements Category: f 'l[ COR ·. Fire Prevention Auto. Sprinkle ~bH Reviewed by: Date of Report: 03/28/2001 ------------ Name: Lindley Fire Prot. Address: 2220 E. Via Burton City, State: Anaheim CA 92806 Plan Checker: Job #: 003345 ------- Job Name: Aston Views Plaza Bldg #: CB003345 ------------------ Job Address: 1808 Aston Avenue Ste. or Bldg. No. ~ Approved D Approved Subject to D Incomplete Review FD Job# The item you have submitted for review has been approved. The approval is based on plans, information and / or specifications provided in your submittal; therefore any changes to these items after this date, including field modifications, must be reviewed by this office to insure continued conformance with applicable codes and standards. Please review carefully all comments attached as failure to comply with instructions in this report can result in suspension of permit to construct or install improvements. The item you have submitted for review has been approved subject to the attached conditions. The approval is based on plans, information and/or specifications provided in your submittal. Please review carefully all comments attached, as failure to comply with instructions in this report can result in suspension of permit to construct or install improvements. Please resubmit to this office the necessary plans and/ or specifications required to indicate compliance with applicable codes and standards. The item you have submitted for review is incomplete. At this time, this office cannot adequately conduct a review to determine compliance with the applicable codes and I or standards. Please review carefully all comments attached. Please resubmit the necessary plans and / or specifications to this office for review and approval. 1st 003345 2nd FD File# 3rd Other Agency ID LINDLEY FIRE PROTECTION CO. 2220 E. VIA BURTON ANAHEIM,CA 714-535-5761 HYDRAULIC CALCULATIONS FOR ASTON VIEWS PLAZA CARLSBAD, CALIFORNIA FIRST FLOOR DATE: 1-17-01 -DESIGN DATA- SYSTEM DENSITY: AREA OF APPLICATION: COVERAGE PER SPRINKLER: NUMBER OF SPRINKLERS CALCULATED: TOTAL SPRINKLER WATER FLOW REQUIRED: TOTAL WATER REQUIRED (INCLUDING HOSE) FLOW AND PRESSURE & BASE OF RISER: SPRINKLER ORIFICE SIZE: CONTRACTOR CERTIFICATION NUMBER: .15 GPM/SQ. FT. 2000 SQ. FT. 130 SQ. FT. 16 358.4 GPM 608.4 GPM 358.4 GPM@ 92.5 PSI ½" C16/C34 NO. 713562 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 Date: 01/17/2001 ASTONFF.SDF JOB TITLE: ASTON VIEWS FIRST FLOOR .15 FOR 2000 WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) U4 103.5 94.5 1683.0 102.1 608.4 96.3 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 608.4 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 150.0 GPM OTHER HOSE STREAM ALLOWANCES 100.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 358.4 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) Hl 12.4 K= 5.60 12.1 19.5 H2 12.4 K= 5.60 12.4 19.7 H3 12.4 K= 5.60 13.4 20.5 H4 12.4 K= 5.60 15.6 22.1 HS 12.4 K= 5.60 18.4 24.0 H6 12.4 K= 5.60 12.5 19.8 H7 12.4 K= 5.60 12.8 20.0 H8 12.4 K= 5.60 13.8 20.8 H9 12.4 K= 5.60 16.1 22.5 Hl0 12.4 K= 5.60 18.9 24.4 Hll 12.4 K= 5.60 13.9 20.9 H12 12.4 K= 5.60 14.2 21.1 H13 12.4 K= 5.60 15.4 21. 9 H14 12.4 K= 5.60 17.8 23.6 H15 12.4 K= 5.60 21. 0 25.7 H16 12.4 K= 5.60 32.4 31. 9 H17 29.0 ----51. 6 --- H18 29.0 ----51.6 --- H19 29.0 ----51. 6 --- H20 29.0 ----51. 6 --- H21 29.0 ----51. 6 --- H22 29.0 ----51.6 --- H23 29.0 ----51. 6 --- H24 29.0 ----51. 6 --- H25 29.0 ----51.6 --- H26 29.0 ----51. 6 --- H27 29.0 51. 6 --- H28 29.0 ----51. 6 --- H29 29.0 ----51.6 --- H30 29.0 ----51. 6 --- H31 29.0 ----51.6 --- H32 29.0 ----51. 6 --- 1 12.4 19.0 --- 2 10.9 25.0 --- SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 Date: 01/17/2001 ASTONFF.SDF JOB TITLE: ASTON VIEWS FIRST FLOOR .15 FOR 2000 NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 3 12.4 ----19.6 --- 4 10.9 25.7 --- 5 12 .4 ----21. 8 --- 6 10.9 ----28.4 --- 7 12.4 33.0 --- 8 10.9 34.2 --- 9 10.9 ----53.5 --- 10 10.9 56.0 --- 11 10.9 61.1 --- 12 10.9 67.2 --- 13 10.9 73.6 --- 13A 10.9 69.6 --- 14 10.9 ----81.1 --- 15 10.9 ----81.1 --- 15A 10.9 ----85.3 --- 16 10.9 87.5 --- 17 29.0 51. 6 --- 18 27.5 52.2 --- 19 29.0 51. 6 --- 20 27.5 ----52.2 --- 21 29.0 ----51.6 --- 22 27.5 52.2 --- 23 29.0 ----51. 6 --- 24 27.5 ----52.2 --- 25 27.5 ----52.2 --- 26 27.5 49.8 27 27.5 ----58.0 --- 28 27.5 ----62.3 --- 29 27.5 65.9 --- 29A 27.5 ----63.7 --- 30 27.5 71.2 --- 31 27.5 71. 7 --- 32 27.5 75.5 --- 33 10.9 83.7 --- 34 10.9 ----85.3 --- U4 0.0 SOURCE 96.3 458.4 BOR 0.0 HOSE STREAM 92.5 100.0 UI 0.0 ----92.6 --- U2 0.0 ----92.7 --- U3 0.0 ----96.2 --- SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 Date: 01/17/2001 ASTONFF.SDF JOB TITLE: ASTON VIEWS FIRST FLOOR .15 FOR 2000 PIPE DATA PIPE TAG Q{GPM) DIA ( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) F.L./FT (PSI) Pipe: 1 -19.5 1.508 PL 13.00 PF 0.3 Hl 12 .4 5.6 12.1 19.5 3.5 120 FTG PE 0.0 H2 12.4 5.6 12.4 19.7 0.021 TL 13.00 PV 0.1 Pipe: 2 -39.2 1. 508 PL 13.00 PF 1.0 H2 12.4 5.6 12.4 19.7 7.0 120 FTG PE 0.0 H3 12.4 5.6 13.4 20.5 0.077 TL 13.00 PV 0.3 Pipe: 3 -59.7 1.508 PL 13.00 PF 2.2 H3 12.4 5.6 13.4 20.5 10.7 120 FTG PE 0.0 H4 12.4 5.6 15.6 22.1 0.168 TL 13.00 PV 0.8 Pipe: 4 -81. 8 1. 508 PL 1.50 PF 3.5 H4 12.4 5.6 15.6 22.1 14.7 120 FTG T PE 0.0 1 12.4 0.0 19.0 0.0 0.301 TL 11.50 PV 1.5 Pipe: 5 24.0 1.508 PL 11.50 PF 0.7 1 12.4 0.0 19.0 0.0 4.3 120 FTG T PE 0.0 HS 12.4 5.6 18.4 24.0 0.031 TL 21.50 PV 0.1 Pipe: 6 -105.8 1.508 PL 0.83 PF 5.2 1 12.4 0.0 19.0 0.0 19.0 120 FTG T PE 0.7 2 10.9 0.0 25.0 0.0 0.485 TL 10.83 PV 2.4 Pipe: 7 -19.8 1.508 PL 13.00 PF 0.3 H6 12.4 5.6 12.5 19.8 3.6 120 FTG PE 0.0 H7 12.4 5.6 12.8 20.0 0.022 TL 13.00 PV 0.1 Pipe: 8 -39.8 1.508 PL 13.00 PF 1.0 H7 12.4 5.6 12.8 20.0 7.2 120 FTG PE 0.0 HS 12.4 5.6 13.8 20.8 0.079 TL 13.00 PV 0.3 Pipe: 9 -60.7 1. 508 PL 13.00 PF 2.2 HS 12.4 5.6 13.8 20.8 10.9 120 FTG PE 0.0 H9 12.4 5.6 16.1 22.5 0.173 TL 13.00 PV 0.8 Pipe: 10 -83.1 1.508 PL 1.50 PF 3.6 H9 12.4 5.6 16.1 22.5 14.9 120 FTG T PE 0.0 3 12.4 0.0 19.6 0.0 0.310 TL 11.50 PV 1.5 Pipe: 11 24.4 1.508 PL 11.50 PF 0.7 3 12.4 0.0 19.6 0.0 4.4 120 FTG T PE 0.0 Hl0 12.4 5.6 18.9 24.4 0.032 TL 21.50 PV 0.1 Pipe: 12 -107.5 1.508 PL 0.83 PF 5.4 3 12.4 0 .0 19.6 0.0 19.3 120 FTG T PE 0.7 4 10.9 0.0 25.7 0.0 0.499 TL 10.83 PV 2.5 Pipe: 13 -20.9 1. 508 PL 13.00 PF 0.3 Hll 12.4 5.6 13.9 20.9 3.8 120 FTG PE 0.0 H12 12.4 5.6 14.2 21.1 0.024 TL 13.00 PV 0.1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 Date: 01/17/2001 ASTONFF.SDF JOB TITLE: ASTON VIEWS FIRST FLOOR .15 FOR 2000 PIPE DATA (cont.) PIPE TAG Q(GPM) DIA ( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW (C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) F.L./FT (PSI) Pipe: 14 -42.0 1. 508 PL 13.00 PF 1.1 H12 12.4 5.6 14.2 21.1 7.5 120 FTG PE 0.0 H13 12.4 5.6 15.4 21. 9 0.088 TL 13.00 PV 0.4 Pipe: 15 -63.9 1.508 PL 13.00 PF 2.5 H13 12.4 5.6 15.4 21. 9 11.5 120 FTG PE 0.0 H14 12.4 5.6 17.8 23.6 0.191 TL 13.00 PV 0.9 Pipe: 16 -87.6 1. 508 PL 1.50 PF 3.9 H14 12.4 5.6 17.8 23.6 15.7 120 FTG T PE 0.0 5 12.4 0.0 21. 8 0.0 0.341 TL 11.50 PV 1. 7 Pipe: 17 25.7 1.508 PL 11.50 PF 0.8 5 12.4 0.0 21.8 0.0 4.6 120 FTG T PE 0.0 H15 12.4 5.6 21. 0 25.7 0.035 TL 21.50 PV 0.1 Pipe: 18 -113.3 1. 508 PL 0.83 PF 5.9 5 12.4 0 .. 0 21. 8 0.0 20.3 120 FTG T PE · 0.7 6 10.9 0.0 28.4 0.0 0.549 TL 10.83 PV 2.8 Pipe: 19 -31.9 1.508 PL 1.50 PF 0.6 H16 12.4 5.6 32.4 31. 9 5.7 120 FTG T PE 0.0 7 12.4 0.0 33.0 0.0 0.053 TL 11.50 PV 0.2 Pipe: 20 -31.9 1. 508 'PL 0.83 PF 0.6 7 12.4 0.0 33.0 0.0 5.7 120 FTG T PE 0.7 8 10.9 0.0 34.2 0.0 0.053 TL 10.83 PV 0.2 Pipe: 21 -105.8 2.223 PL 10.00 PF 0.7 2 10.9 0.0 25.0 0.0 8.7 120 FTG PE 0.0 4 10.9 0.0 25.7 0.0 0.073 TL 10.00 PV 0.5 Pipe: 22 -213.3 2.223 PL 10.00 PF 2.7 4 10.9 0.0 25.7 0.0 17.6 120 FTG PE 0.0 6 10.9 0.0 28.4 0.0 0.268 TL 10.00 PV 2.1 Pipe: 23 -326.6 2.223 PL 10.00 PF 5.9 6 10.9 0.0 28.4 0.0 27.0 120 FTG PE 0.0 8 10.9 0.0 34.2 0.0 0.589 TL 10.00 PV 4.9 Pipe: 24 -358.5 2.223 PL 13.58 PF 19.3 8 10.9 0.0 34.2 0.0 29.6 120 FTG T PE 0.0 9 10.9 0.0 53.5 0.0 0.699 TL 27.58 PV 5.9 Pipe: 25 -163.1 2.723 PL 15.29 PF 2.4 9 10.9 0.0 53.5 0.0 9.0 120 FTG TL PE 0.0 10 10.9 0.0 56.0 0.0 0.061 TL 40.29 PV 0.5 Pipe: 26 -195.3 2.723 PL 89.67 PF 7.6 9 10.9 0.0 53.5 0.0 10.8 120 FTG PE 0 .0 11 10.9 0.0 61.1 0.0 0.085 TL 89.67 PV 0.8 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page S Date: 01/17/2001 ASTONFF.SDF JOB TITLE: ASTON VIEWS FIRST FLOOR .15 FOR 2000 PIPE DATA (cont.) PIPE TAG Q(GPM) DIA ( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) F.L./FT (PSI) Pipe: 27 -195.3 2.723 PL 72.00 PF 6.1 11 10.9 0.0 61.1 0.0 10.8 120 FTG PE 0.0 12 10.9 0.0 67.2 0.0 0.085 TL 72.00 PV 0.8 Pipe: 28 -195.3 2.723 PL 25.67 PF 2.4 12 10.9 0.0 67.2 0.0 10.8 120 FTG F PE 0.0 13A 10.9 0.0 69.6 0.0 0.085 TL 28.67 PV 0.8 Pipe: 28A -195.3 2 .. 723 PL 43.12 PF 3.9 13A 10.9 0.0 69.6 0.0 10.8 120 FTG F PE 0.0 13 10.9 0.0 73.6 0.0 0.085 TL 46.12 PV 0.8 Pipe: 29 -195.3 2.723 PL 88.50 PF 7.5 13 10.9 0.0 73.6 0.0 10.8 120 FTG PE 0.0 14 10.9 0.0 81.1 0.0 0.085 TL 88.50 PV 0.8 Pipe: 30 -195.3 2.723 PL 1.00 PF 0.1 14 10.9 0.0 81.1 0.0 10.8 120 FTG PE 0.0 15 10.9 0.0 81.1 0.0 0.085 TL 1.00 PV 0.8 Pipe: 31 -195.3 2.723 PL 43.17 PF 4.2 15 10.9 0.0 81.1 0.0 10.8 120 FTG L PE 0.0 15A 10.9 0.0 85.3 0.0 0.085 TL 49.17 PV 0.8 Pipe: 31A -195.3 4.328 PL 5.17 PF 0.0 15A 10.9 0.0 85.3 0.0 4.3 120 FTG PE 0.0 34 10.9 0.0 85.3 0.0 0.009 TL 5.17 PV 0.1 Pipe: 32 -358.5 4.328 PL 62.17 PF 2.1 34 10.9 0.0 85.3 0.0 7.8 120 FTG 2L PE 0.0 16 10.9 0.0 87.5 0.0 0.027 TL 78.17 PV 0.4 Pipe: 33 -358.5 4.328 PL 10.88 PF 0.3 16 10.9 0.0 87.5 0.0 7.8 120 FTG PE 4.7 BOR 0.0 H.S. 92.5 100.0 0.027 TL 10.88 PV 0.4 Pipe: 34 0.0 1.508 PL 13.00 PF 0.0 H17 29.0 0.0 51.6 0.0 0.0 120 FTG PE 0.0 H18 29.0 0.0 51. 6 0.0 0.000 TL 13.00 PV 0.0 Pipe: 35 0.0 1.508 PL 13.00 PF 0.0 H18 29.0 0.0 51. 6 0.0 0.0 120 FTG PE 0.0 H19 29.0 0.0 51. 6 0.0 0.000 TL 13.00 PV 0.0 Pipe: 36 0.0 1.508 PL 13.00 PF 0.0 H19 29.0 0.0 51. 6 0.0 0.0 120 FTG PE 0.0 H20 29.0 0.0 51.6 0.0 0.000 TL 13.00 PV 0.0 Pipe: 37 0.0 1.508 PL 1. 50 PF 0.0 H20 29.0 0.0 51. 6 0.0 0.0 120 FTG T PE 0.0 17 29.0 0.0 51. 6 0.0 0.000 TL 11. 50 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 Date: 01/17/2001 ASTONFF.SDF JOB TITLE: ASTON VIEWS FIRST FLOOR .15 FOR 2000 PIPE DATA (cont.) PIPE TAG Q(GPM) DIA ( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) F.L./FT (PSI) Pipe: 38 0.0 1. 508 PL 9.50 PF 0.0 17 29.0 0.0 51. 6 0.0 0.0 120 FTG T PE 0.0 H21 29.0 0.0 51.6 0.0 0.000 TL 19.50 PV 0.0 Pipe: 39 0.0 1.508 PL 0.83 PF 0.0 17 29.0 0.0 51.6 0.0 0.0 120 FTG T PE 0.6 18 27.5 0.0 52.2 0.0 0.000 TL 10.83 PV 0.0 Pipe: 40 0.0 1.508 PL 13.00 PF 0.0 H22 29.0 0.0 51.6 0.0 0.0 120 FTG PE 0.0 H23 29.0 0.0 51. 6 0.0 0.000 TL 13.00 PV 0.0 Pipe: 41 0.0 1.508 PL 13.00 PF 0.0 H23 29.0 0.0 51.6 0.0 0.0 120 FTG PE 0.0 H24 29.0 0.0 51.6 0.0 0.000 TL 13.00 PV 0.0 Pipe: 42 0.0 1.508 PL 13.00 PF 0.0 H24 29.0 0.0 51.6 0.0 0.0 120 FTG PE 0.0 H25 29.0 0.0 51.6 0.0 0.000 TL 13.00 PV 0.0 Pipe: 43 0.0 1.508 PL 1.50 PF 0.0 H25 29.0 0.0 51.6 0.0 0.0 120 FTG T PE 0.0 19 29.0 0.0 51.6 0.0 0.000 TL 11.50 PV 0.0 Pipe: 44 0.0 1. 508 PL 9.50 PF 0.0 19 29.0 0.0 51. 6 0.0 0.0 120 FTG T PE 0.0 H26 29.0 0.0 51.6 0.0 0.000 TL 19.50 PV 0.0 Pipe: 45 0.0 1.508 PL 0.83 PF 0.0 19 29.0 0.0 51.6 0.0 0.0 120 FTG T PE 0.6 20 27.5 0.0 52.2 0.0 0.000 TL 10.83 PV 0.0 Pipe: 46 0.0 1.508 PL 13.00 PF 0.0 H27 29.0 0.0 51.6 0.0 0.0 120 FTG PE! 0.0 H28 29.0 0.0 51.6 0.0 0.000 TL 13.00 PV 0.0 Pipe: 47 0.0 1.508 PL 13.00 PF 0.0 H28 29.0 0.0 51.6 0.0 0.0 120 FTG PE 0.0 H29 29.0 0.0 51.6 0.0 0.000 TL 13.00 PV 0.0 Pipe: 48 0.0 1.508 PL 13.00 PF 0.0 H29 29.0 0.0 51. 6 0.0 0.0 120 FTG PE 0.0 H30 29.0 0.0 51. 6 0.0 0.000 TL 13.00 PV 0.0 Pipe: 49 0.0 1.508 PL 1.50 PF 0.0 H30 29.0 0.0 51.6 0.0 0.0 120 FTG T PE 0.0 21 29.0 0.0 51. 6 0.0 0.000 TL 11. 50 PV 0.0 Pipe: 50 0.0 1. 508 PL 9.50 PF 0.0 21 29.0 0.0 51. 6 0.0 0.0 120 FTG T PE 0.0 H31 29.0 0.0 51. 6 0.0 0.000 TL 19.50 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 Date: 01/17/2001 ASTONFF.SDF JOB TITLE: ASTON VIEWS FIRST FLOOR .15 FOR 2000 PIPE DATA (cont.) PIPE TAG Q(GPM) DIA ( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW (C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) F.L./FT (PSI) Pipe: 51 0.0 1. 508 PL 0.83 PF 0.0 21 29.0 0.0 51. 6 0.0 0.0 120 FTG T PE 0.6 22 27.5 0.0 52.2 0.0 0.000 TL 10.83 PV 0.0 Pipe: 52 0.0 1.508 PL 1.50 PF 0.0 H32 29.0 0.0 51. 6 0.0 0.0 120 FTG T PE 0.0 23 29.0 0.0 Sl.6 0.0 0.000 TL 11.50 PV 0.0 Pipe: 53 0.0 1. 508 PL 0.83 PF 0.0 23 29.0 0.0 51. 6 0.0 0.0 120 FTG T PE 0.6 24 27.5 0.0 52.2 0.0 0.000 TL 10.83 PV 0.0 Pipe: 54 0.0 2.223 PL 10.00 PF 0.0 18 27.5 0.0 52.2 0.0 0.0 120 FTG PE 0.0 20 27.5 0.0 52.2 0.0 0.000 TL 10.00 PV 0.0 Pipe: 55 0.0 2.223 PL 10.00 PF 0.0 20 27.5 0.0 52.2 0.0 0.0 120 FTG PE 0.0 22 27.5 0.0 52.2 0.0 0.000 TL 10.00 PV 0.0 Pipe: 56 0.0 2.223 PL 10.00 PF 0.0 22 27.5 0.0 52.2 0.0 0.0 120 FTG PE 0.0 24 27.5 0.0 52.2 0.0 0.000 TL 10.00 PV 0.0 Pipe: 57 0.0 2.723 PL 13.58 PF 0.0 24 27.5 0.0 52.2 0.0 0.0 120 FTG T PE 0.0 25 27.5 0.0 52.2 0.0 0.000 TL 32.58 PV 0.0 Pipe: 58 163.1 2.723 PL 15.29 PF 2.4 25 27.5 0.0 52.2 0.0 9.0 120 FTG TL PE 0.0 26 27.5 0.0 49.8 0.0 0.061 TL 40.29 PV 0.5 Pipe: 59 163.1 2.723 PL 16.62 PF 1. 0 26 27.5 0.0 49.8 0.0 9.0 120 FTG PE 7.2 10 10.9 0.0 56.0 0.0 0.061 TL 16.62 PV 0.5 Pipe: 60 -163.1 2.723 PL 95.67 PF 5.8 25 27.5 0.0 52.2 0.0 9.0 120 FTG PE 0.0 27 27.5 0.0 58.0 0.0 0.061 TL 95.67 PV 0.5 Pipe: 61 -163.1 2.723 PL 70.42 PF 4.3 27 27.5 0.0 58.0 0.0 9.0 120 FTG PE 0.0 28 27.5 0.0 62.3 0.0 0.061 TL 70.42 PV 0.5 Pipe: 62 -163.1 2.723 PL 20.50 PF 1.4 28 27.5 0.0 62.3 0.0 9.0 120 FTG F PE 0.0 29A 27.5 0.0 63.7 0.0 0.061 TL 23.50 PV 0.5 Pipe: 62A -163.1 2.723 PL 33.33 PF 2.2 29A 27.5 0.0 63.7 0.0 9.0 120 FTG F PE 0.0 29 27.5 0.0 65.9 0.0 0.061 TL 36.33 PV 0.5 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Date: 01/17/2001 Page 8 ASTONFF.SDF JOB TITLE: ASTON VIEWS FIRST FLOOR .15 FOR 2000 PIPE DATA (cont.) PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. NODES ( FT) (K) PT DISC. VEL(FPS) HW(C) (FT) (PSI) (GPM) F.L./FT SUM. (PSI) 29 30 30 31 31 32 32 33 33 34 Pipe: 63 27.5 27.5 Pipe: 64 27.5 27.5 Pipe: 65 27.5 27.5 Pipe: 66 27.5 10.9 Pipe: 67 10.9 10.9 Pipe: 68 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 BOR 0.0 H.S. UI 0.0 0.0 UI U2 U3 U2 U3 U4 Pipe: 69 0.0 0.0 Pipe: 70 0.0 0.0 Pipe: 71 0.0 0.0 NOTES: 0.0 0.0 0.0 0.0 0.0 SRCE 65.9 71.2 71.2 71. 7 71.7 75.5 75.5 83.7 83.7 85.3 -163.1 0.0 9.0 0.0 -163.1 0.0 9.0 0.0 -163.1 0.0 9.0 0.0 -163.1 0.0 9.0 0.0 -163.1 0.0 9.0 0.0 -458.5 92.5 100.0 2.7 92.6 0.0 92.6 92.7 -458.5 0.0 2.9 0.0 2.723 PL 120 FTG 0.061 TL 2.723 PL 120 FTG 0.061 TL 2.723 PL 120 FTG 0.061 TL 2.723 PL 120 FTG 0.061 TL 2.723 PL 120 FTG 0.061 TL 87.29 87.29 7.00 7.00 51. 00 2L 63.00 16.62 16.62 ·2.33 TL 27.33 PF PE PV PF PE PV PF PE PV PF PE PV PF PE PV 8.390 PL 11.00 PF 140 FTG 2L PE 0.001 TL · 55.00 PV 8.044 PL 150 FTG 0.001 TL 25.00 TL 73.00 PF PE PV FIXED PRESSURE LOSS DEVICE 96.2 92.7 96.2 96.3 0.0 3.5 psi, 458.5 gpm 0.0 -458.4 0.0 2.9 (N/A) 8.044 PL 150 FTG 0.001 TL 22.00 T2LG 87.00 PF PE PV 5.3 0.0 0.5 0.4 0.0 0.5 3.8 0.0 0.5 1.0 7.2 0.5 1. 7 0.0 0.5 0.1 0.0 0.0 0.1 0.0 0.1 0.1 0.0 0.1 (1) Calculations were performed by the HASS 6.5.0 computer program under license no. 38010408 granted by HRS Systems, Inc. 4792 Lavista Road Tucker, GA 30084 (2) The system has been balanced to provide an average imbalance at each node of 0.001 gpm and a maximum imbalance at any node of 0.109 gpm. (3) Velocity pressures are printed for information only, and are not used in balancing the system. Maximum water velocity is 29.6 ft/sec at pipe 24. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Date: 01/17/2001 JOB TITLE: ASTON VIEWS FIRST FLOOR .15 FOR 2000 (4) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet ( in) E T L C B G Ell Tee LngEll ChkVlv BfyVlv GatVlv 8.390 31. 00 60.00 22.00 78.00 21. 00 7.00 PAGE: E MATERIAL: PVC150 HWC: 150 Diameter Equivalent Fitting Lengths in Feet ( in) E T L C B G Ell Tee LngEll ChkVlv BfyVlv GatVlv 8.044 26.00 35.00 13.00 45.00 17.00 4.00 PAGE: J MATERIAL: FIRELINE HWC: 120 Diameter Equivalent Fitting Lengths in Feet ( in) E T L C B G Page 9 ASTONFF.SDF N NPTee 60.00 N F NPTee 45 35.00 9.00 A D Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPVlv N F NPTee 5 1.508 5.00 10.00 3.00 12.00 12.00 2.00 20.00 17.00 7.00 1.00 2.223 7.00 14.00 4.00 15.00 10.00 1.00 17.00 14.00 12.00 2.00 2.723 10.00 19.00 6.00 22.00 16.00 2.00 22.00 16.00 17.00 3.00 4.328 14.00 28.00 8.00 31. 00 22.00 4.00 35.00 14.00 26.00 4.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Date: 01/17/2001 JOB TITLE: ASTON VIEWS FIRST FLOOR .15 FOR 2000 WATER SUPPLY CURVE p R E s s u R E ( p s I ) 108+ I *\\\\\\\\\\\ I o \\\\\\\\\\\\ 99+ \\\\\\\\\\\\ 90+ 81+ 72+ 63+ 54+ 45+ 36+ 27+ 18+ 9+ X \\\\\\\\\\\ 94.5 psi@ 1683 gpm-> * Flow Test Point LEGEND X = Required Water Supply 96.29 psi@ 608.4 gpm 0 = Available Water Supply 102.13 psi@ 608.4 gpm " " Page 10 ASTONFF.SDF 0++-+---+----+-----+------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) LINDLEY FIRE PROTECTION CO. 2220 E. VIA BURTON ANAHEIM,CA 714-535-5761 HYDRAULIC CALCULATIONS FOR ASTON VIEWS PLAZA CARLSBAD, CALIFORNIA SECOND FLOOR DATE: 1-17-01 -DESIGN DATA- SYSTEM DENSITY: AREA OF APPLICATION: COVERAGE PER SPRINKLER: NUMBER OF SPRINKLERS CALCULATED: TOTAL SPRINKLER WATERFLOWREQU1RED: TOTAL WATER REQU1RED (INCLUDING HOSE) FLOW AND PRESSURE & BASE OF RISER: SPRINKLER ORIFICE SIZE: CONTRACTOR CERTIFICATION NUMBER: .15 GPM/SQ. FT. 2000 SQ. FT. 130 SQ. FT. 15 358.6 GPM 608.6 GPM 358.6 GPM@ 89.5 PSI ½" C16/C34 NO. 713562 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 Date: 01/17/2001 ASTONSF.SDF JOB TITLE: ASTON VIEWS SECOND FLOOR .15 FOR 2000 WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) U4 103.5 94.5 1683.0 102.1 608.6 93.3 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 608.6 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 150.0 GPM OTHER HOSE STREAM ALLOWANCES 100.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 358.6 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) Hl 12.4 ----56.0 --- H2 12.4 ----56.0 --- H3 12.4 56.0 --- H4 12.4 56.0 --- HS 12.4 ----56.0 --- H6 12.4 ----56.0 --- H7 12.4 56.0 --- H8 12.4 ----56.0 --- H9 12.4 ----56.0 --- Hl0 12.4 ----56.0 --- Hll 12.4 56.0 --- H12 12.4 56.0 --- H13 12.4 ----56.0 --- H14 12.4 ----56.0 --- H15 12.4 ----56.0 --- H16 12.4 ----56.0 --- H17 29.0 K= 5.60 12.1 19.5 H18 29.0 K= 5.60 12.4 19.7 H19 29.0 K= 5.60 13.4 20.5 H20 29.0 K= 5.60 15.6 22.1 H21 29.0 K= 5.60 18.4 24.0 H22 29.0 K= 5.60 12.5 19.8 H23 29.0 K= 5.60 12.8 20.0 H24 29.0 K= 5.60 13.8 20.8 H25 29.0 K= 5.60 16.1 22.4 H26 29.0 K= 5.60 19.0 24.4 H27 29.0 K= 5.60 13.9 20.9 H28 29.0 K= 5.60 14.2 21.1 H29 29.0 K= 5.60 15 .4 21. 9 H30 29.0 K= 5.60 17.8 23.6 H31 29.0 K= 5.60 21.1 25.7 H32 29.0 K= 5.60 32.4 31. 9 1 12.4 56.0 --- 2 10.9 ----56.6 --- SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 Date: 01/17/2001 ASTONSF.SDF JOB TITLE: ASTON VIEWS SECOND FLOOR .15 FOR 2000 NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 3 12.4 56.0 --- 4 10.9 ----56.6 --- 5 12.4 56.0 --- 6 10.9 56.6 --- 7 12.4 56.0 --- 8 10.9 56.6 --- 9 10.9 56.6 --- 10 10.9 53.9 --- 11 10.9 62.8 --- 12 10.9 ----67.7 --- 13 10.9 72.8 --- 13A 10.9 ----69.7 --- 14 10.9 ----78.9 --- 15 10.9 ----79.0 --- 15A 10.9 ----82.4 --- 16 10.9 84.5 --- 17 29.0 ----19.1 --- 18 27.5 ----25.0 --- 19 29.0 ----19.6 --- 20 27.5 25.7 --- 21 29.0 21. 8 --- 22 27.5 28.4 --- 23 29.0 ----33.0 --- 24 27.5 34.3 --- 25 27.5 42.7 --- 26 27.5 45.5 --- 27 27.5 ----50.0 --- 28 27.5 ----55.4 --- 29 27.5 59.9 --- 29A 27.5 ----57.1 --- 30 27.5 66.5 --- 31 27.5 67.1 --- 32 27.5 71.9 --- 33 10.9 ----80.3 --- 34 10.9 82.4 --- U4 0.0 SOURCE 93.3 458.6 BOR 0.0 HOSE STREAM 89.5 100.0 UI 0.0 89.6 --- U2 0.0 ----89.7 --- U3 0.0 ----93.2 --- SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 Date: 01/17/2001 ASTONSF.SDF JOB TITLE: ASTON VIEWS SECOND FLOOR .15 FOR 2000 PIPE DATA PIPE TAG Q(GPM) DIA ( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) F.L./FT (PSI) Pipe: 1 0.0 1. 508 PL 13.00 PF 0.0 Hl 12.4 0.0 56.0 0.0 0.0 120 FTG PE 0.0 H2 12.4 0.0 56.0 0.0 0.000 TL 13.00 PV 0.0 Pipe: 2 0.0 1. 508 PL 13.00 PF 0.0 H2 12.4 0.0 56.0 0.0 0.0 120 FTG PE 0.0 H3 12.4 0.0 56.0 0.0 0.000 TL 13.00 PV 0.0 Pipe: 3 0.0 1. 508 PL 13.00 PF 0.0 H3 12.4 0.0 56.0 0.0 0.0 120 FTG PE 0.0 H4 12.4 0.0 56.0 0.0 0.000 TL 13.00 PV 0.0 Pipe: 4 0.0 1.508 PL 1.50 PF 0.0 H4 12.4 0.0 56.0 0.0 0.0 120 FTG T PE 0.0 1 12.4 0.0 56.0 0.0 0.000 TL 11.50 PV 0.0 Pipe: 5 0.0 1.508 PL 11.50 PF 0.0 1 12.4 0.0 56.0 0.0 0.0 120 FTG T PE 0.0 HS 12.4 0.0 56.0 0.0 0.000 TL 21.50 PV 0.0 Pipe: 6 0.0 1. 508 PL 0.83 PF 0.0 1 12.4 0.0 56.0 0.0 0.0 120 FTG T PE 0.7 2 10.9 0.0 56.6 0.0 0.000 TL 10.83 PV 0.0 Pipe: 7 0.0 1. 508 PL 13.00 PF 0.0 H6 12.4 0.0 56.0 0.0 0.0 120 FTG PE 0.0 H7 12.4 0.0 56.0 0.0 0.000 TL 13.00 PV 0.0 Pipe: 8 0.0 1. 508 PL 13.00 PF 0.0 H7 12.4 0.0 56.0 0.0 0.0 120 FTG PE 0.0 H8 12.4 0.0 56.0 0.0 0.000 TL 13.00 PV 0.0 Pipe: 9 0.0 1.508 PL 13.00 PF 0.0 H8 12.4 0.0 56.0 0.0 0.0 120 FTG PE 0.0 H9 12.4 0.0 56.0 0.0 0.000 TL 13.00 PV 0.0 Pipe: 10 0.0 1. 508 PL 1. 50 PF 0.0 H9 12.4 0.0 56.0 0.0 0.0 120 FTG T PE 0.0 3 12.4 0.0 56.0 0.0 0.000 TL 11.50 PV 0.0 Pipe: 11 0.0 1. 508 PL 11.50 PF 0.0 3 12.4 0.0 56.0 0.0 0.0 120 FTG T PE 0.0 Hl0 12.4 0.0 56.0 0.0 0.000 TL 21. 50 PV 0.0 Pipe: 12 0.0 1. 508 PL 0.83 PF 0.0 3 12.4 0.0 56.0 0.0 0.0 120 FTG T PE 0.7 4 10.9 0.0 56.6 0.0 0.000 TL 10.83 PV 0.0 Pipe: 13 0.0 1. 508 PL 13.00 PF 0.0 Hll 12.4 0.0 56.0 0.0 0.0 120 FTG PE 0.0 H12 12.4 0.0 56.0 0.0 0.000 TL 13.00 PV 0.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 Date: 01/17/2001 ASTONSF.SDF JOB TITLE: ASTON VIEWS SECOND FLOOR .15 FOR 2000 PIPE DATA (cont.) PIPE TAG Q(GPM) DIA ( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW (C) (FT) SUM. NODES (FT) ( K) (PSI) (GPM) F.L./FT (PSI) Pipe: 14 0.0 1. 508 PL 13.00 PF 0.0 H12 12.4 0.0 56.0 0.0 0.0 120 FTG PE 0.0 H13 12 .4 0.0 56.0 0.0 0.000 TL 13.00 PV 0.0 Pipe: 15 0.0 1. 508 PL 13.00 PF 0.0 H13 12.4 0.0 56.0 0.0 0.0 120 FTG PE 0.0 H14 12.4 0.0 56.0 0.0 0.000 TL 13.00 PV 0.0 Pipe: 16 0.0 1.508 PL 1.50 PF 0.0 H14 12.4 0.0 56.0 0.0 0.0 120 FTG T PE 0.0 5 12.4 0.0 56.0 0.0 0.000 TL 11.50 PV 0.0 Pipe: 17 0.0 1.508 PL 11.50 PF 0.0 5 12.4 0.0 56.0 0.0 0.0 120 FTG T PE 0.0 H15 12.4 0.0 56.0 0.0 0.000 TL 21.50 PV 0.0 Pipe: 18 0.0 1.508 PL 0.83 PF 0.0 5 12.4 0.0 56.0 0.0 0.0 120 FTG T PE 0.7 6 10.9 0.0 56.6 0.0 0.000 TL 10.83 PV 0.0 Pipe: 19 0.0 1.508 PL 1.50 PF 0.0 H16 12.4 0.0 56.0 0.0 0.0 120 FTG T PE 0.0 7 12.4 0.0 56.0 0.0 0.000 TL 11.50 PV 0.0 Pipe: 20 0.0 1. 508 PL 0.83 PF 0.0 7 12.4 0.0 56.0 0.0 0.0 120 FTG T PE 0.7 8 10.9 0.0 56.6 0.0 0.000 TL 10.83 PV 0.0 Pipe: 21 0.0 2.223 PL 10.00 PF 0.0 2 10.9 0.0 56.6 0.0 0.0 120 FTG PE 0.0 4 10.9 0.0 56.6 0.0 0.000 TL 10.00 PV 0.0 Pipe: 22 0.0 2.223 PL 10.00 PF 0.0 4 10.9 0.0 56.6 0.0 0.0 120 FTG PE 0.0 6 10.9 0.0 56.6 0.0 0.000 TL 10.00 PV 0.0 Pipe: 23 0.0 2.223 PL 10.00 PF 0.0 6 10.9 0.0 56.6 0.0 0.0 120 FTG PE 0.0 8 10.9 0.0 56.6 0.0 0.000 TL 10.00 PV 0.0 Pipe: 24 0.0 2.223 PL 13.58 PF 0.0 8 10.9 0.0 56.6 0.0 0.0 120 FTG T PE 0.0 9 10.9 0.0 56.6 0.0 0.000 TL 27.58 PV 0.0 Pipe: 25 174.4 2.723 PL 15.29 PF 2.8 9 10.9 0.0 56.6 0.0 9.6 120 FTG TL PE 0.0 10 10.9 0.0 53.9 0.0 0.069 TL 40.29 PV 0.6 Pipe: 26 -174.4 2.723 PL 89.67 PF 6.2 9 10.9 0.0 56.6 0.0 9.6 120 FTG PE 0.0 11 10.9 0.0 62.8 0.0 0.069 TL 89.67 PV 0.6 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 Date: 01/17/2001 ASTONSF.SDF JOB TITLE: ASTON VIEWS SECOND FLOOR .15 FOR 2000 PIPE DATA (cont.) PIPE TAG Q(GPM) DIA ( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW (C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) F.L./FT (PSI) Pipe: 27 -174.4 2.723 PL 72.00 PF 4.9 11 10.9 0.0 62.8 0.0 9.6 120 FTG PE 0.0 12 10.9 0.0 67.7 0.0 0.069 TL 72.00 PV 0.6 Pipe: 28 -174.4 2.723 PL 25.67 PF 2.0 12 10.9 0.0 67.7 0.0 9.6 120 FTG F PE 0.0 13A 10.9 0.0 69.7 0.0 0.069 TL 28.67 PV 0.6 Pipe: 28A -174.4 2.723 PL 43.12 PF 3.2 13A 10.9 0.0 69.7 0.0 9.6 120 FTG F PE 0.0 13 10.9 0.0 72.8 0.0 0.069 TL 46.12 PV 0.6 Pipe: 29 -174.4 2.723 PL 88.50 PF 6.1 13 10.9 0.0 72.8 0.0 9.6 120 FTG PE 0.0 14 10.9 0.0 78.9 0.0 0.069 TL 88.50 PV 0.6 Pipe: 30 -174.4 2.723 PL 1.00 PF 0.1 14 10.9 0.0 78.9 0.0 9.6 120 FTG PE 0.0 15 10.9 0.0 79.0 0.0 0.069 TL 1.00 PV 0.6 Pipe: 31 -174.4 2.723 PL 43.17 PF 3.4 15 10.9 0.0 79.0 0.0 9.6 120 FTG L PE 0.0 15A 10.9 0.0 82.4 0.0 0.069 TL 49.17 PV 0.6 Pipe: 31A -174.4 4.328 PL 5.17 PF 0.0 15A 10.9 0.0 82.4 0.0 3.8 120 FTG PE 0.0 34 10.9 0.0 82.4 0.0 0.007 TL 5.17 PV 0.1 Pipe: 32 -358.6 4.328 PL 62.17 PF 2.1 34 10.9 0.0 82.4 0.0 7.8 120 FTG 2L PE 0.0 16 10.9 0.0 84.5 0.0 0.027 TL 78.17 PV 0.4 Pipe: 33 -358.6 4.328 PL 10.88 PF 0.3 16 10.9 0.0 84.5 0.0 7.8 120 FTG PE 4.7 BOR 0.0 H.S. 89.5 100.0 0.027 TL 10.88 PV 0.4 Pipe: 34 -19.5 1.508 PL 13.00 PF 0.3 H17 29.0 5.6 12.1 19.5 3.5 120 FTG PE 0.0 H18 29.0 5.6 12.4 19.7 0.021 TL 13.00 PV 0.1 Pipe: 35 -39.2 1.508 PL 13.00 PF 1.0 H18 29.0 5.6 12.4 19.7 7.0 120 FTG PE 0.0 H19 29.0 5.6 13.4 20.5 0.077 TL 13.00 PV 0.3 Pipe: 36 -59.7 1.508 PL 13.00 PF 2.2 H19 29.0 5.6 13.4 20.5 10.7 120 FTG PE 0.0 H20 29.0 5.6 15.6 22.1 0.168 TL 13.00 PV 0.8 Pipe: 37 -81.8 1.508 PL 1. 50 PF 3.5 H20 29.0 5 .6 15.6 22.1 14.7 120 FTG T PE 0.0 17 29 .0 0.0 19.1 0.0 0.301 TL 11.50 PV 1. 5 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 Date: 01/17/2001 ASTONSF.SDF JOB TITLE: ASTON VIEWS SECOND FLOOR .15 FOR 2000 PIPE DATA (cont.) PIPE TAG Q(GPM) DIA ( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW (C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) F.L./FT (PSI) Pipe: 38 24.0 1. 508 PL 9.50 PF 0.6 17 29.0 0.0 19.1 0.0 4.3 120 FTG T PE 0.0 H21 29.0 5.6 18.4 24.0 0.031 TL 19.50 PV 0.1 Pipe: 39 -105.9 1. 508 PL 0.83 PF 5.3 17 29.0 0.0 19.1 0.0 19.0 120 FTG T PE 0.6 18 27.5 0.0 25.0 0.0 0.485 TL 10.83 PV 2.4 Pipe: 40 -19.8 1.508 PL 13.00 PF 0.3 H22 29.0 5.6 12.5 19.8 3.6 120 FTG PE 0.0 H23 29.0 5.6 12.8 20.0 0.022 TL 13.00 PV 0.1 Pipe: 41 -39.8 1.508 PL 13.00 PF 1.0 H23 29.0 5.6 12.8 20.0 7.2 120 FTG PE 0.0 H24 29.0 5.6 13.8 20.8 0.079 TL 13.00 PV 0.3 Pipe: 42 -60.6 1. 508 PL 13.00 PF 2.2 H24 29.0 5.6 13.8 20.8 10.9 120 FTG PE 0.0 H25 29.0 5.6 16.1 22.4 0.173 TL 13.00 PV 0.8 Pipe: 43 -83.1 1. 508 PL 1.50 PF 3.6 H25 29.0 5.6 16.1 22.4 14.9 120 FTG T PE 0.0 19 29.0 0.0 19.6 0.0 0.310 TL 11.50 PV 1.5 Pipe: 44 24.4 1. 508 PL 9.50 PF 0.6 19 29.0 0.0 19.6 0.0 4.4 120 FTG T PE 0.0 H26 29.0 5.6 19.0 24.4 0.032 TL 19.50 PV 0.1 Pipe: 45 -107.5 1.508 PL 0.83 PF 5.4 19 29.0 0.0 19.6 0.0 19.3 120 FTG T PE 0.6 20 27.5 0.0 25.7 0.0 0.499 TL 10.83 PV 2.5 Pipe: 46 -20.9 1. 508 PL 13.00 PF 0.3 H27 29.0 5.6 13.9 20.9 3.8 120 FTG PE 0.0 H28 29.0 5.6 14.2 21.1 0.024 TL 13.00 PV 0.1 Pipe: 47 -42.0 1.508 PL 13.00 PF 1.1 H28 29.0 5.6 14.2 21.1 7.5 120 FTG PE 0.0 H29 29.0 5.6 15.4 21. 9 0.088 TL 13.00 PV 0.4 Pipe: 48 -63.9 1. 508 PL 13.00 PF 2.5 H29 29.0 5.6 15.4 21. 9 11.5 120 FTG PE 0.0 H30 29.0 5.6 17.8 23.6 0.191 TL 13.00 PV 0.9 Pipe: 49 -87.6 1.508 PL 1.50 PF 3.9 H30 29.0 5.6 17.8 23.6 15.7 120 FTG T PE 0.0 21 29.0 0.0 21. 8 0.0 0.341 TL 11.50 PV 1. 7 Pipe: 50 25.7 1. 508 PL 9.50 PF 0.7 21 29.0 0.0 21. 8 0.0 4.6 120 FTG T PE 0.0 H31 29.0 5.6 21.1 25.7 0.035 TL 19.50 PV 0.1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 Date: 01/17/2001 ASTONSF.SDF JOB TITLE: ASTON VIEWS SECOND FLOOR .15 FOR 2000 PIPE DATA (cont.) PIPE TAG Q(GPM) DIA ( IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) F.L./FT (PSI) Pipe: 51 -113.3 1. 508 PL 0.83 PF 6.0 21 29.0 0.0 21. 8 0.0 20.4 120 FTG T PE 0.6 22 27.5 0.0 28.4 0.0 0.550 TL 10.83 PV 2.8 Pipe: 52 -31. 9 1. 508 PL 1. 50 PF 0.6 H32 29.0 5.6 32.4 31.9 5.7 120 FTG T PE 0.0 23 29.0 0.0 33.0 0.0 0.053 TL 11.50 PV 0.2 Pipe: 53 -31. 9 1.508 PL 0.83 PF 0.6 23 29.0 0.0 33.0 0.0 5.7 120 FTG T PE 0.6 24 27.5 0.0 34.3 0.0 0.053 TL 10.83 PV 0.2 Pipe: 54 -105.9 2.223 PL 10.00 PF 0.7 18 27.5 0.0 25.0 0.0 8.8 120 FTG PE 0.0 20 27.5 0.0 25.7 0.0 0.073 TL 10.00 PV 0.5 Pipe: 55 -213.4 2.223 PL 10.00 PF 2.7 20 27.5 0.0 25.7 0.0 17.6 120 FTG PE 0.0 22 27.5 0.0 28.4 0.0 0.268 TL 10.00 PV 2.1 Pipe: 56 -326.7 2.223 PL 10.00 PF 5.9 22 27.5 0.0 28.4 0.0 27.0 120 FTG PE 0.0 24 27.5 0.0 34.3 0.0 0.589 TL 10.00 PV 4.9 Pipe: 57 -358.6 2.723 PL 13.58 PF 8.5 24 27.5 0.0 34.3 0.0 19.8 120 FTG T PE 0.0 25 27.5 0.0 42.7 0.0 0.261 TL 32.58 PV 2.6 Pipe: 58 -174.4 2.723 PL 15.29 PF 2.8 25 27.5 0.0 42.7 0.0 9.6 120 FTG TL PE 0.0 26 27.5 0.0 45.5 0.0 0.069 TL 40.29 PV 0.6 Pipe: 59 -174.4 2.723 PL 16.62 PF 1.1 26 27.5 0.0 45.5 0.0 9.6 120 FTG PE 7.2 10 10.9 0.0 53.9 0.0 0.069 TL 16.62 PV 0.6 Pipe: 60 -184.2 2.723 PL 95.67 PF 7.3 25 27.5 0.0 42.7 0.0 10.1 120 FTG PE 0.0 27 27.5 0.0 50.0 0.0 0.076 TL 95.67 PV 0.7 Pipe: 61 -184.2 2.723 PL 70.42 PF 5.4 27 27.5 0.0 50.0 0.0 10.1 120 FTG PE 0.0 28 27.5 0.0 55.4 0.0 0.076 TL 70.42 PV 0.7 Pipe: 62 -184.2 2.723 PL 20.50 PF 1. 8 28 27.5 0.0 55.4 0.0 10.1 120 FTG F PE 0.0 29A 27.5 0.0 57.1 0.0 0.076 TL 23.50 PV 0.7 Pipe: 62A -184.2 2.723 PL 33.33 PF 2.8 29A 27.5 0.0 57.1 0.0 10.1 120 FTG F PE 0.0 29 27.5 0.0 59.9 0.0 0.076 TL 36.33 PV 0.7 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Date: 01/17/2001 JOB TITLE: ASTON VIEWS SECOND FLOOR .15 FOR 2000 PIPE DATA (cont. ) PIPE TAG Q(GPM) DIA(IN) LENGTH END ELEV. NOZ. NODES (FT) (K) 29 30 30 31 31 32 32 33 33 34 BOR UI UI U2 Pipe: 63 27.5 27.5 Pipe: 64 27.5 27.5 Pipe: 65 27.5 27.5 Pipe: 66 27.5 10.9 Pipe: 67 10.9 10.9 Pipe: 68 0.0 0.0 Pipe: 69 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 H.S. 0.0 0.0 0.0 PT DISC. VEL(FPS) HW(C) (FT) (PSI) (GPM) F.L./FT 59.9 66.5 66.5 67.1 67.1 71. 9 71.9 80.3 80.3 82.4 89.5 89.6 89.6 89.7 -184.2 0.0 10.1 0.0 -184.2 0.0 10.1 0.0 -184.2 0.0 10.1 0.0 -184.2 0.0 10.1 0.0 -184.2 0.0 10.1 0.0 -458.6 100.0 2.7 0.0 -458.6 0.0 2.9 0.0 2.723 PL 120 FTG 0.076 TL 2.723 PL 120 FTG 0.076 TL 2.723 PL 120 FTG 0.076 TL 2.723 PL 120 FTG 0.076 TL 2.723 PL 120 FTG 0.076 TL 8.390 PL 140 FTG 0.001 TL 8.044 PL 150 FTG 0.001 TL 87.29 87.29 7.00 7.00 51. 00 2L 63.00 16.62 16.62 2.33 TL 27.33 11. 00 2L 55.00 25.00 TL 73.00 Page 8 ASTONSF.SDF PRESS. SUM. (PSI) PF PE PV PF PE PV PF PE PV PF PE PV PF PE PV PF PE PV PF PE PV 6.6 0.0 0.7 0.5 0.0 0.7 4.8 0.0 0.7 1.3 7.2 0.7 2.1 0.0 0.7 0.1 0.0 0.0 0.1 0.0 0.1 Pipe: 70 0.0 0.0 FIXED PRESSURE LOSS DEVICE U3 U2 U3 U4 Pipe: 71 0.0 0.0 NOTES: 0.0 0.0 0.0 SRCE 93.2 89.7 93.2 93.3 0.0 3.5 psi, 458.6 gpm 0.0 -458.6 0.0 2.9 (N/A) 8.044 PL 150 FTG 0.001 TL 22.00 T2LG 87.00 PF PE PV 0.1 0.0 0.1 (1) Calculations were performed by the HASS 6.5.0 computer program under license no. 38010408 granted by HRS Systems, Inc. 4792 Lavista Road Tucker, GA 30084 (2) The system has been balanced to provide an average imbalance at each node of 0.001 gpm and a maximum imbalance at any node of 0.098 gpm. (3) Velocity pressures are printed for information only, and are not used in balancing the system. Maximum water velocity is 27.0 ft/sec at pipe 56. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Date: 01/17/2001 JOB TITLE: ASTON VIEWS SECOND FLOOR .15 FOR 2000 (4) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet ( in) E T L C B G Ell Tee LngEll ChkVlv BfyVlv GatVlv 8.390 31. 00 60.00 22.00 78.00 21. 00 7.00 PAGE: E MATERIAL: PVC150 HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G Ell Tee LngEll ChkVlv BfyVlv GatVlv 8.044 26.00 35.00 13.00 45.00 17.00 4.00 PAGE: J MATERIAL: FIRELINE HWC: 120 Diameter Equivalent Fitting Lengths in · Feet (in) E T L C B G Page 9 ASTONSF.SDF N NPTee 60.00 N F NPTee 45 35.00 9.00 A D Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPVlv N F NPTee 5 1.508 5.00 10.00 3.00 12.00 12.00 2.00 20.00 17.00 7.00 1.00 2.223 7.00 14.00 4.00 15.00 10.00 1.00 17.00 14.00 12.00 2.00 2.723 10.00 19.00 6.00 22.00 16.00 2.00 22.00 16.00 17.00 3.00 4.328 14.00 28.00 8.00 31. 00 22.00 4.00 35.00 14.00 26.00 4.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Date: 01/17/2001 JOB TITLE: ASTON VIEWS SECOND FLOOR .15 FOR 2000 WATER SUPPLY CURVE p R E s s u R E ( p s I ) 108+ I *\\\\\\\\\\\ I o \\\\\\\\\\\\ 99+ \\\\\\\\\\\\ 90+ 81+ 72+ 63+ 54+ 45+ 36+ 27+ 18+ X 9+ 0 = \\\\\\\\\\\ 94.5 psi@ 1683 gpm-> * X Flow Test Point LEGEND Required Water Supply 93.34 psi@ 608.6 gpm " " " " " = Available Water Supply II 102.13 psi @ 608.6 gpm II II Page 10 ASTONSF.SDF O++-+---+----+-----+------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) · ...... _ LOBE. AUTOMATIC SPRINKLERS MODEL JN BULB $PRA-Y SERIES FIRE SPRINKLER - CORPORATION ·-UPRIGHT•PENDENT VERTICAL-SIDEWALL HORIZONTAL SIDEWALL CONVENTIONAL (OLD STYLE) DESCRIPTION AND OPERATION· The Globe Model JN. Sprinkler is a low profile yet durable design which utilizes a frangible glass ampule as the thermosensitive element While the sprinkler provides an aesthetically pleasing appearance, it can be installed wherever standard spray sprinklers are specified. This sprinkler series is available in various styles, orifices, temperature ratings and finishes to meet varying--design requirements. · The heart of Globe's Model JN sprinkler proven actuating assembly is a hermetically sealed-frangible glass ampule that contains a precisely measured amount of fluid. When heat is absorbed, the liquid within the bulb expands increasing the internal pressure. At the prescribed temperature the internal pressure within the ampule exceeds the strength of the glass cau_sing the glass to shatter. This results in water discharge which is· distributed in ---an approved pattern depending upon the deflector style used. TECHNICAL DATA " U.S. Patent No. 5,494, I 14. ~ See reverse side for Approvals and Specifications. Temperature Ratings -I 35°F (57°C), I 55°F (68°C}, I 75°F (79°C}, 200°F (9~°C}, 286 °F ( 141 °C), 360°F ( 1· 82°C}, 500°F (260°C). o Water Working Pressure Rating -175 psi (12 Bars). @ Factory tested hydrostatically to 500 psi (34 Bars). • Maximum low temperature glass bulb rating is -67°F (-55°C). e Frame -bronze • Deflector -brass ® Screw -brass Bulb seat -engineered plastic ~ O-ring -silicone elastomer ~ Bulb -glass with glycerin solution, 5mm size. UPRIGHT PENDENT ,, ~\ tA ::.:-:· ,.., •::«-' ... · ·:•~:-- CONVENTIONAL . VERTICAL · SIDEWALL HORIZONTAL SIDEWALL -SPRINKLER TEMPERATURE RATING/CLASSIFICATION and COLOR. CODING AVAILABLE CLASSIFICATION . SPRINKLER .TEMPERATURES ORDINARY INTERMEDIATE HIGH EXTRA HIGH ULTRA HIGH 4077 AIRPARK DRIVE, STANDISH, MICHIGAN 48658 APRIL 1998 A-12N BULB COLOR ORANGE/RED YELLOW/GREEN BLUE MAUVE BLACK N.F.P.A. MAXIMUM CEILING TEMPERATURE 517-846-4583 • FAX 517-846-9231 .. BULLETIN JN-1, ·REV. #4 ·~AUTOMATIC SPRINKLERS MODEL JN BULB SPRAY SERIES UPRIGHT• PENDENT• VERTICAL SIDEWALL ·-· HORIZONTAL SIDEWALL • CONVENTIONAL (OLD STYLE) SPECIFICATIONS ORIFICE SIZE NOMINAL "K" FACTOR THREAD SIZE *LENGTH FINISHES 3/8" (10 mm) 2.8 .. 7/16" (12.5 _mm) 4.2 1/2" (15 mm) 5.6 17/32" (20 mm) 7.8 17/32" (20 mm) 8.1 NOTE: METRIC CONVERSIONS ARE APPROXIMATE. IJS•F 1ss•F 175•f STYLE ORIFICE SIZE 57•c ,a•c 79•c 3/8" X X X 7/16" X X X UPRIGHT 1/2" X X X 17/32 ... X X X · 17/32" X X X 3/8" X X X 7/16" X X X PENDENT 1/2" X X X 17/32'>:ft. X X X 17/32" X X X 3/8" t X X X VERTICAL 7/16" X X X SIDEWALL t . 1/2" X X X 3/8" X X X HORIZONTAL 7/16" X X X SIDEWALL§ 1/2" X X X CONVENTIONAL 1/2" X X X · (OLD STYLE) 17/32" X X X ORDERING INFORMATION SPECIFY Quantity Model Number , Style Orifice <, Thread Sizes ,, Temperature Finishes desired (39 metric) 1/2" NPT (59 metric) 1/2" NPT (80 metric) 1/2" NPT ( I 11 metric) 1/2" NPT (116 metric) 3/4" NPT APPROVALS 2oo•F t~60•F tt 2&6•F soo•F U.L 93•c 1ie1•c 112·c 2,o•c X X X X X X X X X ·x X X X X X X X X X X X X X X X X X X X X X X X X X X X X X X X X X X X X X X X X X X X X X X X X X X X X X X ·X X X X X X X X •.. ~ 1/4" (5.7 cm) Factory Bronze ~tin Chrome ~2 1/4" (5.7 cm) Bright Chrome 2 1/4" (5.7 cm) White Polyester Black Polyester ~ 1/4" (5.7 cm)" w-ax··coated ~Lead Coated 2 7/16" (6.2 cm) ~over lead ··• HORIZONTAL SIDEWALL IS l 9/16". ** EXCLUDING PINTLE. *** FINISHES AVAILABLE ON SPEOAL ORDER. ****WAX COATING U.L LISTED uP:ro 2oo·F ONLY .. CANADIAN F.M. LP.C. N.Y.C. -D.O.B. U.L MEA IO 1-92-E X --X X ·--X . ~-. ... X X X X X X -X X X X X X -----X X ---X '" X . "X X X X X -X X :x X X X -----X X -X .. X X -X X -.. -X X ---X X X -X .. X -X X X -X X I HORIZONTAL SIDEWALL UL LIITTD FOR DEFLECTOR◄" TO 12" BELOW.THE CEILING. t VERTICAL SIDEWALL UL LISTED FOR LIGHT HAZARD ONLY. t 3/8" VERTICAL SIDEWALL UL LISTED FOR UPRIGHT INSTALLATION ONLY. • 17/32" X 1/2" NPT. tt 360°F AND S00°F ARE MODEL "J." GLOBE® PRODUCT WARRANTY Quantity -Model JN Wrenches -PIN 325390 (1/2"); P/N 312366 (LO.) Globe agrees to repair or replace any of its own manufac- tured products found to be defective in material or workman- ship for a period of one year_ from date of s~ipment. For specific details of o'ur warranty please refer to Price List Terms and Conditions of~ale (Our·Price List). LOBE FIRE SPRINKLER CORPORATION 4077 AIRPARK DRIVE, STANDISH, MICHIGAN 48658 517-846-4583 FAX 517-846-9231 1-800~248-0278 www.globesprinkler.com APRIL 1998 PRINTED U.S.A. BULLETIN JN-1, REV. #4 LOBE® QUICI( RESPONSE AUTOMATIC SPRINKLERS . FIRE SPRINKLER CORPORATION · MODEL JN BlJLB SPRAirSJtRIES . RECESSE»··-_PENDENT . RECESSED VERTICAL SIDEWALL D 0. RECESSED HORIZONTAL SIDEWALL ESCRIPTION AND 1'ERATION . .. . _· The Globe Quick Response Model JN Sprinkler is a low profile yet durable design which utilizes a 3mm frangible glass ampule as the thermosensitive element. This provides sprinkler operation approxi- mately six times faster than ordinary sprinklers. While the Quick Response Sprinkler provides an aesthetically pleasin_g appearance, it can · be installed wherever standard spray sprinklers are specified but offers the additional feature of greatly increased safety to life. Quick Response Sprinklers should be used advisedly and under the direction of approving authorities having jurisdiction .. The heart of Globe's Model JN sprinkler proven actuating assembly is a hermetically sealed frangible glass ampule that contains a precisely measured amount of fluid. When heat is absorbed, the liquid within the bulb expands increasing the internal pressure. At the prescribed temperature the internal pressure within the ampule exceeds the strength of the glass caus.ing the glass to shatter. This results in water discharge which is distributed in an approved pattern depending upon the deflector style used. The patented seat design consists of an engineered plastic seat and silicone o-ring. This combination has advantages over other types of seating arrangements, in that the plastic seat is an insulator which provides for no heat loss from the bulb to the water in the system, resulting in faster response. In addition, the plastic seat is not subject to corrosion or deterioration by chemicals, bacteria or electrolysis. TECHNICAL DATA U.S. Patent No. 5,494, I 14. ·· See reverse side for Approvals and Spedfications. Temperature Ratings -I 35°F (57°C), I 55°F (68°C), I 75°F (79°C), · 200°F (93°C), 286°F (141 °C). Water Working Pressure Rating -175 psi ( 12 Bars). < Factory tested hydrostatically to 500 psi (34 Bars). Maximum low temperature glass bulb rating is -67°F (-SS°C). Frame -bronze ,. Deflector -brass Screw -brass Bulb seat -engineered plastic _ O-ring -silicone elastomer Bulb -glass with alcohol based solution, 3mm size. Escutcheon Assembly -steel -· QUICK RESPONSE . · .. RECESSED PENDENT .... QUICK R_ESPONSE RECESSED VERTICAL SIDEWALL QUICK RESPONSE RECESSED HORIZONTAL SIDEWALL •.. SPRINKLER TEMPERATURE RATING/CLASSIFICATION and COLOR CODING CLASSIFICATION ORDINARY INTERMEDIATE HIGH AVAILABLE SPRINKLER TEMPERATURES 79°C/93°C I4I°c 4077 AIRPARK DRIVE, STANDISH, MICHIGAN 48658 DECEMBER 1998 A-7N BULB ·· COLOR ORANGE/RED YELLOW/GREEN BLUE N·.F.P.A. MAXIMUM CEILING TEMPERATURE 66°C . 'io7°C 517-846-4583 • FAX 517-846-9231 BULLETIN JN-Q.R. RECESSED. REV. #4 QUICK RESPONSE AUTOMATIC SPRINKLERS MODEL JN BULB .SPRAY SERIES RECESSED PENDENT• ·RECESSED VERTICAL SIDEWALL . RECESSED HORIZONTAL SIDE-WALL SPECIFICATIONS .. ORIFICE SIZE NOMINAL "K" FACTOR ··· THREAD SIZE· *LENGTH FINISHES 3/8" (10 mm) 2.8 (39 metric) 1/2" NPT :+o1c2 1 /4" (5.7 cm) Factory Bronze 7/16" (12.5 mm) 4.2 (59 metric) 1/2" NPT ~ 114" (5.7 cm) :tc:+:itcSatin Chrome Bright Chrome 1/2" (IS mm) 5.6 (80 metric) 1/2" NPT. 2 1/4'.' (5.7 cm) White Polyester+ --· '17/32" (20 mm) 7.8 .. ( 111 metric) 1/2" NPT :+o1c2 1/4., (5.7 cm) Black Polyester+ 17/32" (20 mm) 8.1 ( 116 metric) 3/4" NPT 2 7/16" (6.2 cm) :toFtcLead Coated NOTE: METRIC CONVERSIONS ARE APPROXIMATE. ~ORIZONTAL SIDEWALL IS 2 9/16N. ,...EXCLUDING PINTLE. APPROVALS STYLE ORIFICE 135°F 155°F 175°F 200°F 286°F SIZE s1°c 68°C 1,·c 93•c 1 ◄1°c · 3/8" X X X X X · 7/16" X X X X X PENDENT 1/2" X X X X X RECESSED t 17/32"* X X X X X 17/32" X X . X X X VERTICAL SIDEWALL 7/16" X X · X X X RECESSED; 1/2" X X X X X .. 3/8" X X X x ··· X HORIZONTAL SIDEWALL 7/16" X X X X X RECESSED§ 1/2" X X X X X 17/32" x-X X X X U.L. X X X X X X X X X X X ~INISHES AVAILABLE ON SPECIAL ORDER. +AVAILABLE AS UL LISTED CORROSION RESISTANT WHEN SPECjflED ON ORDER. ... CANADIAN F.M. L.P.C. N.Y.C. -D.O.B. U.L. MEA 101-92-E· X ------X X ------X X ··x X X X X ---X X X X X X ------X X ' ------X . . X ·------X X -----X X -----X X -----X CROSS SECTIONS §HORIZONTALSIDEWALLU.LANDC-U.LLISTEDFORDEFLECTOR◄NTO ll"BELOWTHECEILING. . . · . tLISTED FOR ALL HAZARDS. RETAINER ·i ,• MIN. 1/8'....J 1 .~./.: .. MAX. -----' PENDENT LOBE® FIRE SPRINKLER CORPORATION · DECEMBER 1998 2 W 15• DIA. tVERTICAL SIDEWALL U.L AND C-U.L LISTED FOR LIGHT HAZARD ONLY . ..&cO:-cc~ *17/32"Xl/l"NPT. ORDERING INFORMATION SPECIFY 1..-+~--r7"7 7¼~-::::;_,-'• Quantity Model Number Style l-1\1-~~~~__j:::::!J "Orifice " Thread Sizes .' Temperature 11a· : Finishes desired VERTICAL SIDEWALL . Quantity -Model JN Recessed Wrenches -P/N 325391 (I /2"); P/N 32540 I, Rev. -F (LO.) I'" ll 1/2'"...., REDUCER R£TAIN[R HORIZONTAL SIDEWALL GLOBE® PROD-UCT WARRANTY Globe agrees to repair or replace any of.its own manufac- tured products found to be defective in material or workman- ship for a period of one year from date of shipment. For specific details of our warranty please refer to Price List Terms and Con.ditions of Sale (Our Pi-ice List). 4077 AIRPARK DRIVE, STANDISH, MICHIGAN 48658 517-846-4583 FAX 517-846-9231 1-800-248-0278 www.globesprinkler.com PRINTED U.S.A. · BULLETIN JN-Q.R. RECESSED. REV. #4