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HomeMy WebLinkAbout5781 VAN ALLEN WAY; ; AS090145; PermitCity of Carlsbad Sprinkler Permit Permit No: AS090145 5781 VAN ALLEN Job Address: WY Permit Type: SPRINK Parcel No: 2121304400 Lot #: 0 Status: ISSUED Applied 11/18/2009 Approved: 11/25/2009 Reference No.: Issued: 11/25/2009 PC #: Inspector: Project Title: LIFE TECHNOLOGIES THREE FIRE SPRINKLER INSPECTIONS @ $65/EA Applicant: WESTERN FIRE PROTECTION 13630 DANIELSON P0 WAY CA 858-513-4949 Owner: GRIFFIN CAPITAL CARLSBAD POINTE INVESTORS L L C C/O INVITROGEN CORPORATION 1600 FARADAY AVE CARLSBAD CA Fees ($) Add'I Fees ($) Total ($) Balance ($) 195 0 195 0 I I I I I I I I I I I I I I I I I I I WESTERN FIRE PROTECTION, INC. REMOTE AREA U 13630 DANIELSON STREET POWAY,CA 92064 HYDRAULIC CALCULATIONS FOR LIFE TECHNOLOGIES 5781 VAN ALLEN WAY CARLSBAD, CA 92008 "FILE NUMBER: C-2625 DATE: NOV 13, 2009 -DESIGN DATA- OCCUPANCY CLASSIFICATION: GROUP A PLASTICS CARTONED DENSITY: 0.30 GPM PER SQ.FT. AREA OF APPLICATION: 2000 SQ.FT. @ ROOF + 13 IN-RACK COVERAGE PER SPRINKLER: 80 SQ.FT. MAX NUMBER OF SPRINKLERS CALCULATED: 26 AT ROOF, 13 IN-RACKS ROOF SPRINKLER DEMAND: (8 NODE X6) 905.7 GPM 8 53.2 PSI IN-RACK DEMAND: (8 NODE X6): 314.0 GPM 8 53.2 PSI FLOW AND PRESSURE (8 BOR) : 1219.7 GPM @ 55.9 PSI TOTAL WATER REQUIRED (including hose): 1727.4 GPM SPRINKLER K FACTOR: K=8.0 AT ROOF, K=5.6 IN-RACKS DESIGN/LAYOUT BY: G.RUIZ AUTHORITY HAVING JURISDICTION: CARLSBAD FIRE DEPARTMENT CONTRACTOR CERTIFICATION NUMBER: CALCULATIONS BY H ASS COMPUTER PROGRAM (LICENSE # 50040828 HRS SYSTEMS, INC. TUCKER, GA 30084 TUCKER, GA 30084 These htLfl to 1tipsLe1t( Ctl1t W, the cuIT' ptch CC md tiitdiI d' in tot L C the kdCI' The oWil1' of COIOI lCtO tlfll\ iitthiC ht fC t' LtppOO ot alt apPiC alto't it bit ti timg 10, 111110 w,v retie\ en the 1wtiec Of COB" actot t thtt ptnttt With the P1' 11tct,autdt IS thjt ttii ' or rchltCC' tOI M1C tol lult ottpha11 with nad codes and I11dii1d'. t ,11_.IE 1?'{ Ole- "I" huthhng c1tdc or for any r jigellce enpoit.thdtY to, (t,C,CI1UCS. errors. lii ptatr' Whether or itot IiOtC' ttii I RtC )MMEm ppPK(.)VAL 0 t.ttCOMMt) APPh(t AS I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 11/13/2009NOLOGIES RACKS\CALCULATIONS\AREA A RACK D-CT FEEDREV.SDF JOB TITLE: Area "A" Racks IWATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D I NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SRC 111.6 102.6 1060.0 89.6 1719.7 73.5 AGGREGATE FLOW ANALYSIS: TOTAL TOTAL FLOW AT SOURCE HOSE STREAM ALLOWANCE AT SOURCE 1719.7 500.0 GPM GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 1219.7 GPM I NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE I (FT) (PSI) (GPM) Si 31.8 K= 8.00 18.4 34.3 I S2 31.8 K= 8.00 18.0 34.0 S3 31 O K= 8.00 17.9 33.9 S4 3.8 K= 8.00 17.9 33.9 31.8 K= 8.00 18.0 33.9 I S5 S6 31.8 K= 8.00 18.2 34.2 S7 31.8 K= 8.00 18.8 34.7 31.8 K= 8.00 19.8 35.6 I S8 S9 31.8 K= 8.00 18.4 34.3 S1O 31.8 K= 8.00 18.1 34.0 Sil 31.8 K= 8.00 18.0 33.9 31.8 K= 8.00 18.0 33.9 I S12 S13 31.8 K= 8.00 18.0 34.0 S14 31.8 K= 8.00 18.3 34.2 S15 31.8 K= 8.00 18.9 34.7 I S16 31.8 K= 8.00 19.9 35.7 S17 31.8 K= 8.00 18.5 34.4 S18 31.8 K= 8.00 18.2 34.1 I S19 31.8 K= 8.00 18.1 34.0 S20 31.8 K= 8.00 18.1 34.0 S21 31.8 K= 8.00 18.2 34.1 S22 31.8 K= 8.00 18.4 34.3 I S23 31.8 K= 8.00 19.0 34.9 S24 31.8 K= 8.00 20.0 35.8 I S25 S26 31.8 31.8 K= K= 8.00 8.00 25.6 25.6 40.5 40.5 1 9.2 K= 5.60 16.9 23.0 2 9.2 K= 5.60 17.0 23.1 1 39.2 K= 5.60 17.3 23.3 4 9.2 K= 5.60 18.4 24.0 5 9.2 K= 5.60 19.8 24.9 6 4.2 K= 5.60 28.4 29.8 I 7 18.2 K= 5.60 15.0 21.7 8 18.2 K= 5.60 15.1 21.8- I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 11/13/2009NOLOGIES RACKS\CALCULATIONS\AREA A RACK D-CT FEED-REV.SDF JOB TITLE: Area "A" Racks NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE I (FT) (PSI) (GPM) 9 18.2 K= 5.60 15.4 22.0 10 18.2 K= 5.60 16.0 22.4 I 11 18.2 K= 5.60 17.4 23.4 12 18.2 K= 5.60 22.3 26.5 13 18.2 K= 5.60 25.2 28.1 4.2 - - - - 37.5 - - I Xl X2 18.2 - - - - 32.2 - - - X3 30.0 - - - - 31.4 - - - - X4 30.0 - - - - 34.7 - - - X5 30.0 - - - - 41.2 - - - X6 3.0 - - - - 53.2 - - - Ri 31.8 - - - - 22.9 - - - I R2 31.8 - - - - 26.0 - - - R3 31.8 - - - - 23.0 - - - R4 31.8 - - - - 26.0 - - - 31.8 - - - - 23.2 - - - I R5 R6 31.8 - - - - 26.1 - - - R7 31.8 - - - - 26.3 - - - R8 31.8 - - - - 27.2 - - - I R9 31.8 - - - - 27.1 - - - RiO 31.8 - - - - 27.7 - - - Rll 31.8 - - - - 27.6 - - - 31.8 - - - - 28.1 - - - I R12 R13 31.8 - - - - 28.2 - - - R14 31.8 - - - - 28.5 - - - I RiS R16 31.8 31.8 - - - - - - - - 28.7 28.9 - - - - - -. R17 31.8 - - - - 29.2 - - - R18 31.8 - - - - 29.3 - - - R19 31.8 - - - - 29.6 - - - I R20 31.8 - - - - 29.7 - - - R21 31.8 - - - - 30.1 - - - R22 31.8 - - - - 30.2 - - - I R23 31.8 - - - - 30.6 - - - R24 31.8 - - - - 30.6 - - - R25 31.8 - - - - 31.0 - - - I R26 31.8 - - - - 31.1 - - - R27 31.8 - - - - 31.4 - - - R28 31.8 - - - - 31.6 - - - R29 31.8 - - - - 31.8 - - - I R30 31.8 - - - - 32.1 - - - R31 31.8 - - - - 32.2 - - - I R32 R33 31.8 31.8 - - - - - - - - 32.6 32.6 - - - - - - R34 31.8 - - - - 33.2 - - - R35 31.8 - - - - 32.9 - - - R36 31.8 - - - - 33.7 - - - I R37 31.8 - - - - 33.3 - - - R38 31.8 - - - - 34.4 - - - R39 31.8 - - - - 33.5 - - - I R40 31.8 - - - - 34.6 - - - R41 31.8 - - - - 33.7 - - - I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 11/13/2009NOLOGIES RACKS\CALCULATIONS\AREA A RACK D-CT FEED-REV.SDF JOE TITLE: Area "A" Racks I NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE I (FT) (PSI) (GPM) R42 31.8 - - - - 34.7 - - - I R43 31.8 - - - - 33.9 - - - R44 31.8 - - - - 34.8 - - - R45 31.8 - - - - 34.1 - - - R46 31.8 - - - - 34.9 - - - I R47 31.8 - - - - 34.2 - - - R48 31.8 - - - - 35.1 - - - R49 31.8 - - - - 34.3 - - - l RSO 31.8 - - - - 35.2 - - - R51 31.8 - - - - 34.4 - - - R52 31.8 - - - - 35.4 - - - R53 31.8 - - - - 34.4 - - - ' R54 31.8 - - - - 35.5 - - - R55 31.8 - - - - 34.5 - - - R56 31.8 - - - - 35.7 - - - I R57 31.8 - - - - 34.5 - - - R58 31.8 - - - - 35.9 - - - R59 31.8 - - - - 34.6 - - - R60 31.8 - - - - 36.1 - - - I R61 31.8 - - - - 34.6 - - - R62 31.8 - - - - 36.3 - - - Ml 30.8 - - - - 25.9 - - - I M2 30.8 - - - - 27.5 - - - M3 30.8 - - - - 26.0 - - - M4 30.8 - - - - 27.6 - - - I M5 30.8 - - - - 26.3 - - - M6 30.8 - - - - 27.7 - - - M7 30.8 - - - - 26.8 - - - M8 30.8 - - - - 27.9 - - - I M9 30.8 - - - - 27.5 - - - MiD 30.8 - - - - 28.2 - - - Mil 30.8 - - - - 28.0 - - - I M12 30.8 - - - - 28.6 - - - M13 30.8 - - - - 28.6 - - - M14 30.8 - - - 28.9 - - - I MiS 30.8 - - - - 29.1 - - - M16 30.8 - - - - 29.3 - - - M17 30.8 - - - - 29.6 - - - M18 30.8 - - - - 29.8 - - - I M19 30.8 - - - - 30.1 - - - M20 30.8 - - - - 30.2 - - - M21 30.8 - - - - 30.5 - - - I M22 30.8 - - - - 30.6 - - - M23 30.8 - - - - 31.0 - - - M24 30.8 - - - - 31.1 - - - M25 30.8 - - - - 31.4 - - - I M26 30.8 - - - - 31.6 - - - M27 30.8 - - - - 31.8 - - - M28 30.8 - - - - 32.0 - - - I M29 30.8 - - - - 32.2 - - - M30 30.8 - - - - 32.5 - - - M31 30.8 - - - - 32.6 - - - I 1 NODE ANALYSIS DATA NODE TAG ELEVATION I (PT) M32 M33 I M34 M35 M36 I M37 M38 M38A I M39 M40 M41 M42 I M43 M44 M45 I M46 M47 M48 M49 M50 M51 M52 I M53 M54 M55 I M56 M57 M58 M59 I M60 M61 N62 l TOR BOR DI UG2 UG4 UG5 UG 6 I UG7 BF1 BF2 I SRC 30.8 - - - - 33.1 - - - 30.8 - - - - 33.0 - - - 30.8 - - - - 33.6 - - - 30.8 - - - - 33.3 - - - 30.8 - - - - 34.2 - - - 30.8 - - - - 33.6 - - - 30.8 - - - - 34.9 - - - 30.8 - - - - 35.0 - - - 30.8 - - - - 33.9 - - - 30.8 - - - - 35.1 - - - 30.8 - - - - 34.1 - - - 30.8 - - - - 35.2 - - - 30.8 - - - - 34.3 - - - 30.8 - - - - 35.3 - - - 30.8 - - - - 34.4 - - - 30.8 - - - - 35.5 - - - 30.8 - - - - 34.5 - - - 30.8 - - - - 35.6 - - - 30.8 - - - - 34.6 - - - 30.8 - - - - 35.7 - - - 30.8 - - - - 34.7 - - - 30.8 - - - - 35.9 - - - 30.8 - - - - 34.8 - - - 30.8 - - - - 36.1 - - - 30.8 - - - - 34.8 - - - 30.8 - - - - 36.2 - - - 30.8 - - - - 34.9 - - - 30.8 - - - - 36.4 - - - 30.8 - - - - 34.9 - - - 30.8 - - - - 36.6 - - - 30.8 - - - - 34.9 - - - 30.8 - - - - 36.8 - - - 30.8 - - - - 38.9 - - - 0.5 - - - - 55.9 - - - -3.0 - - - - 57.8 - - - -3.0 - - - - 58.4 - - - -3.0 - - - - 62.5 - - - -3.0 - - - T 63.1 - - - -3.0 - - - - 71.8 - - - -3.0 - - - - 72.6 - - - 3.0 - - - - 60.9 - - - 3.0 - - - - 68.9 - - - 0.0 SOURCE 73.5 1219.7 NODE TYPE PRESSURE DISCHARGE (PSI) (GPM) I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 11/13/2009NOLOGIES RACKS\CALCULATIONS\AREA A RACK D-CT FEED-REV.SDF JOB TITLE: Area "A" Racks I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 11/13/2009NOLO GIES RACKS\CALCULATIONS\AREA A RACK D-CT FEED-REV.SDF JOB TITLE: Area "A" Racks PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. I END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (PT) SUM. NODES (PT) (K) (PSI) (GPM) FL/FT (PSI) I Pipe: 1 107.2 2.157 PL 75.67 PP 7.6 R2 31.8 0.0 26.0 0.0 9.4 120 FTG T PE 0.0 51 31.8 8.0 18.4 34.3 0.087 TL 87.67 PV I Pipe: 2 72.9 2.157 PL 8.00 PF 0.3 - 51 31.8 8.0 18.4 34.3 6.4 120 FTG ---- PE 0.0 I S2 31.8 8.0 18.0 34.0 0.043 TL 8.00 PV Pipe: 3 39.0 2.157 PL 8.00 PP 0.1 S2 31.8 8.0 18.0 34.0 3.4 120 FTG ---- FE 0.0 I S3 31.8 8.0 17.9 33.9 0.013 TL 8.00 PV Pipe: 4 5.1 2.157 PL 8.00 PP 0.0 I S3 31.8 8.0 17.9 33.9 0.4 120 FTG ---- FE 0.0 S4 31.8 8.0 17.9 33.9 0.000 TL 8.00 PV Pipe: 5 -28.8 2.157 PL 8.00 PF 0.1 I S4 31.8 8.0 17.9 33.9 2.5 120 FTG ---- FE 0.0 S5 31.8 8.0 18.0 33.9 0.008 TL 8.00 PV Pipe: 6 -62.7 2.157 FL 8.00 PF 0.3 S5 31.8 8.0 18.0 33.9 5.5 120 FTG ---- FE 0.0 S6 31.8 8.0 18.2 34.2 0.032 TL 8.00 PV I Pipe: 7 -96.8 2.157 FL 8.00 PP 0.6 S6 31.8 8.0 18.2 34.2 8.5 120 FTG ---- FE 0.0 S7 31.8 8.0 18.8 34.7 0.072 TL 8.00 PV I Pipe: 8 -131.5 2.157 FL 8.00 FE' 1.0 S7 31.8 8.0 18.8 34.7 11.5 120 FTG ---- FE 0.0 ' S8 31.8 8.0 19.8 35.6 0.127 TL 8.00 PV Pipe: 9 -167.1 2.157 FL 3.83 PF 3.1 S8 31.8 8.0 19.8 35.6 14.7 120 FTG T PE 0.0 Ri 31.8 0.0 22.9 0.0 0.197 TL 15.83 PV Pipe: 10 107.2 2.157 FL 75.67 PP 7.6 I R4 31.8 0.0 26.0 0.0 9.4 120 FTG T PE 0.0 S9 31.8 8.0 18.4 34.3 0.087 TL 87.67 PV Pipe: 11 72.8 2.157 FL 8.00 FE' 0.3 I S9 31.8 8.0 18.4 34.3 6.4 120 FTG ---- FE 0.0 Slo 31.8 8.0 18.1 34.0 0.042 TL 8.00 PV Pipe: 12 38.8 2.157 FL 8.00 PP 0.1 S1O 31.8 8.0 18.1 34.0 3.4 120 FTG ---- FE 0.0 511 31.8 8.0 18.0 33.9 0.013 TL 8.00 PV I I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 11/13/2009NOLO GIES RACKS\CALCULATIONS\AREA A RACK D-CT FEED-REV.SDF JOE TITLE: Area "A" Racks I PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. I NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 13 4.9 2.157 PL 8.00 PF 0.0 Sil 31.8 8.0 18.0 33.9 0.4 120 FTG ---- FE 0.0 I S12 31.8 8.0 18.0 33.9 0.000 TL 8.00 PV Pipe: 14 -29.0 2.157 FL 8.00 PF 0.1 I S12 31.8 8.0 18.0 33.9 2.5 120 FTG ---- FE 0.0 S13 31.8 8.0 18.0 34.0 0.008 TL 8.00 PV Pipe: 15 -62.9 2.157 PL 8.00 PF 0.3 I 813 31.8 8.0 18.0 34.0 5.5 120 FTG ---- FE 0.0 S14 31.8 8.0 18.3 34.2 0.032 TL 8.00 PV Pipe: 16 -97.1 2.157 FL 8.00 PF 0.6 S14 31.8 8.0 18.3 34.2 8.5 120 FTG ---- PE 0.0 S15 31.8 8.0 18.9 34.7 0.072 TL 8.00 PV I Pipe: 17 -131.8 2.157 PL 8.00 PP 1.0 S15 31.8 8.0 18.9 34.7 11.6 120 FTG ---- FE 0.0 S16 31.8 8.0 19.9 35.7 0.127 TL 8.00 PV 1 Pipe: 18 -167.5 2.157 FL 3.83 PF 3.1 S16 31.8 8.0 19.9 35.7 14.7 120 FTG T PE 0.0 I R3 31.8 0.0 23.0 0.0 0.198 TL 15.83 PV Pipe: 19 107.0 2.157 PL 75.67 PF 7.6 R6 31.8 0.0 26.1 0.0 9.4 120 FTG T FE 0.0 I S17 31.8 8.0 18.5 34.4 0.086 TL 87.67 PV Pipe: 20 72.5 2.157 PL 8.00 PP 0.3 I S17 31.8 8.0 18.5 34.4 6.4 120 FTG ---- FE 0.0 S18 31.8 8.0 18.2 34.1 0.042 TL 8.00 PV Pipe: 21 38.4 2.157 FL 8.00 PF 0.1 I S18 31.8 8.0 18.2 34.1 3.4 120 FTG ---- FE 0.0 S19 31.8 8.0 18.1 34.0 0.013 TL 8.00 PV I Pipe: 22 4.4 2.157 PL 8.00 PF 0.0 I S19 31.8 8.0 18.1 34.0 0.4 120 FTG ---- FE 0.0 S20 31.8 8.0 18.1 34.0 0.000 TL 8.00 PV Pipe: 23 -29.6 2.157 FL 8.00 PF 0.1 - S20 31.8 8.0 18.1 34.0 2.6 120 FTG ---- FE 0.0 I S21 31.8 8.0 18.2 34.1 0.008 TL 8.00 pv Pipe: 24 -63.7 2.157 FL 8.00 PF 0.3 S21 31.8 8.0 18.2 34.1 5.6 120 FTG ---- PE 0.0 I S22 31.8 8.0 18.4 34.3 0.033 TL 8.00 PV Pipe: 25 -98.1 2.157 FL 8.00 PP 0.6 S22 31.8 8.0 18.4 34.3 8.6 120 FTG ---- FE 0.0 S23 31.8 8.0 19.0 34.9 0.074 TL 8.00 PV I SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: I SPRINKLER 11/13/2009NOLO GIES RACKS\CALCULATIONS\AREA A RACK D-CT FEED-REV.SDF JOB TITLE: Area "A" Racks 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) I 1.0 Pipe: 26 -133.0 2.157 PL 8.00 PF S23 31.8 8.0 19.0 34.9 11.7 120 FTG ---- PE 0.0 I S24 31.8 8.0 20.0 35.8 0.129 TL 8.00 PV Pipe: 27 -168.8 2.157 PL 3.83 PF 3.2 31.8 8.0 20.0 35.8 14.8 120 FTG T PE 0.0 I S24 R5 31.8 0.0 23.2 0.0 0.201 TL 15.83 PV Pipe: 28 46.8 2.157 PL 75.67 PP 1.6 31.8 0.0 27.2 0.0 4.1 120 FTG T PE 0.0 I R8 S25 31.8 8.0 25.6 40.5 0.019 TL 87.67 PV • Pipe: 29 6.4 2.157 PL 8.00 PF 0.0 S25 31.8 8.0 25.6 40.5 0.6 120 FTG ---- PE 0.0 S26 31.8 8.0 25.6 40.5 0.000 TL 8.00 PV I Pipe: 30 -34.1 2.157 PL 51.83 PF 0.7 - S26 31.8 8.0 25.6 40.5 3.0 120 FTG T PE 0.0 R7 31.8 0.0 26.3 0.0 0.010 TL 63.83 PV 1 Pipe: 31 20.8 2.157 PL 135.42 PP 0.7 RiO 31.8 0.0 27.7 0.0 1.8 120 FTG 2T PE 0.0 I R9 31.8 0.0 27.1 0.0 0.004 TL 159.42 PV Pipe: 32 -17.1 2.157 PL 135.42 PP 0.5 Rll 31.8 0.0 27.6 0.0 1.5 120 FTG 2T PE 0.0 R12 31.8 0.0 28.1 0.0 0.003 TL 159.42 PV Pipe: 33 -13.9 2.157 PL 135.42 PP 0.3 31.8 0.0 28.2 0.0 1.2 120 FTG 2T PE 0.0 I R13 R14 31.8 0.0 28.5 0.0 0.002 TL 159.42 PV Pipe: 34 -11.2 2.157 PL 135.42 PP 0.2 I R15 31.8 0.0 28.7 0.0 1.0 120 FTG 2T PE 0.0 R16 31.8 0.0 28.9 0.0 0.001 TL 159.42 PV I Pipe: 35 -9.0 2.157 PL 135.42 PP 0.1 R17 31.8 0.0 29.2 0.0 0.8 120 FTG 2T PE 0.0 R18 31.8 0.0 29.3 0.0 0.001 TL 159.42 PV I Pipe: 36 -7.5 2.157 PL 135.42 PP 0.1 R19 31.8 0.0 29.6 0.0 0.7 120 FTG 2T PE 0.0 R20 31.8 0.0 29.7 0.0 0.001 TL 159.42 PV I Pipe: 37 -6.8 2.157 PL 135.42 PF 0.1 R21 31.8 0.0 30.1 0.0 0.6 120 FTG 2T PE 0.0 I R22 31.8 0.0 30.2 0.0 0.001 TL 159.42 PV Pipe: 38 -7.0 2.157 PL 135.42 PP 0.1 R23 31.8 0.0 30.6 0.0 0.6 120 FTG 2T PE 0.0 I R24 31.8 0.0 30.6 0.0 0.001 TL 159.42 PV I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 11/13/2009NOLOGIES RACKS\CALCULATIONS\AREA A RACK D-CT FEED-REV.SDF JOB TITLE: Area FlAP! Racks I 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) I 0.1 Pipe: 39 -8.1 2.157 PL 135.42 PF R25 31.8 0.0 31.0 0.0 0.7 120 FTG 2T PE 0.0 R26 31.8 0.0 31.1 0.0 0.001 TL 159.42 PV Pipe: 40 -9.9 2.157 PL 135.42 PF 0.2 31.8 0.0 31.4 0.0 0.9 120 FTG 2T PE 0.0 l R27 R28 31.8 0.0 31.6 0.0 0.001 TL 159.42 PV Pipe: 41 -12.4 2.157 PL 135.42 PF 0.3 I R29 31.8 0.0 31.8 0.0 1.1 120 FTG 2T PE 0.0 R30 31.8 0.0 32.1 0.0 0.002 TL 159.42 PV 42 -15.3 2.157 PL 135.42 PF 0.4 I Pipe: R31 31.8 0.0 32.2 0.0 1.3 120 FTG 2T PE 0.0 R32 31.8 0.0 32.6 0.0 0.002 TL 159.42 PV I Pipe: 43 -18.8 2.157 FL 135.42 PP 0.6 R33 31.8 0.0 32.6 0.0 1.7 120 FTG 2T PE 0.0 R34 31.8 0.0 33.2 0.0 0.003 TL 159.42 PV I Pipe: 44 -22.7 2.157 FL 135.42 PP 0.8 R35 31.8 0.0 32.9 0.0 2.0 120 FTG 2T PE 0.0 I R36 31.8 0.0 33.7 0.0 0.005 TL 159.42 PV Pipe: 45 -27.2 2.157 PL 135.42 PP 1.1 R37 31.8 0.0 33.3 0.0 2.4 120 FTG 2T PE 0.0 I R38 31.8 0.0 34.4 0.0 0.007 TL 159.42 PV Pipe: 46 -26.8 2.157 PL 135.42 PP 1.1 31.8 0.0 33.5 0.0 2.4 120 FTG 2T PE 0.0 I R39 R40 31.8 0.0 34.6 0.0 0.007 TL 159.42 PV Pipe: 47 -25.5 2.157 PL 135.42 PF 1.0 R41 31.8 0.0 33.7 0.0 2.2 120 FTG 2T PE 0.0 R42 31.8 0.0 34.7 0.0 0.006 TL 159.42 PV I Pipe: 48 -24.7 2.157 PL 135.42 PF 0.9 R43 31.8 0.0 33.9 0.0 2.2 120 FTG 2T PE 0.0 R44 31.8 0.0 34.8 0.0 0.006 TL 159.42 PV I Pipe: 49 -24.4 2.157 FL 135.42 PP 0.9 R45 31.8 0.0 34.1 0.0 2.1 120 FTG 2T PE 0.0 R46 31.8 0.0 34.9 0.0 0.006 TL 159.42 PV I Pipe: 50 -24.5 2.157 FL 135.42 PP 0.9 R47 31.8 0.0 34.2 0.0 2.2 120 FTG 2T PE 0.0 I R48 31.8 0.0 35.1 0.0 0.006 TL 159.42 PV Pipe: 51 -25.0 2.157 PL 135.42 PP 0.9 R49 31.8 0.0 34.3 0.0 2.2 120 FTG 2T PE 0.0 I R50 31.8 0.0 35.2 0.0 0.006 TL 159.42 PV I SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: I SPRINKLER 11/13/2009NOLO GIES RACKS\CALCULATIONS\AREA A RACK D-CT FEED-REV.SDF JOB TITLE: Area VTA Racks 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) I Pipe: 52 -25.9 2.157 PL 135.42 PF 1.0 R51 31.8 0.0 34.4 0.0 2.3 120 FTG 2T PE 0.0 I R52 31.8 0.0 35.4 0.0 0.006 TL 159.42 PV Pipe: 53 -27.1 2.157 PL 135.42 PP 1.1 31.8 0.0 34.4 0.0 2.4 120 FTG 2T PE 0.0 I R53 R54 31.8 0.0 35.5 0.0 0.007 TL 159.42 PV Pipe: 54 -28.7 2.157 PL 135.42 PF 1.2 31.8 0.0 34.5 0.0 2.5 120 FTG 2T PE 0.0 I R55 R56 31.8 0.0 35.7 0.0 0.008 TL 159.42 PV 55 -30.4 2.157 PL 135.42 PP 1.3 I Pipe: R57 31.8 0.0 34.5 0.0 2.7 120 FTG 2T PE 0.0 R58 31.8 0.0 35.9 0.0 0.008 TL 159.42 PV I Pipe: 56 -32.3 2.157 PL 135.42 PP 1.5 R59 31.8 0.0 34.6 0.0 2.8 120 FTG 2T PS 0.0 R60 31.8 0.0 36.1 0.0 0.009 TL 159.42 PV I Pipe: 57 -34.4 2.157 PL 135.42 PF 1.7 R61 31.8 0.0 34.6 0.0 3.0 120 FTG 2T PE 0.0 I R62 31.8 0.0 36.3 0.0 0.011 TL 159.42 PV Pipe: 58 -167.1 2.157 PL 1.00 PF 2.6 Ri 31.8 0.0 22.9 0.0 14.7 120 FTG T PE 0.4 ' Ml 30.8 0.0 25.9 0.0 0.197 TL 13.00 PV Pipe: 59 -107.2 2.157 PL 1.00 PP 1.1 31.8 0.0 26.0 0.0 9.4 120 FTG T PE 0.4 I R2 N2 30.8 0.0 27.5 0.0 0.087 TL 13.00 PV Pipe: 60 -167.5 2.157 PL 1.00 PF 2.6 I R3 31.8 0.0 23.0 0.0 14.7 120 FTG T PS 0.4 M3 30.8 0.0 26.0 0.0 0.198 TL 13.00 PV I Pipe: 61 -107.2 2.157 PL 1.00 PP 1.1 • R4 31.8 0.0 26.0 0.0 9.4 120 FTG T PE 0.4 M4 30.8 0.0 27.6 0.0 0.087 TL 13.00 PV I Pipe: 62 -168.8 2.157 PL 1.00 PP 2.6 - R5 31.8 0.0 23.2 0.0 14.8 120 FTG T PE 0.4 M5 30.8 0.0 26.3 0.0 0.201 TL 13.00 PV I Pipe: 63 -107.0 2.157 PL 1.00 PP 1.1 R6 31.8 0.0 26.1 0.0 9.4 120 FTG T PE 0.4 I M6 30.8 0.0 27.7 0.0 0.086 TL 13.00 PV Pipe: 64 -34.1 2.157 PL 1.00 PP 0.1 R7 31.8 0.0 26.3 0.0 3.0 120 FTG T PE 0.4 I M7 30.8 0.0 26.8 0.0 0.010 TL 13.00 PV I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 I DATE: 11/13/2009NOLO GIES RACKS\CALCULATIONS\AREA A RACK D-CT FEED-REV.SDF JOB TITLE: Area "A" Racks I 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) I Pipe: 65 -46.8 2.157 PL 1.00 PF 0.2 R8 31.8 0.0 27.2 0.0 4.1 120 FTG T PE 0.4 I M8 30.8 0.0 27.9 0.0 0.019 TL 13.00 PV Pipe: 66 20.8 2.157 PL 1.00 PF 0.1 31.8 0.0 27.1 0.0 1.8 120 FTG T PE 0.4 I R9 M9 30.8 0.0 27.5 0.0 0.004 TL 13.00 PV Pipe: 67 -20.8 2.157 PL 1.00 PF 0.1 I RiO 31.8 0.0 27.7 0.0 1.8 120 FTG T PE 0.4 M10 30.8 0.0 28.2 0.0 0.004 TL 13.00 PV I Pipe: 68 17.1 2.157 PL 1.00 PF 0.0 Rib 31.8 0.0 27.6 0.0 1.5 120 FTG T PE 0.4 Mil 30.8 0.0 28.0 0.0 0.003 TL 13.00 PV I Pipe: 69 -17.1 2.157 PL 1.00 PF 0.0 R12 31.8 0.0 28.1 0.0 1.5 120 FTG T PE 0.4 M12 30.8 0.0 28.6 0.0 0.003 TL 13.00 PV I Pipe: 70 13.9 2.157 PL 1.00 PF 0.0 R13 31.8 0.0 28.2 0.0 1.2 120 FTG T PE 0.4 I M13 30.8 0.0 28.6 0.0 0.002 TL 13.00 PV Pipe: 71 -13.9 2.157 PL 1.00 PF 0.0 R14 31.8 0.0 28.5 0.0 1.2 120 FTG T PE 0.4 M14 30.8 0.0 28.9 0.0 0.002 TL 13.00 PV Pipe: 72 11.2 2.157 PL 1.00 PF 0.0 31.8 0.0 28.7 0.0 1.0 120 FTG T PE 0.4 i RiS MiS 30.8 0.0 29.1 0.0 0.001 TL 13.00 PV Pipe: 73 -11.2 2.157 PL 1.00 PF 0.0 I R16 31.8 0.0 28.9 0.0 1.0 120 FTG T PE 0.4 M16 30.8 0.0 29.3 0.0 0.001 TL 13.00 PV I Pipe: 74 9.0 2.157 PL 1.00 PF 0.0 • R17 31.8 0.0 29.2 0.0 0.8 120 FTG T PR 0.4 M17 30.8 0.0 29.6 0.0 0.001 TL 13.00 PV I Pipe: 75 -9.0 2.157 PL 1.00 PF 0.0 R18 31.8 0.0 29.3 0.0 0.8 120 FTG T PE 0.4 M18 30.8 0.0 29.8 0.0 0.001 TL 13.00 PV I 0.0 Pipe: 76 7.5 2.157 PL 1.00 PF R19 31.8 0.0 29.6 0.0 0.7 120 FTG T PR 0.4 I M19 30.8 0.0 30.1 0.0 0.001 TL 13.00 PV Pipe: 77 -7.5 2.157 PL 1.00 PF 0.0 R20 31.8 0.0 29.7 0.0 0.7 120 FTG T PR 0.4 I M20 30.8 0.0 30.2 0.0 0.001 TL 13.00 PV I SYSTEM HYDRAULIC ANALYSIS Page 12 DATE: I SPRINKLER 11/13/2009NOLO GIES RACKS\CALCULATIONS\AREA A RACK D-CT FEED-REV.SDF JOB TITLE: Area "A" Racks 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) I PF 0.0 Pipe: 78 6.8 2.157 FL 1.00 R21 31.8 0.0 30.1 0.0 0.6 120 FTG T PE 0.4 M21 30.8 0.0 30.5 0.0 0.001 TL 13.00 PV Pipe: 79 -6.8 2.157 PL 1.00 PF 0.0 31.8 0.0 30.2 0.0 0.6 120 FTG T PE 0.4 l R22 M22 30.8 0.0 30.6 0.0 0.001 TL 13.00 PV Pipe: 80 7.0 2.157 PL 1.00 PF 0.0 I R23 31.8 0.0 30.6 0.0 0.6 120 FTG T PE 0.4 M23 30.8 0.0 31.0 0.0 0.001 TL 13.00 PV • Pipe: 81 -7.0 2.157 PL 1.00 PF 0.0 • R24 31.8 0.0 30.6 0.0 0.6 120 FTG T PE 0.4 M24 30.8 0.0 31.1 0.0 0.001 TL 13.00 PV Pipe: 82 8.1 2.157 FL 1.00 PF 0.0 - R25 31.8 0.0 31.0 0.0 0.7 120 FTG T FE 0.4 M25 30.8 0.0 31.4 0.0 0.001 TL 13.00 PV I Pipe: 83 -8.1 2.157 PL 1.00 PF 0.0 R26 31.8 0.0 31.1 0.0 0.7 120 FTG T FE 0.4 I M26 30.8 0.0 31.6 0.0 0.001 TL 13.00 PV Pipe: 84 9.9 2.157 FL 1.00 PF 0.0 R27 31.8 0.0 31.4 0.0 0.9 120 FTG T FE 0.4 M27 30.8 0.0 31.8 0.0 0.001 TL 13.00 PV Pipe: 85 -9.9 2.157 FL 1.00 PF 0.0 31.8 0.0 31.6 0.0 0.9 120 FTG T FE 0.4 I R28 M28 30.8 0.0 32.0 0.0 0.001 TL 13.00 PV Pipe: 86 12.4 2.157 FL 1.00 PF 0.0 I R29 31.8 0.0 31.8 0.0 1.1 120 FTG T FE 0.4 M29 30.8 0.0 32.2 0.0 0.002 TL 13.00 PV I Pipe: 87 -12.4 2.157 FL 1.00 PF 0.0 • R30 31.8 0.0 32.1 0.0 1.1 120 FTG T PS 0.4 M30 30.8 0.0 32.5 0.0 0.002 TL 13.00 PV I Pipe: 88 15.3 2.157 FL 1.00 PF 0.0 R31 31.8 0.0 32.2 0.0 1.3 120 FTG T PE 0.4 M31 30.8 0.0 32.6 0.0 0.002 TL 13.00 PV I PF 0.0 Pipe: 89 -15.3 2.157 FL 1.00 R32 31.8 0.0 32.6 0.0 1.3 120 FTG T PE 0.4 I M32 30.8 0.0 33.1 0.0 0.002 TL 13.00 PV Pipe: 90 18.8 2.157 FL 1.00 PF 0.0 R33 31.8 0.0 32.6 0.0 1.7 120 FTG T FE 0.4 l M33 30.8 0.0 33.0 0.0 0.003 TL 13.00 PV I SYSTEM HYDRAULIC ANALYSIS Page 13 DATE: I SPRINKLER 11/13/2009NOLO GIES RACKS\CALCULATIONS\AREA A RACK D-CT FEED-REV.SDF JOB TITLE: Area "A" Racks 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) I 0.0 Pipe: 91 -18.8 2.157 FL 1.00 PP R34 31.8 0.0 33.2 0.0 1.7 120 FTG T PE 0.4 I M34 30.8 0.0 33.6 0.0 0.003 TL 13.00 PV Pipe: 92 22.7 2.157 PL 1.00 PP 0.1 31.8 0.0 32.9 0.0 2.0 120 FTG T PE 0.4 I R35 M35 30.8 0.0 33.3 0.0 0.005 TL 13.00 PV Pipe: 93 -22.7 2.157 FL 1.00 PF 0.1 I R36 31.8 0.0 33.7 0.0 2.0 120 FTG T FE 0.4 M36 30.8 0.0 34.2 0.0 0.005 TL 13.00 PV I Pipe: 94 27.2 2.157 PL 1.00 PP 0.1 • R37 31.8 0.0 33.3 0.0 2.4 120 FTG T FE 0.4 M37 30.8 0.0 33.6 0.0 0.007 TL 13.00 PV Pipe: 95 -27.2 2.157 FL 1.00 PP 0.1 - R38 31.8 0.0 34.4 0.0 2.4 120 FTG T PE 0.4 M38 30.8 0.0 34.9 0.0 0.007 TL 13.00 PV I Pipe: 96 26.8 2.157 PL 1.00 PF 0.1 R39 31.8 0.0 33.5 0.0 2.4 120 FTG T PE 0.4 I M39 30.8 0.0 33.9 0.0 0.007 TL 13.00 PV Pipe: 97 -26.8 2.157 PL 1.00 PF 0.1 R40 31.8 0.0 34.6 0.0 2.4 120 FTG T PE 0.4 M40 30.8 0.0 35.1 0.0 0.007 TL 13.00 PV Pipe: 98 25.5 2.157 PL 1.00 PP 0.1 R41 31.8 0.0 33.7 0.0 2.2 120 FTG T FE 0.4 I M41 30.8 0.0 34.1 0.0 0.006 TL 13.00 PV Pipe: 99 -25.5 2.157 PL 1.00 PF 0.1 U R42 31.8 0.0 34.7 0.0 2.2 120 FTG T PE 0.4 M42 30.8 0.0 35.2 0.0 0.006 TL 13.00 PV I Pipe: 100 24.7 2.157 FL 1.00 PP 0.1 U R43 31.8 0.0 33.9 0.0 2.2 120 FTG T PE 0.4 M43 30.8 0.0 34.3 0.0 0.006 TL 13.00 PV I Pipe: 101 -24.7 2.157 PL 1.00 PP 0.1 R44 31.8 0.0 34.8 0.0 2.2 120 FTG T PE 0.4 M44 30.8 0.0 35.3 0.0 0.006 TL 13.00 PV I Pipe: 102 24.4 2.157 FL 1.00 PP 0.1 R45 31.8 0.0 34.1 0.0 2.1 120 FTG T PE 0.4 I M45 30.8 0.0 34.4 0.0 0.006 TL 13.00 PV Pipe: 103 -24.4 2.157 PL 1.00 PP 0.1 R46 31.8 0.0 34.9 0.0 2.1 120 FTG T FE 0.4 I M46 30.8 0.0 35.5 0.0 0.006 TL 13.00 PV I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 14 DATE: 11/13/2009NOLOGIES RACKS\CALCULATIONS\AREA A RACK D-CT FEED-REV.SDF JOB TITLE: Area "A" Racks I PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(PPS) HW(C) (FT) SUM. NODES (PT) (K) (PSI) (GPM) FL/FT (PSI) I Pipe: 104 24.5 2.157 PL 1.00 PF 0.1 R47 31.8 0.0 34.2 0.0 2.2 120 FTG T PE 0.4 M47 30.8 0.0 34.5 0.0 0.006 TL 13.00 PV Pipe: 105 -24.5 2.157 PL 1.00 PP 0.1 31.8 0.0 35.1 0.0 2.2 120 FTG T PE 0.4 I R48 M48 30.8 0.0 35.6 0.0 0.006 TL 13.00 PV Pipe: 106 25.0 2.157 PL 1.00 PF 0.1 I R49 31.8 0.0 34.3 0.0 2.2 120 FTG T PE 0.4 M49 30.8 0.0 34.6 0.0 0.006 TL 13.00 PV I Pipe: 107 -25.0 2.157 PL 1.00 PP 0.1 • R50 31.8 0.0 35.2 0.0 2.2 120 FTG T PE 0.4 M50 30.8 0.0 35.7 0.0 0.006 TL 13.00 PV I Pipe: 108 25.9 2.157 PL 1.00 PF 0.1 - R51 31.8 0.0 34.4 0.0 2.3 120 FTG T PE 0.4 M51 30.8 0.0 34.7 0.0 0.006 TL 13.00 PV I 0.1 Pipe: 109 -25.9 2.157 PL 1.00 PP R52 31.8 0.0 35.4 0.0 2.3 120 FTG T PE 0.4 I M52 30.8 0.0 35.9 0.0 0.006 TL 13.00 PV Pipe: 110 27.1 2.157 PL 1.00 PP 0.1 R53 31.8 0.0 34.4 0.0 2.4 120 FTG T PE 0.4 M53 30.8 0.0 34.8 0.0 0.007 TL 13.00 PV Pipe: 111 -27.1 2.157 PL 1.00 PP 0.1 31.8 0.0 35.5 0.0 2.4 120 FTG T PE 0.4 I R54 M54 30.8 0.0 36.1 0.0 0.007 TL 13.00 PV Pipe: 112 28.7 2.157 PL 1.00 PP 0.1 U R55 31.8 0.0 34.5 0.0 2.5 120 FTG T PE 0.4 M55 30.8 0.0 34.8 0.0 0.008 TL 13.00 PV I Pipe: 113 -28.7 2.157 PL 1.00 PP 0.1 U R56 31.8 0.0 35.7 0.0 2.5 120 FTG T PE 0.4 M56 30.8 0.0 36.2 0.0 0.008 TL 13.00 PV I Pipe: 114 30.4 2.157 PL 1.00 PP 0.1 R57 31.8 0.0 34.5 0.0 2.7 120 FTG T PE 0.4 M57 30.8 0.0 34.9 0.0 0.008 TL 13.00 PV I 0.1 Pipe: 115 -30.4 2.157 PL 1.00 PP R58 31.8 0.0 35.9 0.0 2.7 120 FTG T FE 0.4 I M58 30.8 0.0 36.4 0.0 0.008 TL 13.00 PV Pipe: 116 32.3 2.157 PL 1.00 PP 0.1 R59 31.8 0.0 34.6 0.0 2.8 120 FTG T FE 0.4 I M59 30.8 0.0 34.9 0.0 0.009 TL 13.00 PV I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 15 DATE: 11/13/2009NOLOGIES RACKS\CALCULATIONS\AREA A RACK D-CT FEED-REV.SDF JOB TITLE: Area "AT' Racks 1 PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) H(C) (FT) SUM. I NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 117 -32.3 2.157 PL 1.00 PF 0.1 R60 31.8 0.0 36.1 0.0 2.8 120 FTG T PE 0.4 M60 30.8 0.0 36.6 0.0 0.009 TL 13.00 PV Pipe: 118 34.4 2.157 PL 1.00 PF 0.1 31.8 0.0 34.6 0.0 3.0 120 FTG T PE 0.4 I R61 M61 30.8 0.0 34.9 0.0 0.011 TL 13.00 PV Pipe: 119 -34.4 2.157 PL 1.00 PF 0.1 I R62 31.8 0.0 36.3 0.0 3.0 120 FTG T PE 0.4 M62 30.8 0.0 36.8 0.0 0.011 TL 13.00 PV I Pipe: 120 -167.1 4.260 PL 10.00 PF 0.1 Ml 30.8 0.0 25.9 0.0 3.8 120 FTG ---- PE 0.0 M3 30.8 0.0 26.0 0.0 0.007 TL 10.00 PV I Pipe: 121 -334.6 4.260 PL 10.00 PF 0.3 M3 30.8 0.0 26.0 0.0 7.5 120 FTG ---- PE 0.0 M5 30.8 0.0 26.3 0.0 0.026 TL 10.00 PV l Pipe: 122 -503.4 4.260 PL 10.00 PF 0.6 M5 30.8 0.0 26.3 0.0 11.3 120 FTG ---- PE 0.0 I M7 30.8 0.0 26.8 0.0 0.055 TL 10.00 PV Pipe: 123 -537.5 4.260 PL 10.00 PF 0.6 I M7 M9 30.8 30.8 0.0 0.0 26.8 27.5 0.0 0.0 12.1 120 0.062 FTG TL ---- 10.00 PE PV 0.0 Pipe: 124 -516.7 4.260 PL 10.00 PF 0.6 I M9 30.8 0.0 27.5 0.0 11.6 120 FTG ---- PE 0.0 Mil 30.8 0.0 28.0 0.0 0.058 TL 10.00 PV Pipe: 125 -499.6 4.260 PL 10.00 PF 0.5 I Mil 30.8 0.0 28.0 0.0 11.2 120 FTG ---- PE 0.0 M13 30.8 0.0 28.6 0.0 0.054 TL 10.00 PV I Pipe: 126 -485.7 4.260 PL 10.00 PF 0.5 M13 30.8 0.0 28.6 0.0 10.9 120 FTG ---- PE 0.0 M15 30.8 0.0 29.1 0.0 0.052 TL 10.00 PV I Pipe: 127 -474.6 4.260 PL 10.00 PF 0.5 MiS 30.8 0.0 29.1 0.0 10.7 120 FTG ---- PE 0.0 I M17 30.8 0.0 29.6 0.0 0.049 TL 10.00 PV Pipe: 128 -465.6 4.260 PL 10.00 PF 0.5 M17 30.8 0.0 29.6 0.0 10.5 120 FTG ---- PE 0.0 I M19 30.8 0.0 30.1 0.0 0.048 TL 10.00 PV Pipe: 129 -458.1 4.260 PL 10.00 PP 0.5 M19 30.8 0.0 30.1 0.0 10.3 120 FTG ---- PE 0.0 I I M21 30.8 0.0 30.5 0.0 0.046 TL 10.00 PV I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 16 DATE: 11/13/2009NOLOGIES RACKS\CALCULATIONS\AREA A RACK D-CT FEED-REV.SDF JOB TITLE: Area "AT' Racks I 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) I Pipe: 130 -451.3 4.260 PL 10.00 PP 0.5 M21 30.8 0.0 30.5 0.0 10.2 120 FTG ---- PE 0.0 M23 30.8 0.0 31.0 0.0 0.045 TL 10.00 PV Pipe: 131 -444.3 4.260 PL 10.00 PF 0.4 30.8 0.0 31.0 0.0 10.0 120 FTG ---- PE 0.0 I M23 M25 30.8 0.0 31.4 0.0 0.044 TL 10.00 PV Pipe: 132 -436.2 4.260 PL 10.00 PP 0.4 I M25 30.8 0.0 31.4 0.0 9.8 120 FTG ---- PE 0.0 M27 30.8 0.0 31.8 0.0 0.042 TL 10.00 PV 133 -426.2 4.260 PL 10.00 PP 0.4 I Pipe: M27 30.8 0.0 31.8 0.0 9.6 120 FTG ---- PE 0.0 M29 30.8 0.0 32.2 0.0 0.041 TL 10.00 PV I Pipe: 134 -413.8 4.260 PL 10.00 PP 0.4 M29 30.8 0.0 32.2 0.0 9.3 120 FTG ---- FE 0.0 M31 30.8 0.0 32.6 0.0 0.038 TL 10.00 PV I Pipe: 135 -398.5 4.260 PL 10.00 PP 0.4 M31 30.8 0.0 32.6 0.0 9.0 120 FTG ---- PE 0.0 I M33 30.8 0.0 33.0 0.0 0.036 TL 10.00 PV Pipe: 136 -379.7 4.260 PL 10.00 PP 0.3 M33 30.8 0.0 33.0 0.0 8.5 120 FTG ---- PE 0.0 M35 30.8 0.0 33.3 0.0 0.033 TL 10.00 PV Pipe: 137 -357.0 4.260 PL 10.00 PF 0.3 30.8 0.0 33.3 0.0 8.0 120 FTG ---- PE 0.0 I M35 M37 30.8 0.0 33.6 0.0 0.029 TL 10.00 PV Pipe: 138 -329.8 4.260 PL 10.00 PP 0.3 I M37 30.8 0.0 33.6 0.0 7.4 120 FTG ---- PE 0.0 M39 30.8 0.0 33.9 0.0 0.025 TL 10.00 PV I Pipe: 139 -303.0 4.260 PL 10.00 PP 0.2 M39 30.8 0.0 33.9 0.0 6.8 120 FTG ---- PE 0.0 M41 30.8 0.0 34.1 0.0 0.022 TL 10.00 PV I Pipe: 140 -277.5 4.260 PL 10.00 PF 0.2 M41 30.8 0.0 34.1 0.0 6.2 120 FTG ---- PE 0.0 M43 30.8 0.0 34.3 0.0 0.018 TL 10.00 PV I 0.2 Pipe: 141 -252.8 4.260 PL 10.00 PP M43 30.8 0.0 34.3 0.0 5.7 120 FTG ---- FE 0.0 I M45 30.8 0.0 34.4 0.0 0.015 TL 10.00 PV Pipe: 142 -228.4 4.260 PL 10.00 PP 0.1 M45 30.8 0.0 34.4 0.0 5.1 120 FTG ---- PE 0.0 I M47 30.8 0.0 34.5 0.0 0.013 TL 10.00 PV I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 17 DATE: 11/13/2009NOLO GIES RACKS\CALCULATIONS\AREA A RACK D-CT FEED-REV.SDF JOB TITLE: Area "A" Racks I 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) I Pipe: 143 -203.9 4.260 PL 10.00 PF 0.1 M47 30.8 0.0 34.5 0.0 4.6 120 FTG ---- PS 0.0 M49 30.8 0.0 34.6 0.0 0.010 TL 10.00 PV Pipe: 144 -178.9 4.260 PL 10.00 PF 0.1 30.8 0.0 34.6 0.0 4.0 120 FTG ---- PE 0.0 I M49 M51 30.8 0.0 34.7 0.0 0.008 TL 10.00 PV Pipe: 145 -153.0 4.260 PL 10.00 PF 0.1 I M51 30.8 0.0 34.7 0.0 3.4 120 FTG ---- PE 0.0 M53 30.8 0.0 34.8 0.0 0.006 TL 10.00 PV 146 -125.8 4.260 PL 10.00 PF 0.0 I Pipe: M53 30.8 0.0 34.8 0.0 2.8 120 FTG ---- PE 0.0 M55 30.8 0.0 34.8 0.0 0.004 TL 10.00 PV I Pipe: 147 -97.2 4.260 PL 10.00 PF 0.0 M55 30.8 0.0 34.8 0.0 2.2 120 FTG ---- PS 0.0 M57 30.8 0.0 34.9 0.0 0.003 TL 10.00 PV I Pipe 148 -66.8 4.260 PL 10.00 PF 0.0 M57 30.8 0.0 34.9 0.0 1.5 120 FTG ---- PE 0.0 I M59 30.8 0.0 34.9 0.0 0.001 TL 10.00 PV Pipe: 149 -34.4 4.260 PL 10.00 PF 0.0 M59 30.8 0.0 34.9 0.0 0.8 120 FTG ---- PS 0.0 I M61 30.8 0.0 34.9 0.0 0.000 TL 10.00 PV Pipe: 150 -107.2 4.260 PL 10.00 PF 0.0 30.8 0.0 27.5 0.0 2.4 120 FTG ---- PE 0.0 U M2 M4 30.8 0.0 27.6 0.0 0.003 TL 10.00 PV Pipe: 151 -214.3 4.260 PL 10.00 PE 0.1 I M4 30.8 0.0 27.6 0.0 4.8 120 FTG ---- PE 0.0 M6 30.8 0.0 27.7 0.0 0.011 TL 10.00 PV I Pipe: 152 -321.3 4.260 PL 10.00 PF 0.2 M6 30.8 0.0 27.7 0.0 7.2 120 FTG ---- PE 0.0 M8 30.8 0.0 27.9 0.0 0.024 TL 10.00 PV I Pipe: 153 -368.2 4.260 PL 10.00 PF 0.3 M8 30.8 0.0 27.9 0.0 8.3 120 FTG ---- PE 0.0 M10 30.8 0.0 28.2 0.0 0.031 TL 10.00 PV I Pipe: 154 -389.0 4.260 PL 10.00 PF 0.3 M10 30.8 0.0 28.2 0.0 8.8 120 FTG ---- PS 0.0 M12 30.8 0.0 28.6 0.0 0.034 TL 10.00 PV Pipe: 155 -406.1 4.260 PL 10.00 PF 0.4 M12 30.8 0.0 28.6 0.0 9.1 120 FTG ---- PE 0.0 I M14 30.8 0.0 28.9 0.0 0.037 TL 10.00 PV I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 18 DATE: 11/13/2009NOLO GIES RACKS\CALCULATIONS\AREA A RACK D-CT FEED-REV.SDF JOB TITLE: Area 'TA" Racks 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) I Pipe: 156 -420.0 4.260 PL 10.00 PF 0.4 M14 30.8 0.0 28.9 0.0 9.5 120 FTG ---- FE 0.0 M16 30.8 0.0 29.3 0.0 0.039 TL 10.00 PV Pipe: 157 -431.1 4.260 PL 10.00 PF 0.4 30.8 0.0 29.3 0.0 9.7 120 FTG ---- FE 0.0 I M16 M18 30.8 0.0 29.8 0.0 0.041 TL 10.00 PV Pipe: 158 -440.1 4.260 PL 10.00 PF 0.4 I M18 30.8 0.0 29.8 0.0 9.9 120 FTG ---- PE 0.0 M20 30.8 0.0 30.2 0.0 0.043 TL 10.00 PV 159 -447.6 4.260 PL 10.00 PF 0.4 I Pipe: M20 30.8 0.0 30.2 0.0 10.1 120 FTG ---- FE 0.0 M22 30.8 0.0 30.6 0.0 0.044 TL 10.00 PV I Pipe: 160 -454.4 4.260 PL 10.00 PF 0.5 M22 30.8 0.0 30.6 0.0 10.2 120 FTG ---- FE 0.0 M24 30.8 0.0 31.1 0.0 0.046 TL 10.00 FV I Pipe: 161 -461.4 4.260 FL 10.00 PF 0.5 M24 30.8 0.0 31.1 0.0 10.4 120 FTG ---- FE 0.0 I M26 30.8 0.0 31.6 0.0 0.047 TL 10.00 PV Pipe: 162 -469.6 4.260 FL 10.00 PF 0.5 M26 30.8 0.0 31.6 0.0 10.6 120 FTG ---- FE 0.0 I M28 30.8 0.0 32.0 0.0 0.049 TL 10.00 PV Pipe: 163 -479.5 4.260 FL 10.00 PF 0.5 30.8 0.0 32.0 0.0 10.8 120 FTG ---- PE 0.0 I M28 M30 30.8 0.0 32.5 0.0 0.050 TL 10.00 PV Pipe: 164 -491.9 4.260 FL 10.00 PF 0.5 I M30 30.8 0.0 32.5 0.0 11.1 120 FTG ---- FE 0.0 M32 30.8 0.0 33.1 0.0 0.053 TL 10.00 PV I Pipe: 165 -507.2 4.260 FL 10.00 PF 0.6 M32 30.8 0.0 33.1 0.0 11.4 120 FTG ---- FE 0.0 M34 30.8 0.0 33.6 0.0 0.056 TL 10.00 PV I Pipe: 166 -526.0 4.260 FL 10.00 PF 0.6 M34 30.8 0.0 33.6 0.0 11.8 120 FTG ---- FE 0.0 M36 30.8 0.0 34.2 0.0 0.060 TL 10.00 FV I Pipe: 167 -548.7 4.260 FL 10.00 PF 0.6 M36 30.8 0.0 34.2 0.0 12.4 120 FTG ---- FE 0.0 I M38 30.8 0.0 34.9 0.0 0.065 TL 10.00 PV Pipe: 168 -575.9 4.260 PL 2.00 PF 0.1 M38 30.8 0.0 34.9 0.0 13.0 120 FTG ---- FE 0.0 I M38A 30.8 0.0 35.0 0.0 0.071 TL 2.00 PV I SYSTEM HYDRAULIC ANALYSIS Page 19 DATE: I SPRINKLER 11/13/2009NOLO GIES RACKS \CALCULAT IONS \AREA A RACK D-CT FEED-REV.SDF JOB TITLE: Area "A" Racks 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) I 0.1 Pipe: 169 -575.9 6.357 PL 8.00 PF M38A 30.8 0.0 35.0 0.0 5.8 120 FTG ---- PE 0.0 M40 30.8 0.0 35.1 0.0 0.010 TL 8.00 PV Pipe: 170 -602.7 6.357 PL 10.00 PF 0.1 30.8 0.0 35.1 0.0 6.1 120 FTG ---- PE 0.0 I M40 M42 30.8 0.0 35.2 0.0 0.011 TL 10.00 PV Pipe: 171 -628.2 6.357 PL 10.00 PF 0.1 I M42 30.8 0.0 35.2 0.0 6.4 120 FTG ---- PE 0.0 M44 30.8 0.0 35.3 0.0 0.012 TL 10.00 PV 172 -652.9 6.357 PL 10.00 PF 0.1 I Pipe: M44 30.8 0.0 35.3 0.0 6.6 120 FTG ---- PE 0.0 M46 30.8 0.0 35.5 0.0 0.013 TL 10.00 PV I Pipe: 173 -677.3 6.357 PL 10.00 PF 0.1 M46 30.8 0.0 35.5 0.0 6.8 120 FTG ---- PE 0.0 M48 30.8 0.0 35.6 0.0 0.014 TL 10.00 PV I Pipe: 174 -701.8 6.357 PL 10.00 PF 0.1 M48 30.8 0.0 35.6 0.0 7.1 120 FTG ---- PE 0.0 I M50 30.8 0.0 35.7 0.0 0.015 TL 10.00 PV Pipe: 175 -726.8 6.357 PL 10.00 PF 0.2 M50 30.8 0.0 35.7 0.0 7.3 120 FTG ---- PE 0.0 M52 30.8 0.0 35.9 0.0 0.016 TL 10.00 PV Pipe: 176 -752.7 6.357 PL 10.00 PF 0.2 30.8 0.0 35.9 0.0 7.6 120 FTG ---- PE 0.0 I M52 M54 30.8 0.0 36.1 0.0 0.017 TL 10.00 PV Pipe: 177 -779.9 6.357 PL 10.00 PF 0.2 M54 30.8 0.0 36.1 0.0 7.9 120 FTG ---- PE 0.0 M56 30.8 0.0 36.2 0.0 0.018 TL 10.00 PV I Pipe: 178 -808.5 6.357 PL 10.00 PF 0.2 M56 30.8 0.0 36.2 0.0 8.2 120 FTG ---- PE 0.0 M58 30.8 0.0 36.4 0.0 0.019 TL 10.00 PV I Pipe: 179 -839.0 6.357 PL 10.00 PF 0.2 M58 30.8 0.0 36.4 0.0 8.5 120 FTG ---- PE 0.0 M60 30.8 0.0 36.6 0.0 0.020 TL 10.00 PV I Pipe: 180 -871.3 6.357 PL 10.00 PF 0.2 M60 30.8 0.0 36.6 0.0 8.8 120 FTG ---- PE 0.0 M62 30.8 0.0 36.8 0.0 0.022 TL 10.00 PV Pipe: 181 -905.7 6.357 PL 15.00 PF 2.1 M62 30.8 0.0 36.8 0.0 9.2 120 FTG 2ET PE 0.0 I TOR 30.8 0.0 38.9 0.0 0.023 TL 89.00 PV I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 20 DATE: 11/13/2009NOLOGIES RACKS\CALCULATIONS\AREA A RACK D-CT FEED-REV.SDF JOB TITLE: Area "A" Racks I PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. I NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 182 -905.7 6.357 PL 27.75 PF 2.3 TOR 30.8 0.0 38.9 0.0 9.2 120 FTG ETB PE 12.0 I x6 3.0 0.0 53.2 0.0 0.023 TL 96.75 PV Pipe: 183 -23.0 1.728 PL 6.00 PF 0.1 I i9.2 5.6 16.9 23.0 3.1 120 FTG ---- PE 0.0 2 9.2 5.6 17.0 23.1 0.015 TL 6.00 PV Pipe: 184 -46.1 1.728 PL 6.83 PF 0.4 I 2 9.2 5.6 17.0 23.1 6.3 120 FTG ---- PE 0.0 3 9.2 5.6 17.3 23.3 0.054 TL 6.83 PV I Pipe: 185 -69.4 1.728 PL 9.17 PF 1.0 I 3 9.2 5.6 17.3 23.3 9.5 120 FTG ---- PE 0.0 4 9.2 5.6 18.4 24.0 0.114 TL 9.17 PV I Pipe: 186 -93.4 1.728 PL 6.83 PF 1.4 - 4 9.2 5.6 18.4 24.0 12.8 120 FTG ---- PE 0.0 I 9.2 5.6 19.8 24.9 0.198 TL 6.83 PV Pipe: 187 -118.3 1.728 PL 9.75 PF 6.5 5 9.2 5.6 19.8 24.9 16.2 120 FTG 2E PE 2.2 I 6 4.2 5.6 28.4 29.8 0.307 TL 21.04 PV Pipe: 188 -148.2 1.728 PL 8.25 PF 9.1 6 4.2 5.6 28.4 29.8 20.3 120 FTG T PE 0.0 I xi 4.2 0.0 37.5 0.0 0.465 TL 19.54 PV Pipe: 189 -21.7 1.728 PL 10.00 PF 0.1 I 7 18.2 5.6 15.0 21.7 3.0 120 FTG ---- PE 0.0 I 8 18.2 5.6 15.1 21.8 0.013 TL 10.00 PV Pipe: 190 -43.5 1.728 PL 6.00 PF 0.3 8 18.2 5.6 15.1 21.8 5.9 120 FTG ---- PE 0.0 9 18.2 5.6 15.4 22.0 0.048 TL 6.00 PV I Pipe: 191 -65.5 1.728 PL 6.00 PF 0.6 9 18.2 5.6 15.4 22.0 9.0 120 FTG ---- PE 0.0 10 18.2 5.6 16.0 22.4 0.103 TL 6.00 PV I Pipe: 192 -87.9 1.728 PL 7.92 PF 1.4 10 18.2 5.6 16.0 22.4 12.0 120 FTG ---- PE 0.0 I ii 18.2 5.6 17.4 23.4 0.177 TL 7.92 PV Pipe: 192A -111.3 1.728 PL 6.50 PF 4.9 11 18.2 5.6 17.4 23.4 15.2 120 FTG 2E PE 0.0 12 18.2 5.6 22.3 26.5 0.274 TL 17.79 PV Pipe: 192B -137.7 1.728 PL 7.00 PF 2.8 I 12 18.2 5.6 22.3 26.5 18.8 120 FTG ---- PE 0.0 13 18.2 5.6 25.2 28.1 0.406 TL 7.00 PV I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 21 DATE: 11/13/2009NOLOGIES RACKS\CALCULATIONS\AREA A RACK D-CT FEEDREV.SDF JOB TITLE: Area "A" Racks PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. I NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 193 -165.8 1.728 PL 1.00 PF 7.0 13 18.2 5.6 25.2 28.1 22.7 120 FTG T PE 0.0 X2 18.2 0.0 32.2 0.0 0.573 TL 12.29 PV Pipe: 194 -148.2 3.314 PL 9.00 PF 0.8 4.2 0.0 37.5 0.0 5.5 120 FTG ET BE -6.1 I X1 X2 18.2 0.0 32.2 0.0 0.020 TL 41.03 PV Pipe: 195 -314.0 3.314 PL 22.42 PP 4.3 I X2 18.2 0.0 32.2 0.0 11.7 120 FTG ET BE -5.1 X3 30.0 0.0 31.4 0.0 0.078 TL 54.45 PV 196 -314.0 4.431 PL 111.25 PF 3.3 I Pipe: X3 30.0 0.0 31.4 0.0 6.5 120 FTG 4E PE 0.0 X4 30.0 0.0 34.7 0.0 0.019 TL 175.05 PV I Pipe: 197 -314.0 4.431 PL 244.92 PP 6.5 X4 30.0 0.0 34.7 0.0 6.5 120 FTG 6E PE 0.0 X5 30.0 0.0 41.2 0.0 0.019 TL 340.61 PV I Pipe: 198 -314.0 6.395 PL 27.00 PF 0.3 X5 30.0 0.0 41.2 0.0 3.1 120 FTG ETB PE 11.7 I X6 3.0 0.0 53.2 0.0 0.003 TL 96.90 PV Pipe: 199 -1219.7 6.395 PL 4.50 PF 1.6 X6 3.0 0.0 53.2 0.0 12.2 120 FTG 2E PE 1.1 I BOR 0.5 0.0 55.9 0.0 0.039 TL 40.74 PV Pipe: 200 -1219.7 7.980 PL 10.00 PP 0.4 BOR 0.5 0.0 55.9 0.0 7.8 150 FTG 2L PE 1.5 I DI -3.0 0.0 57.8 0.0 0.009 TL 50.00 PV • Pipe: 201 -1219.7 7.980 PL 40.00 PP 0.6 DI -3.0 0.0 57.8 0.0 7.8 150 FTG E PE 0.0 UG2 -3.0 0.0 58.4 0.0 0.009 TL 67.00 By I Pipe: 202 -1219.7 7.980 PL 407.17 PP 4.1 UG2 -3.0 0.0 58.4 0.0 7.8 150 FTG T PE 0.0 UG4 -3.0 0.0 62.5 0.0 0.009 TL 460.17 By I Pipe: 203 -1219.7 7.980 PL 25.50 PF 0.6 UG4 -3.0 0.0 62.5 0.0 7.8 150 FTG 2L PE 0.0 UGS -3.0 0.0 63.1 0.0 0.009 TL 65.50 By I Pipe: 204 -1219.7 8.390 PL 6.00 PP 0.4 UGS -3.0 0.0 63.1 0.0 7.1 140 FTG 2L PE -2.6 BF'l 3.0 0.0 60.9 0.0 0.008 TL 50.00 PV Pipe: 205 FIXED PRESSURE LOSS DEVICE • BF2 3.0 0.0 68.9 0.0 8.0 psi, 1219.7 gpm • BF1 3.0 0.0 60.9 0.0 I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 22 DATE: 11/13/2009NOLOGIES RACKS\CALCULATIONS\AREA A RACK D-CT FEED-REV.SDF JOB TITLE: Area "A" Racks I PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. I NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 206 -1219.7 8.390 PL 6.00 PF 0.4 BF2 3.0 0.0 68.9 0.0 7.1 140 FTG 2L PE 2.6 UG6 -3.0 0.0 71.8 0.0 0.008 TL 50.00 PV Pipe: 207 -1219.7 7.980 PL 16.83 PF 0.8 I UG6 -3.0 0.0 71.8 0.0 7.8 150 FTG TL PE 0.0 UG7 -3.0 0.0 72.6 0.0 0.009 TL 89.83 PV Pipe: 208 -1219.7 7.980 PL 126.00 PF 2.1 I UG7 -3.0 0.0 72.6 0.0 7.8 150 FTG 2ETG PE -1.3 SRC 0.0 SRCE 73.5 (N/A) 0.009 TL 239.00 PV NOTES (HASS) I (1) Calculations were performed by the HASS 8.0 computer program under license no. 50040828 granted by HRS Systems, Inc. 208 South Public Square Petersburg, TN 37144 The system has been calculated to provide an average I imbalance at each node of 0.001 gpm and a maximum imbalance at any node of 0.196 gpm. Total pressure at each node is used in balancing the system. I Maximum water velocity is 22.7 ft/sec at pipe 193. (4) a. System remote area HAS been proven or 'peaked' I b. Minimum pressure at any sprinkler: 16.894 psi I c. Minimum pressure with remote area shifted one sprinkler space toward left cross main: 16.925 psi d. Remote area is located adjacent to right cross main I (S) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP I I I I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 23 DATE: 11/13/2009NOLOGIES RACKS\CALCULATIONS\AREA A RACK D-CT FEED-REV.SDF JOB TITLE: Area "A" Racks PAGE: * MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N I Eli Tee LngEil ChkViv BfyVlv GatVlv AimChk DPViv NPTee 1.728 5.64 11.29 2.82 12.70 8.47 1.41 14.11 14.11 11.29 3.314 10.19 21.84 7.28 23.29 14.56 1.46 18.93 18.93 21.84 I 4.431 15.95 31.90 9.57 35.09 19.14 3.19 31.90 31.90 31.90 6.395 18.12 38.83 11.65 41.42 12.94 3.88 36.24 36.24 38.83 B MATERIAL: THNWL HWC: 120 I PAGE: Diameter Equivalent Fitting Lengths in Feet (in) B T L C B G A D N Eli Tee LngEii ChkViv BfyViv GatVlv AlmChk DPViv NPTee I 2.157 6.00 12.00 3.00 14.00 8.00 1.00 12.00 12.00 12.00 4.260 13.00 26.00 8.00 29.00 16.00 3.00 26.00 26.00 26.00 6.357 18.00 38.00 11.00 40.00 13.00 4.00 35.00 35.00 38.00 PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N I Eli Tee LngEfl ChkViv BfyViv GatVlv NPTee 8.390 31.00 59.00 22.00 76.00 20.00 7.00 59.00 I PAGE: E MATERIAL: PVC150 HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Eli Tee LngEii ChkVlv BfyViv GatVlv NPTee I 7.980 27.00 53.00 20.00 68.00 18.00 6.00 53.00 I DATE: 1 JOB TIT: I I B a 0 0 LO H 0 0 H 0 cj 0 0 0 0 0 I- 0 0 0 0 0 0 0 H O 0 0 0 0 0 0 0 U) C'I CD U 41 -i4:11U)U)F11 U SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 25 DATE: 11/13/2009NOLO GIES RACKS\CALCULATIONS\AREA A RACK D-CT FEEDREV.SDF JOB TITLE: Area "A" Racks WATER SUPPLY CURVE 120+ I 110+ \\\\\ I \\\\\ \\\\\ I I * <-102.6 psi @ 1060 gpm 100+ Flow Test Point 90+ 0 I P 80+ I RI E I S I x S 70+ I UI R I E I I 60+ P I S I I I 50+ ) I 40+ 30+ I = = = = = = = = = = = = = = = = = = = = = = = = = = = = = = 20+ LEGEND I I 11 I X = Required Water Supply it I 73.45 psi @ 1719.7 gpm if 10+ if I I 0 = Available Water Supply 89.57 psi @ 1719.7 gpm FT I o --------+-----+ ------+ --------+ --------+ ---------+ -----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) I I WESTERN FIRE PROTECTION, INC. REMOTE AREA #2 13630 DANIELSON STREET POWAY,CA 92064 HYDRAULIC CALCULATIONS FOR LIFE TECHNOLOGIES 5781 VAN ALLEN WAY CARLSBAD, CA 92008 'FILE NUMBER: C-2625 DATE: OCT 13, 2009 -DESIGN DATA- OCCUPANCY CLASSIFICATION: GROUP A PLASTICS CARTONED DENSITY: 0.30 GPM PER SQ.FT. AREA OF APPLICATION: 2000 SQ.FT. 8 ROOF + 11 IN-RACK COVERAGE PER SPRINKLER: 80 SQ.FT. MAX NUMBER OF SPRINKLERS CALCULATED: 26 AT ROOF, 11 IN-RACKS ROOF SPRINKLER DEMAND: (8 NODE G) 965.0 GPM 8 61.4 PSI IN-RACK DEMAND: (@ NODE G) : 234.1 GPM 8 61.4 PSI FLOW AND PRESSURE (8 BOR) : 1199.1 GPM 8 64.1 PSI TOTAL WATER REQUIRED (including hose) : 1699.0 GPM SPRINKLER K FACTOR: K=8.0 AT ROOF, K=5.6 IN-RACKS DESIGN/LAYOUT BY: G.RUIZ AUTHORITY HAVING JURISDICTION: CARLSBAD FIRE DEPARTMENT CONTRACTOR CERTIFICATION NUMBER: CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE # 50040828 HRS SYSTEMS, INC. TUCKER, GA 30084 TUCKER, GA 30084 I I I I I I I I I I I I I I I I I I I DATE: I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 9/4/2009SENT\C -2625 LIFE TECHNOLOGIES RACKS\CALCULATIONS\AREA B.SDF JOB TITLE: Area B WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ!D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. I TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SRC 111.6 102.6 1060.0 90.1 1699.0 83.4 AGGREGATE FLOW ANALYSIS: I TOTAL FLOW AT SOURCE 1699.0 GPM HOSE STREAM ALLOWANCE AT SOURCE 500.0 GPM U TOTAL OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 1199.0 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE I (FT) (PSI) (GPM) 51 31.8 K= 8.00 21.2 36.9 S2 31.8 K= 8.00 20.8 36.5 S3 31.8 K= 8.00 20.4 36.1 S4 31.8 K= 8.00 20.3 36.1 S5 31.8 K= 8.00 20.4 36.1 • S6 31.8 K= 8.00 20.6 36.3 • S7 31.8 K= 8.00 21.2 36.8 SB 31.8 K= 8.00 22.2 37.7 • S9 31.8 K= 8.00 21.1 36.8 S1O 31.8 K= 8.00 20.6 36.3 Sli 31.8 K= 8.00 20.5 36.2 S12 31.8 K= 8.00 20.5 36.2 I S13 31.8 K= 8.00 20.5 36.2 S14 31.8 K= 8.00 20.7 36.4 S15 31.8 K= 8.00 21.3 36.9 S16 31.8 K= 8.00 22.3 37.8 I S17 31.8 K= 8.00 21.2 36.9 S18 31.8 K= 8.00 20.8 36.5 S19 31.8 K= 8.00 20.6 36.3 I S20 31.8 K= 8.00 20.6 36.3 S21 31.8 K= 8.00 20.6 36.3 S22 31.8 K= 8.00 20.9 36.5 I s23 31.8 K= 8.00 21.4 37.0 S24 31.8 K= 8.00 22.5 37.9 S25 31.8 K= 8.00 28.8 42.9 S26 31.8 K= 8.00 28.8 42.9 I 1 8.8 K= 5.60 17.7 23.5 2 8.8 K= 5.60 17.7 23.6 3 8.8 K= 5.60 18.3 24.0 I 8.8 K= 5.60 19.5 24.7 5 8.8 K= 5.60 21.6 26.0 6 16.5 K= 5.60 15.0 21.7 16.5 K= 5.60 15.1 21.8 I 8 16.5 K= 5.60 15.6 22.1 I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 9/4/2009SENT\C -2625 LIFE TECHNOLOGIES RACKS\CALCULATIONS\AREA E.SDF JOB TITLE: Area .B I NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 9 16.5 K= 5.60 16.5 22.8 10 16.5 K= 5.60 18.3 24.0 1 A I 1 16.5 - - - - 8.8 - - - - 19.7 26.2 - - - - - - B 16.5 - - - - 23.0 - - - C 30.0 - - - - 19.3 - - - D 30.0 - - - - 20.7 - - - E 30.0 - - - - 26.5 - - - F 30.0 - - - - 48.1 - - - G 3.0 - - - - 61.4 - - - Ri 31.8 - - - - 25.5 - - - R2 31.8 - - - - 31.0 - - - R3 31.8 - - - - 25.6 - - - I R4 31.8 - - - - 31.0 - - - R5 31.8 - - - - 25.8 - - - R6 31.8 - - - - 31.0 - - - 31.8 - - - - 29.0 - - - I R7 R8 31.8 - - - - 32.0 - - - R9 31.8 - - - - 29.7 - - - I RiO Rll 31.8 - - - - 31.8 - - - - 32.5 30.4 - - - - - - R12 31.8 - - - - 32.4 - - - R13 31.8 - - - - 30.9 - - - I R14 31.8 - - - - 32.5 - - - R15 31.8 - - - - 31.4 - - - R16 31.8 - - - - 32.6 - - - 31.8 - - - - 31.8 - - - I R17 R18 31.8 - - - - 32.7 - - - R19 31.8 - - - - 32.1 - - - R20 31.8 - - - - 32.9 - - - I R21 31.8 - - - - 32.4 - - R22 31.8 - - - - 33.0 - - - R23 31.8 - - - 32.7 - - - R24 31.8 - - - - 33.1 - - - I R25 31.8 - - - - 33.0 - - - R26 31.8 - - - - 33.2 - - - I R27 R28 31.8 - - - - 31.8 - - - - 33.3 33.4 - - - - - - R29 31.8 -. - - 33.5 - - - R30 31.8 - - - - 33.5 - - - I R31 31.8 - - - - 33.7 - - - R32 31.8 - - - - 33.6 - - - R33 31.8 - - - - 34.0 - - - R34 31.8 - - - - 33.7 - - - R35 I 31.8 - - - - 34.3 - - - R36 31.8 - - - - 33.9 - - - R37 31.8 - - - - 34.6 - - - I R38 31.8 - - - - 34.0 - - - R39 31.8 - - - - 34.9 - - - R40 31.8 - - - - 34.1 - - - R41 31.8 - - - - 35.3 - - - I R42 31.8 - - - - 34.2 - - - I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 9/4/2009SENT\C -2625 LIFE TECHNOLOGIES RACKS\CALCULATIONS\AREA B.SDF JOB TITLE: Area B I NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) R43 31.8 - - - - 35.7 - - - R44 31.8 - - - - 34.3 - - - R45 31.8 - - - - 36.1 - - - R46 31.8 - - - - 34.4 - - - R47 31.8 - - - - 36.6 - - - R48 31.8 - - - - 34.5 - - - 31.8 - - - - 37.2 - - - I R49 R50 31.8 - - - - 34.6 - - - R51 31.8 - - - - 37.9 - - - I R52 R53 31.8 31.8 - - - - 34.7 - - - - - - - 38.7 - - - R54 31.8 - - - - 34.8 - - - R55 31.8 - - - - 39.6 - - - I R56 31.8 - - - - 34.9 - - - R57 31.8 - - - - 40.7 - - - R58 31.8 - - - - 35.0 - - - 31.8 - - - - 41.9 - - - I R59 R60 31.8 - - - - 35.1 - - - R61 31.8 - - - - 43.4 - - - R62 31.8 - - - - 35.2 - - - I Ml 30.8 - - - - 28.6 - - - M2 30.8 - - - - 32.8 - - - M3 30.8 - - - - 28.6 - - - 30.8 - - - - 32.8 - - , - I M4 M5 30.8 - - - - 28.9 - - - M6 30.8 - - - - 32.9 - - - 30.8 - - - - 29.5 - - - I M7 M8 30.8 - - - - 32.9 - - - M9 30.8 - - - - 30.1 - - - MiD 30.8 - - - 33.0 - - - I Mil 30.8 - - - - 30.7 - - - M12 30.8 - - - - 33.0 - - - M13 30.8 - - - - 31.2 - - - 30.8 - - - - 33.1 - - - I M14 M15 30.8 - - - - 31.7 - - - M16 30.8 - - - - 33.2 - - - I M17 MiS 30.8 30.8 - - - - 32.1 - - - - - - - 33.3 - - - M19 30.8 - - - - 32.5 - - - M20 30.8 - - - - 33.4 - - - I M21 30.8 - - - - 32.8 - - - M22 30.8 - - - - 33.5 - - - M23 30.8 - - - - - 33.1 - - - M24 30.8 - - - - 33.6 - - - I M25 30.8 - - - - 33.4 - - - M26 30.8 - - - 33.7 - - - M27 30.8 - - - - 33.7 - - - I M28 30.8 - - - - 33.8 - - - M29 30.8 - - - - 33.9 - - - M30 30.8 - - - - 33.9 - - - M31 30.8 - - - - 34.2 - - - I M32 30.8 - - - - 34.0 - - - I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 9/4/2009SENT\C-2625 LIFE TECHNOLOGIES RACKS\CALCULATIONS\AREA B.SDF JOB TITLE: Area B I NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) I M33 30.8 - - - - 34.5 - - M34 30.8 - - - - 34.2 - - - M35 30.8 - - - - 34.7 - - - I M36 30.8 - - - - 34.3 - - - M37 30.8 - - - - 35.1 - - - M38 30.8 - - - - 34.4 - - - 30.8 - - - - 35.4 - - - I M39 M40 30.8 - - - - 34.5 - - - M41 30.8 - - - - 35.8 - - - I M42 M43 30.8 30.8 - - - - 34.6 - - - - - - - 36.2 - - - M44 30.8 - - - - 34.7 - - - M45 30.8 - - - - 36.7 - - - I M46 30.8 - - - - 34.7 - - - M47 30.8 - - - - 37.2 - - - M48 30.8 - - - - 34.8 - - - 30.8 - - - - 37.9 - - - I M49 M50 30.8 - - - - 34.9 - - - M51 30.8 - - - - 38.6 - - - 30.8 - - - - 34.9 - - - I M52 M53 30.8 - - - - 39.4 - - - M54 30.8 - - - - 34.9 - - - M55 30.8 - - - - 40.4 - - - 30.8 - - - - 35.0 - - I M56 M57 30.8 - - - - 41.6 - - - M58 30.8 - - - - 35.0 - - - - M59 M60 30.8 30.8 - - - - 42.9 - - - - - - - 35.0 - - - M61 30.8 - - - - 44.5 - - - M62 30.8 - - - - 35.0 - - - I TOR 30.8 - - - - 46.9 - - - BOR 0.5 - - - - 64.1 - - - DI -3.0 - - - - 66.1 - - - -3.0 - - - - 66.6 - - - I UG1 UG4 -3.0 - - - - 72.6 - - - UGS -3.0 - - - - 73.2 - - - - UG6 -3.0 - - - - 81.9 - - - I UG7 -3.0 - - - - 82.7 - - - BF1 3.0 - - - - 70.9 - - - 3F2 3.0 - - - - 78.9 - - - SRC 0.0 SOURCE 83.4 1199.0 I I I I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 9/4/2009SENT\C -2625 LIFE TECHNOLOGIES RACKS\CALCULATIONS\AREA B.SDF JOB TITLE: Area B PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. I END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (PT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) - Pipe: 1 121.9 2.157 PL 76.50 PF 9.8 I R2 31.8 0.0 31.0 0.0 10.7 120 FTG T PE 0.0 51 31.8 8.0 21.2 36.9 0.110 TL 88.50 PV I Pipe: 2 85.1 2.157 PL 8.00 PF 0.5 Si 31.8 8.0 21.2 36.9 7.5 120 FTG ---- PE 0.0 S2 31.8 8.0 20.8 36.5 0.057 TL 8.00 PV I Pipe: 3 48.6 2.157 PL 8.00 PP 0.4 S2 31.8 8.0 20.8 36.5 4.3 120 FTG T FE 0.0 I S3 31.8 8.0 20.4 36.1 0.020 TL 20.00 PV Pipe: 4 12.5 2.157 PL 8.00 PP 0.0 S3 31.8 8.0 20.4 36.1 1.1 120 FTG ---- FE 0.0 I S4 31.8 8.0 20.3 36.1 0.002 TL 8.00 PV Pipe: 5 -23.5 2.157 FL 8.00 PF 0.0 I S4 31.8 8.0 20.3 36.1 2.1 120 FTG ---- PE 0.0 S5 31.8 8.0 20.4 36.1 0.005 TL 8.00 PV Pipe: 6 -59.7 2.157 PL 8.00 PF 0.2 I S5 31.8 8.0 20.4 36.1 5.2 120 FTG ---- PE 0.0 S6 31.8 8.0 20.6 36.3 0.029 TL 8.00 PV Pipe: 7 -96.0 2.157 PL 8.00 PF 0.6 S6 31.8 8.0 20.6 36.3 8.4 120 FTG ---- FE 0.0 S7 31.8 8.0 21.2 36.8 0.071 TL 8.00 PV I Pipe: 8 -132.8 2.157 FL 8.00 PP 1.0 S7 31.8 8.0 21.2 36.8 11.7 120 FTG ---- FE 0.0 S8 31.8 8.0 22.2 37.7 0.129 TL 8.00 PV I Pipe: 9 -170.6 2.157 PL 3.83 PP 3.2 S8 31.8 8.0 22.2 37.7 15.0 120 FTG T PE 0.0 I Ri 31.8 0.0 25.5 0.0 0.205 TL 15.83 PV Pipe: 10 122.6 2.157 PL 76.50 PF 9.9 R4 31.8 0.0 31.0 0.0 10.8 120 FTG T FE 0.0 I S9 31.8 8.0 21.1 36.8 0.111 TL 88.50 PV Pipe: 11 85.9 2.157 PL 8.00 PF 0.5 I S9 31.8 8.0 21.1 36.8 7.5 120 FTG ---- FE 0.0 Slo 31.8 8.0 20.6 36.3 0.058 TL 8.00 PV Pipe: 12 49.5 2.157 PL 8.00 PP 0.2 I S1O 31.8 8.0 20.6 36.3 4.3 120 FTG ---- FE 0.0 511 31.8 8.0 20.5 36.2 0.021 TL 8.00 PV I I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 9/4/2009SENT\C-2625 LIFE TECHNOLOGIES RACKS\CALCULATIONS\AREA B.SDF JOB TITLE: Area B I 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) I Pipe: 13 13.3 2.157 PL 8.00 PF 0.0 Sil 31.8 8.0 20.5 36.2 1.2 120 FTG ---- PE 0.0 I S12 31.8 8.0 20.5 36.2 0.002 TL 8.00 PV Pipe: 14 -22.9 2.157 PL 8.00 PF 0.0 S12 31.8 8.0 20.5 36.2 2.0 120 FTG ---- PE 0.0 S13 31.8 8.0 20.5 36.2 0.005 TL 8.00 PV Pipe: 15 -59.1 2.157 PL 8.00 PF 0.2 I S13 31.8 8.0 20.5 36.2 5.2 120 FTG ---- PE 0.0 S14 31.8 8.0 20.7 36.4 0.029 TL 8.00 PV Pipe: 16 -95.5 2.157 PL 8.00 PF 0.6 I S14 31.8 8.0 20.7 36.4 8.4 120 FTG ---- PE 0.0 S15 31.8 8.0 21.3 36.9 0.070 TL 8.00 PV Pipe: 17 -132.4 2.157 PL 8.00 PF 1.0 S15 31.8 8.0 21.3 36.9 11.6 120 FTG ---- PE 0.0 S16 31.8 8.0 22.3 37.8 0.128 TL 8.00 PV I Pipe: 18 -170.2 2.157 PL 3.83 PF 3.2 S16 31.8 8.0 22.3 37.8 14.9 120 FTG T PE 0.0 R3 31.8 0.0 25.6 0.0 0.204 TL 15.83 PV I Pipe: 19 122.1 2.157 PL 76.50 PF 9.8 R6 31.8 0.0 31.0 0.0 10.7 120 FTG T PE 0.0 I S17 31.8 8.0 21.2 36.9 0.110 TL 88.50 PV Pipe: 20 85.2 2.157 PL 8.00 PF 0.5 S17 31.8 8.0 21.2 36.9 7.5 120 FTG ---- PE 0.0 I S18 31.8 8.0 20.8 36.5 0.057 TL 8.00 PV Pipe: 21 48.8 2.157 PL 8.00 PF 0.2 I S18 31.8 8.0 20.8 36.5 4.3 120 FTG ---- PE 0.0 S19 31.8 8.0 20.6 36.3 0.020 TL 8.00 PV Pipe: 22 12.5 2.157 PL 8.00 PF 0.0 I S19 31.8 8.0 20.6 36.3 1.1 120 FTG ---- PE 0.0 S20 31.8 8.0 20.6 36.3 0.002. TL 8.00 PV I Pipe: 23 -23.8 2.157 PL 8.00 PF 0.0 S20 31.8 8.0 20.6 36.3 2.1 120 FTG ---- PE 0.0 S21 31.8 8.0 20.6 36.3 0.005 TL 8.00 PV I Pipe: 24 -60.2 2.157 PL 8.00 PF 0.2 - S21 31.8 8.0 20.6 36.3 5.3 120 FTG ---- PE 0.0 I S22 31.8 8.0 20.9 36.5 0.030 TL 8.00 PV Pipe: 25 -96.7 2.157 PL 8.00 PF 0.6 S22 31.8 8.0 20.9 36.5 8.5 120 FTC ---- PE 0.0 S23 31.8 8.0 21.4 37.0 0.072 TL 8.00 PV I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 9/4/2009SENT\C-2625 LIFE TECHNOLOGIES RACKS\CALCULATIONS\AREA B.SDF JOB TITLE: Area B I 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) I Pipe: 26 -133.8 2.157 PL 8.00 PF 1.0 S23 31.8 8.0 21.4 37.0 11.7 120 FTG ---- PE 0.0 I S24 31.8 8.0 22.5 37.9 0.131 TL 8.00 PV Pipe: 27 -171.7 2.157 PL 3.83 PF 3.3 S24 31.8 8.0 22.5 37.9 15.1 120 FTG T PE 0.0 I R5 31.8 0.0 25.8 0.0 0.208 TL 15.83 PV Pipe: 28 66.7 2.157 PL 76.50 PF 3.2 I R8 31.8 0.0 32.0 0.0 5.9 120 FTG T PE 0.0 S25 31.8 8.0 28.8 42.9 0.036 TL 88.50 PV Pipe: 29 23.7 2.157 PL 8.00 PF 0.0 I S25 31.8 8.0 28.8 42.9 2.1 120 FTG ---- PE 0.0 S26 31.8 8.0 28.8 42.9 0.005 TL 8.00 PV Pipe: 30 -19.2 2.157 PL 51.83 PF 0.2 S26 31.8 8.0 28.8 42.9 1.7 120 FTG T PE 0.0 R7 31.8 0.0 29.0 0.0 0.004 TL 63.83 PV I Pipe: 46 -37.5 2.157 PL 136.33 PF 2.0 Rll 31.8 0.0 30.4 0.0 3.3 120 FTG 2T PE 0.0 R12 31.8 0.0 32.4 0.0 0.012 TL 160.33 PV I Pipe: 47 -33.3 2.157 PL 136.33 PF 1.6 R13 31.8 0.0 30.9 0.0 2.9 120 FTG 2T PE 0.0 I R14 31.8 0.0 32.5 0.0 0.010 TL 160.33 PV Pipe: 48 -29.3 2.157 PL 136.33 PF 1.3 R15 31.8 0.0 31.4 0.0 2.6 120 FTG 2T PE 0.0 R16 31.8 0.0 32.6 0.0 0.008 TL 160.33 PV Pipe: 49 -25.6 2.157 PL 136.33 PF 1.0 I R17 31.8 0.0 31.8 0.0 2.2 120 FTG 2T PE 0.0 R18 31.8 0.0 32.7 0.0 0.006 TL 160.33 PV Pipe: 50 -22.0 2.157 PL 136.33 PF 0.7 I R19 31.8 0.0 32.1 0.0 1.9 120 FTG 2T PE 0.0 R20 31.8 0.0 32.9 0.0 . 0.005 TL 160.33 PV I . Pipe: 51 -18.6 2.157 PL 136.33 PF 0.5 R21 31.8 0.0 32.4 0.0 1.6 120 FTG 2T PE 0.0 R22 31.8 0.0 33.0 0.0 0.003 TL 160.33 PV I Pipe: 52 -15.2 2.157 PL 136.33 PF 0.4 R23 31.8 0.0 32.7 0.0 1.3 120 FTG 2T PE 0.0 R24 31.8 0.0 33.1 0.0 0.002 TL 160.33 PV I Pipe: 53 -11.7 2.157 PL 136.33 PF 0.2 R25 31.8 0.0 33.0 0.0 1.0 120 FTG 2T PE 0.0 R26 31.8 0.0 33.2 0.0 0.001 TL 160.33 PV I DATE: I SPRINKLER SYSTEM HYDRAULIC ANALYSIS 9/4/2009SENT\C -2625 LIFE TECHNOLOGIES RACKS\CALCULATIONS\AREA Page 9 B.SDF JOB TITLE: Area B I PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (PT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) I Pipe: 54 -7.6 2.157 PL 136.33 PF 0.1 R27 31.8 0.0 33.3 0.0 0.7 120 FTG 2T PE 0.0 R28 31.8 0.0 33.4 0.0 0.001 TL 160.33 PV I Pipe: 55 2.1 2.157 PL 136.33 PF 0.0 R29 31.8 0.0 33.5 0.0 0.2 120 FTG 2T PE 0.0 I R30 31.8 0.0 33.5 0.0 0.000 TL 160.33 PV Pipe: 56 8.5 2.157 PL 136.33 PF 0.1 I R31 R32 31.8 31.8 0.0 0.0 33.7 33.6 0.0 0.0 0.7 120 0.001 FTG TL 2T 160.33 PE PV 0.0 Pipe: 57 12.4 2.157 PL 136.33 PF 0.3 I R33 31.8 0.0 34.0 0.0 1.1 120 FTG 2T PE 0.0 R34 31.8 0.0 33.7 0.0 0.002 TL 160.33 PV 58 15.9 2.157 PL 136.33 PP 0.4 I Pipe: R35 31.8 0.0 34.3 0.0 1.4 120 FTG 2T PE 0.0 R36 31.8 0.0 33.9 0.0 0.003 TL 160.33 PV I Pipe: 59 19.3 2.157 PL 136.33 PF 0.6 R37 31.8 0.0 34.6 0.0 1.7 120 FTG 2T PE 0.0 R38 31.8 0.0 34.0 0.0 0.004 TL 160.33 PV I Pipe: 60 22.8 2.157 PL 136.33 PF 0.8 R39 31.8 0.0 34.9 0.0 2.0 120 FTG 2T PE 0.0 l R40 31.8 0.0 34.1 0.0 0.005 TL 160.33 PV Pipe: 61 26.4 2.157 PL 136.33 PP 1.0 R41 31.8 0.0 35.3 0.0 2.3 120 FTG 2T PE 0.0 R42 31.8 0.0 34.2 0.0 0.006 TL 160.33 PV Pipe: 62 30.2 2.157 PL 136.33 PP 1.3 31.8 0.0 35.7 0.0 2.7 120 FTG 2T PE 0.0 I R43 R44 31.8 0.0 34.3 0.0 0.008 TL 160.33 PV Pipe: 63 34.2 2.157 PL 136.33 PF 1.7 R45 31.8 0.0 36.1 0.0 3.0 120 FTG 2T PE 0.0 R46 31.8 0.0 34.4 0.0 0.011 TL 160.33 PV I Pipe: 64 38.6 2.157 PL 136.33 PP 2.1 R47 31.8 0.0 36.6 0.0 3.4 120 FTG 2T PE 0.0 R48 31.8 0.0 34.5 0.0 0.013 TL 160.33 PV I Pipe: 65 43.2 2.157 PL 136.33 PP 2.6 R49 31.8 0.0 37.2 0.0 3.8 120 FTG 2T PE 0.0 R50 31.8 0.0 34.6 0.0 0.016 TL 160.33 PV I Pipe: 66 48.3 2.157 PL 136.33 PP 3.2 R51 31.8 0.0 37.9 0.0 4.2 120 FTG 2T PE 0.0 R52 31.8 0.0 34.7 0.0 0.020 TL 160.33 PV I SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 'SPRINKLER 9/4/2009SENT\C-2625 LIFE TECHNOLOGIES RACKS\CALCULATIONS\AREA B.SDF JOB TITLE: Area B I 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) I Pipe: 67 53.7 2.157 PL 136.33 PF 3.9 R53 31.8 0.0 38.7 0.0 4.7 120 FTG 2T PE 0.0 I R54 31.8 0.0 34.8 0.0 0.024 TL 160.33 PV Pipe: 68 59.6 2.157 PL 136.33 PF 4.7 R55 31.8 0.0 39.6 0.0 5.2 120 FTG 2T PE 0.0 R56 31.8 0.0 34.9 0.0 0.029 TL 160.33 FV Pipe: 69 65.9 2.157 FL 136.33 PF 5.7 31.8 0.0 40.7 0.0 5.8 120 FTG 2T PE 0.0 I R57 R58 31.8 0.0 35.0 0.0 0.035 TL 160.33 PV Pipe: 70 72.8 2.157 PL 136.33 PF 6.8 I R59 31.8 0.0 41.9 0.0 6.4 120 FTG 2T PE 0.0 R60 31.8 0.0 35.1 0.0 0.042 TL 160.33 PV 71 80.3 2.157 PL 136.33 PF 8.2 I Pipe: R61 31.8 0.0 43.4 0.0 7.0 120 FTG 2T PE 0.0 R62 31.8 0.0 35.2 0.0 0.051 TL 160.33 PV I Pipe: 72 -170.6 2.157 FL 1.00 PF 2.7 - Ri 31.8 0.0 25.5 0.0 15.0 120 FTG T PE 0.4 Ml 30.8 0.0 28.6 0.0 0.205 TL 13.00 PV I Pipe: 73 -121.9 2.157 PL 1.00 PF 1.4 R2 31.8 0.0 31.0 0.0 10.7 120 FTG T PE 0.4 ' M2 30.8 0.0 32.8 0.0 0.110 TL 13.00 PV Pipe: 74 -170.2 2.157 PL 1.00 PF 2.7 R3 31.8 0.0 25.6 0.0 14.9 120 FTG T PE 0.4 M3 30.8 0.0 28.6 0.0 0.204 TL 13.00 PV Pipe: 75 -122.6 2.157 PL 1.00 PF 1.4 31.8 0.0 31.0 0.0 10.8 120 FTG T FE 0.4 I R4 M4 30.8 0.0 32.8 0.0 0.111 TL 13.00 PV • Pipe: 76 -171.7 2.157 FL 1.00 PF 2.7 R5 31.8 0.0 25.8 0.0 15.1 120 FTG T FE 0.4 M5 30.8 0.0 28.9 0.0 0.208 TL 13.00 PV I Pipe: 77 -122.1 2.157 FL 1.00 PF 1.4 U R6 31.8 0.0 31.0 0.0 10.7 120 FTG T PE 0.4 M6 30.8 0.0 32.9 0.0 0.110 TL 13.00 PV I Pipe: 78 -19.2 2.157 PL 1.00 PF 0.0 R7 31.8 0.0 29.0 0.0 1.7 120 FTG T PE 0.4 M7 30.8 0.0 29.5 0.0 0.004 TL 13.00 PV I Pipe: 79 -66.7 2.157 PL 1.00 PF 0.5 R8 31.8 0.0 32.0 0.0 5.9 120 FTG T FE 0.4 M8 30.8 0.0 32.9 0.0 0.036 TL 13.00 PV I DATE: I SPRINKLER SYSTEM HYDRAULIC ANALYSIS 9/4/2009SENT\C -2625 LIFE TECHNOLOGIES RACKS\CALCULATIONS\AREA Page 11 B.SDF JOB TITLE: Area B I 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: 80 0.0 2.157 FL 1.00 PF 0.0 R9 31.8 0.0 29.7 0.0 0.0 120 FTG T PE 0.4 M9 30.8 0.0 30.1 0.0 0.000 TL 13.00 PV I Pipe: 81 0.0 2.157 FL 1.00 PF 0.0 RiO 31.8 0.0 32.5 0.0 0.0 120 FTG T FE 0.4 I M10 30.8 0.0 33.0 0.0 0.000 TL 13.00 Fv Pipe: 82 37.5 2.157 FL 1.00 PF 0.2 31.8 0.0 30.4 0.0 3.3 120 FTG T FE 0.4 I Rll Mil 30.8 0.0 30.7 0.0 0.012 TL 13.00 PV Pipe: 83 -37.5 2.157 FL 1.00 PF 0.2 I R12 31.8 0.0 32.4 0.0 3.3 120 FTG T FE 0.4 M12 30.8 0.0 33.0 0.0 0.012 TL 13.00 FV I Pipe: 84 33.3 2.157 FL 1.00 PF 0.1 R13 31.8 0.0 30.9 0.0 2.9 120 FTG T FE 0.4 M13 30.8 0.0 31.2 0.0 0.010 TL 13.00 PV Pipe: 85 -33.3 2.157 FL 1.00 PF 0.1 • R14 31.8 0.0 32.5 0.0 2.9 120 FTG T FE 0.4 M14 30.8 0.0 33.1 0.0 0.010 TL 13.00 PV I Pipe: 86 29.3 2.157 FL 1.00 PP 0.1 R15 31.8 0.0 31.4 0.0 2.6 120 FTG T FE 0.4 I MiS 30.8 0.0 31.7 0.0 0.008 TL 13.00 PV Pipe: 87 -29.3 2.157 FL 1.00 PF 0.1 R16 31.8 0.0 32.6 0.0 2.6 120 FTG T FE 0.4 M16 30.8 0.0 33.2 0.0 0.008 TL 13.00 PV Pipe: 88 25.6 2.157 FL 1.00 PF 0.1 31.8 0.0 31.8 0.0 2.2 120 FTG T FE 0.4 I R17 M17 30.8 0.0 32.1 0.0 0.006 TL 13.00 PV - Pipe: 89 -25.6 2.157 FL 1.00 PP 0.1 I R18 31.8 0.0 32.7 0.0 2.2 120 FTG T FE 0.4 M18 30.8 0.0 33.3 0.0 0.006 TL 13.00 PV • Pipe: 90 22.0 2.157 FL 1.00 PF 0.1 • R19 31.8 0.0 32.1 0.0 1.9 120 FTG T FE 0.4 M19 30.8 0.0 32.5 0.0 0.005 TL 13.00 PV I Pipe: 91 -22.0 2.157 FL 1.00 PF 0.1 R20 31.8 0.0 32.9 0.0 1.9 120 FTG T FE 0.4 M20 30.8 0.0 33.4 0.0 0.005 TL 13.00 PV I Pipe: 92 18.6 2.157 FL 1.00 PP 0.0 R21 31.8 0.0 32.4 0.0 1.6 120 FTG T FE 0.4 M21 30.8 0.0 32.8 0.0 0.003 TL 13.00 PV I DATE: I SPRINKLER SYSTEM HYDRAULIC ANALYSIS 9/4/2009SENT\C-2625 LIFE TECHNOLOGIES RACKS\CALCULATIONS\AREA Page 12 B.SDF JOB TITLE: Area B I 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) I Pipe: 93 -18.6 2.157 PL 1.00 PF 0.0 R22 31.8 0.0 33.0 0.0 1.6 120 FTG T PE 0.4 M22 30.8 0.0 33.5 0.0 0.003 TL 13.00 PV I Pipe: 94 15.2 2.157 FL 1.00 PF 0.0 R23 31.8 0.0 32.7 0.0 1.3 120 FTG T FE 0.4 M23 30.8 0.0 33.1 0.0 0.002 TL 13.00 PV Pipe: 95 -15.2 2.157 FL 1.00 PF 0.0 I R24 M24 31.8 30.8 0.0 0.0 33.1 33.6 0.0 0.0 1.3 120 0.002 FTG TL T 13.00 PE PV 0.4 Pipe: 96 11.7 2.157 PL 1.00 PF 0.0 I R25 31.8 0.0 33.0 0.0 1.0 120 FTG T FE 0.4 M25 30.8 0.0 33.4 0.0 0.001 TL 13.00 PV • Pipe: 97 -11.7 2.157 FL 1.00 PF 0.0 • R26 31.8 0.0 33.2 0.0 1.0 120 FTG T FE 0.4 M26 30.8 0.0 33.7 0.0 0.001 TL 13.00 PV Pipe: 98 7.6 2.157 FL 1.00 PF 0.0 - R27 31.8 0.0 33.3 0.0 0.7 120 FTG T FE 0.4 M27 30.8 0.0 33.7 0.0 0.001 TL 13.00 PV Pipe: 99 -7.6 2.157 FL 1.00 PF 0.0 R28 31.8 0.0 33.4 0.0 0.7 120 FTG T PS 0.4 M28 30.8 0.0 33.8 0.0 0.001 TL 13.00 PV Pipe; 101 -2.1 2.157 FL 1.00 PP 0.0 R29 31.8 0.0 33.5 0.0 0.2 120 FTG T FE 0.4 I M29 30.8 0.0 33.9 0.0 0.000 TL 13.00 PV Pipe: 102 2.1 2.157 FL 1.00 PF 0.0 31.8 0.0 33.5 0.0 0.2 120 FTG T FE 0.4 I R30 M30 30.8 0.0 33.9 0.0 0.000 TL 13.00 PV - Pipe: 103 -8.5 2.157 FL 1.00 PP 0.0 I R31 31.8 0.0 33.7 0.0 0.7 120 FTG T FE 0.4 M31 30.8 0.0 34.2 0.0 0.001 TL 13.00 PV I Pipe: 104 8.5 2.157 FL 1.00 PP 0.0 • R32 31.8 0.0 33.6 0.0 0.7 120 FTG T FE 0.4 M32 30.8 0.0 34.0 0.0 0.001 TL 13.00 PV I Pipe: 105 -12.4 2.157 FL 1.00 PP 0.0 R33 31.8 0.0 34.0 0.0 1.1 120 FTG T FE 0.4 M33 30.8 0.0 34.5 0.0 0.002 TL 13.00 PV I Pipe: 106 12.4 2.157 FL 1.00 PP 0.0 R34 31.8 0.0 33.7 0.0 1.1 120 FTG T PS 0.4 M34 30.8 0.0 34.2 0.0 0.002 TL 13.00 PV I SYSTEM HYDRAULIC ANALYSIS Page 13 DATE: I SPRINKLER 9/4/2009SENT\C -2625 LIFE TECHNOLOGIES RACKS\CALCULATIONS\AREA B.SDF JOB TITLE: Area B U 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) I Pipe: 107 -15.9 2.157 PL 1.00 PF 0.0 R35 31.8 0.0 34.3 0.0 1.4 120 FTG T PE 0.4 M35 30.8 0.0 34.7 0.0 0.003 TL 13.00 PV Pipe: 108 15.9 2.157 PL 1.00 PF 0.0 R36 31.8 0.0 33.9 0.0 1.4 120 FTG T PE 0.4 M36 30.8 0.0 34.3 0.0 0.003 TL 13.00 PV Pipe: 109 -19.3 2.157 PL 1.00 PF 0.0 31.8 0.0 34.6 0.0 1.7 120 FTG T PE 0.4 I R37 M37 30.8 0.0 35.1 0.0 0.004 TL 13.00 PV - Pipe: 110 19.3 2.157 PL 1.00 PF 0.0 I R38 31.8 0.0 34.0 0.0 1.7 120 FTG T PE 0.4 M38 30.8 0.0 34.4 0.0 0.004 TL 13.00 PV • Pipe: 111 -22.8 2.157 PL 1.00 PF 0.1 • R39 31.8 0.0 34.9 0.0 2.0 120 FTG T PE 0.4 M39 30.8 0.0 35.4 0.0 0.005 TL 13.00 PV I Pipe: 112 22.8 2.157 PL 1.00 PF 0.1 - R40 31.8 0.0 34.1 0.0 2.0 120 FTG T PE 0.4 M40 30.8 0.0 34.5 0.0 0.005 TL 13.00 PV I Pipe: 113 -26.4 2.157 PL 1.00 PF 0.1 R41 31.8 0.0 35.3 0.0 2.3 120 FTG T PE 0.4 I M41 30.8 0.0 35.8 0.0 0.006 TL 13.00 PV Pipe: 114 26.4 2.157 PL 1.00 PF 0.1 R42 31.8 0.0 34.2 0.0 2.3 120 FTG T PE 0.4 M42 30.8 0.0 34.6 0.0 0.006 TL 13.00 PV Pipe: 115 -30.2 2.157 PL 1.00 PF 0.1 31.8 0.0 35.7 0.0 2.7 120 FTG T PE 0.4 I R43 M43 30.8 0.0 36.2 0.0 0.008 TL 13.00 PV • Pipe: 116 30.2 2.157 PL 1.00 PF 0.1 R44 31.8 0.0 34.3 0.0 2.7 120 FTG T FE 0.4 M44 30.8 0.0 34.7 0.0 0.008 TL 13.00 PV I Pipe: 117 -34.2 2.157 PL 1.00 PF 0.1 • R45 31.8 0.0 36.1 0.0 3.0 120 FTG T FE 0.4 M45 30.8 0.0 36.7 0.0 0.011 TL 13.00 PV I Pipe: 118 34.2 2.157 FL 1.00 PF 0.1 R46 31.8 0.0 34.4 0.0 3.0 120 FTG T PE 0.4 M46 30.8 0.0 34.7 0.0 0.011 TL 13.00 PV I Pipe: 119 -38.6 2.157 PL 1.00 PF 0.2 R47 31.8 0.0 36.6 0.0 3.4 120 FTG T PE 0.4 M47 30.8 0.0 37.2 0.0 0.013 TL 13.00 PV I SYSTEM HYDRAULIC ANALYSIS Page 14 DATE: I SPRINKLER 9/4/2009SENT\C -2625 LIFE TECHNOLOGIES RACKS\CALCULATIONS\AREA B.SDF JOB TITLE: Area B I 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: 120 38.6 2.157 PL 1.00 PF 0.2 R48 31.8 0.0 34.5 0.0 3.4 120 FTG T PE 0.4 I M48 30.8 0.0 34.8 0.0 0.013 TL 13.00 PV Pipe: 121 -43.2 2.157 PL 1.00 PF 0.2 R49 31.8 0.0 37.2 0.0 3.8 120 FTG T PE 0.4 M49 30.8 0.0 37.9 0.0 0.016 TL 13.00 PV Pipe: 122 43.2 2.157 PL 1.00 PF 0.2 31.8 0.0 34.6 0.0 3.8 120 FTC T PE 0.4 I R50 M50 30.8 0.0 34.9 0.0 0.016 TL 13.00 PV I R51 Pipe: 123 31.8 0.0 37.9 0.0 -48.3 4.2 2.157 120 PL FTG 1.00 T PF PE 0.3 0.4 M51 30.8 0.0 38.6 0.0 0.020 TL 13.00 PV • Pipe: 124 48.3 2.157 PL 1.00 PF 0.3 • R52 31.8 0.0 34.7 0.0 4.2 120 FTG T PE 0.4 M52 30.8 0.0 34.9 0.0 0.020 TL 13.00 PV Pipe: 125 -53.7 2.157 PL 1.00 PF 0.3 - R53 31.8 0.0 38.7 0.0 4.7 120 FTG T PE 0.4 M53 30.8 0.0 39.4 0.0 0.024 TL 13.00 PV I Pipe: 126 53.7 2.157 PL 1.00 PF 0.3 R54 31.8 0.0 34.8 0.0 4.7 120 FTG T PE 0.4 I M54 30.8 0.0 34.9 0.0 0.024 TL 13.00 PV Pipe: 127 -59.6 2.157 PL 1.00 PF 0.4 R55 31.8 0.0 39.6 0.0 5.2 120 FTG T PE 0.4 M55 30.8 0.0 40.4 0.0 0.029 TL 13.00 PV Pipe: 128 59.6 2.157 PL 1.00 PF 0.4 31.8 0.0 34.9 0.0 5.2 120 FTG T PE 0.4 I R56 M56 30.8 0.0 35.0 0.0 0.029 TL 13.00 PV - Pipe: 129 -65.9 2.157 PL 1.00 PF 0.5 I R57 31.8 0.0 40.7 0.0 5.8 120 FTG T PE 0.4 M57 30.8 0.0 41.6 0.0 0.035 TL 13.00 PV Pipe: 130 65.9 2.157 PL 1.00 PF 0.5 • R58 31.8 0.0 35.0 0.0 5.8 120 FTG T PE 0.4 M58 30.8 0.0 35.0 0.0 0.035 TL 13.00 PV I Pipe: 131 -72.8 2.157 PL 1.00 PF 0.6 R59 31.8 0.0 41.9 0.0 6.4 120 FTG T PE 0.4 N59 30.8 0.0 42.9 0.0 0.042 TL 13.00 PV I Pipe: 132 72.8 2.157 FL 1.00 PF 0.6 R60 31.8 0.0 35.1 0.0 6.4 120 FTG T PE 0.4 M60 30.8 0.0 35.0 0.0 0.042 TL 13.00 PV I SYSTEM HYDRAULIC ANALYSIS Page 15 DATE: I SPRINKLER 9/4/2009SENT\C -2625 LIFE TECHNOLOGIES P.ACKS\CALCULATIONS\AREA B.SDF JOB TITLE: Area B I 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: 133 -80.3 2.157 FL 1.00 PF 0.7 R61 31.8 0.0 43.4 0.0 7.0 120 FTG T PE 0.4 I MGi 30.8 0.0 44.5 0.0 0.051 TL 13.00 PV Pipe: 134 80.3 2.157 PL 1.00 PF 0.7 R62 31.8 0.0 35.2 0.0 7.0 120 FTG T PE 0.4 M62 30.8 0.0 35.0 0.0 0.051 TL 13.00 PV Pipe: 135 -170.6 4.260 FL 10.00 PF 0.1 • Ml 30.8 0.0 28.6 0.0 3.8 120 FTG ---- PE 0.0 30.8 0.0 28.6 0.0 0.007 TL 10.00 PV Pipe: 136 -340.8 4.260 PL 10.00 PF 0.3 I M3 30.8 0.0 28.6 0.0 7.7 120 FTG ---- PE 0.0 M5 30.8 0.0 28.9 0.0 0.027 TL 10.00 PV 137 -512.5 4.260 PL 10.00 PF 0.6 I Pipe: M5 30.8 0.0 28.9 0.0 11.5 120 FTG ---- FE 0.0 M7 30.8 0.0 29.5 0.0 0.057 TL 10.00 PV I Pipe: 138 -531.7 4.260 FL 10.00 PF 0.6 M7 30.8 0.0 29.5 0.0 12.0 120 FTG ---- PE 0.0 M9 30.8 0.0 30.1 0.0 0.061 TL 10.00 PV I Pipe: 139 -531.7 4.260 PL 10.00 PF 0.6 M9 30.8 0.0 30.1 0.0 12.0 120 FTG ---- PE 0.0 I Nil 30.8 0.0 30.7 0.0 0.061 TL 10.00 PV Pipe: 140 -494.1 4.260 FL 10.00 PF 0.5 Mil 30.8 0.0 30.7 0.0 11.1 120 FTG ---- PE 0.0 I M13 30.8 0.0 31.2 0.0 0.053 TL 10.00 PV Pipe: 141 -460.8 4.260 PL 10.00 PF 0.5 30.8 0.0 31.2 0.0 10.4 120 FTG ---- FE 0.0 I M13 M15 30.8 0.0 31.7 0.0 0.047 TL 10.00 PV 142 -431.5 4.260 FL 10.00 PF 0.4 I Pipe: M15 30.8 0.0 31.7 0.0 9.7 120 FTG ---- PE 0.0 M17 30.8 0.0 32.1 0.0 0.042 TL 10.00 PV • Pipe: 143 -406.0 4.260 FL 10.00 PF 0.4 • M17 30.8 0.0 32.1 0.0 9.1 120 FTG ---- PE 0.0 M19 30.8 0.0 32.5 0.0 0.037 TL 10.00 PV Pipe: 144 -383.9 4.260 PL 10.00 PF 0.3 M19 30.8 0.0 32.5 0.0 8.6 120 FTG ---- PE 0.0 M21 30.8 0.0 32.8 0.0 0.033 TL 10.00 PV I Pipe: 145 -365.3 4.260 PL 10.00 PF 0.3 M21 30.8 0.0 32.8 0.0 8.2 120 FTG ---- FE 0.0 M23 30.8 0.0 33.1 0.0 0.031 TL 10.00 PV I DATE: I SPRINKLER SYSTEM HYDRAULIC ANALYSIS 9/4/2009SENT\C -2625 LIFE TECHNOLOGIES RACKS\CALCULATIONS\AREA Page 16 B.SDF JOB TITLE: Area B I 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) I Pipe: 146 -350.1 4.260 FL 10.00 PF 0.3 M23 30.8 0.0 33.1 0.0 7.9 120 FTG ---- PE 0.0 M25 30.8 0.0 33.4 0.0 0.028 TL 10.00 PV I Pipe: 147 -338.4 4.260 PL 10.00 PF 0.3 M25 30.8 0.0 33.4 0.0 7.6 120 FTG ---- PE 0.0 M27 30.8 0.0 33.7 0.0 0.026 TL 10.00 PV Pipe: 148 -330.8 4.260 PL 10.00 PF 0.3 I M27 M29 30.8 30.8 0.0 0.0 33.7 33.9 0.0 0.0 7.4 120 0.025 FTG TL ---- 10.00 FE PV 0.0 Pipe: 149 -332.9 4.260 PL 10.00 PF 0.3 I M29 30.8 0.0 33.9 0.0 7.5 120 FTG ---- PE 0.0 M31 30.8 0.0 34.2 0.0 0.026 TL 10.00 PV 150 -341.4 4.260 PL 10.00 PF 0.3 I Pipe: M31 30.8 0.0 34.2 0.0 7.7 120 FTG ---- PE 0.0 M33 30.8 0.0 34.5 0.0 0.027 TL 10.00 PV I Pipe: 151 -353.8 4.260 FL 10.00 PF 0.3 M33 30.8 0.0 34.5 0.0 8.0 120 FTG ---- FE 0.0 M35 30.8 0.0 34.7 0.0 0.029 TL 10.00 PV I Pipe: 152 -369.7 4.260 FL 10.00 PF 0.3 M35 30.8 0.0 34.7 0.0 8.3 120 FTG ---- FE 0.0 I M37 30.8 0.0 35.1 0.0 0.031 TL 10.00 PV Pipe: 153 -389.1 4.260 FL 10.00 PF 0.3 M37 30.8 0.0 35.1 0.0 8.8 120 FTG ---- PE 0.0 M39 30.8 0.0 35.4 0.0 0.034 TL 10.00 PV Pipe: 154 -411.8 4.260 FL 10.00 PF 0.4 30.8 0.0 35.4 0.0 9.3 120 FTG ---- FE 0.0 I M39 M41 30.8 0.0 35.8 0.0 0.038 TL 10.00 PV Pipe: 155 -438.2 4.260 FL 10.00 PF 0.4 M41 30.8 0.0 35.8 0.0 9.9 120 FTG ---- FE 0.0 M43 30.8 0.0 36.2 0.0 0.043 TL 10.00 PV I Pipe: 156 -468.4 4.260 FL 10.00 PF 0.5 M43 30.8 0.0 36.2 0.0 10.5 120 FTG ---- PE 0.0 M45 30.8 0.0 36.7 0.0 0.048 TL 10.00 PV I Pipe: 157 -502.7 4.260 FL 10.00 PF 0.6 M45 30.8 0.0 36.7 0.0 11.3 120 FTG ---- PE 0.0 M47 30.8 0.0 37.2 0.0 0.055 TL 10.00 FV I Pipe: 158 -541.2 4.260 FL 10.00 PP 0.6 M47 30.8 0.0 37.2 0.0 12.2 120 FTG ---- PE 0.0 M49 30.8 0.0 37.9 0.0 0.063 TL 10.00 PV I SYSTEM HYDRAULIC ANALYSIS Page 17 DATE: I SPRINKLER 9/4/2009SENT\C -2625 LIFE TECHNOLOGIES RACKS\CALCULATIONS\AREA B.SDF JOB TITLE: Area B I 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) I Pipe: 159 -584.5 4.260 PL 10.00 PF 0.7 M49 30.8 0.0 37.9 0.0 13.2 120 FTG ---- PE 0.0 I M51 30.8 0.0 38.6 0.0 0.073 TL 10.00 PV Pipe: 160 -632.7 4.260 PL 10.00 PF 0.8 M51 30.8 0.0 38.6 0.0 14.2 120 FTG ---- PE 0.0 M53 30.8 0.0 39.4 0.0 0.084 TL 10.00 PV Pipe: 161 -686.4 4.260 FL 10.00 PF 1.0 30.8 0.0 39.4 0.0 15.5 120 FTG ---- PE 0.0 I M53 M55 30.8 0.0 40.4 0.0 0.098 TL 10.00 PV Pipe: 162 -746.0 4.260 PL 10.00 PF 1.1 I M55 30.8 0.0 40.4 0.0 16.8 120 FTG ---- PE 0.0 M57 30.8 0.0 41.6 0.0 0.114 TL 10.00 PV 163 -811.9 4.260 PL 10.00 PF 1.3 I Pipe: M57 30.8 0.0 41.6 0.0 18.3 120 FTG ---- PE 0.0 M59 30.8 0.0 42.9 0.0 0.134 TL 10.00 PV I Pipe: 164 -884.7 4.260 PL 10.00 PF 1.6 M59 30.8 0.0 42.9 0.0 19.9 120 FTG ---- PE 0.0 M61 30.8 0.0 44.5 0.0 0.157 TL 10.00 PV I Pipe: 165 -121.9 6.357 PL 10.00 PF 0.0 M2 30.8 0.0 32.8 0.0 1.2 120 FTG ---- FE 0.0 I M4 30.8 0.0 32.8 0.0 0.001 TL 10.00 PV Pipe: 166 -244.6 6.357 PL 10.00 PF 0.0 M4 30.8 0.0 32.8 0.0 2.5 120 FTG ---- PE 0.0 M6 30.8 0.0 32.9 0.0 0.002 TL 10.00 PV Pipe: 167 -366.7 6.357 PL 10.00 PF 0.0 30.8 0.0 32.9 0.0 3.7 120 FTG ---- PE 0.0 I M6 M8 30.8 0.0 32.9 0.0 0.004 TL 10.00 PV 168 -433.3 6.357 PL 10.00 PF 0.1 I Pipe: M8 30.8 0.0 32.9 0.0 4.4 120 FTG ---- PE 0.0 M10 30.8 0.0 33.0 0.0 0.006 TL 10.00 PV I Pipe: 169 -433.3 6.357 FL 10.00 PF 0.1 M10 30.8 0.0 33.0 0.0 4.4 120 FTG ---- PE 0.0 M12 30.8 0.0 33.0 0.0 0.006 TL 10.00 PV I Pipe: 170 -470.9 6.357 PL 10.00 PF 0.1 M12 30.8 0.0 33.0 0.0 4.8 120 FTG ---- FE 0.0 M14 30.8 0.0 33.1 0.0 0.007 TL 10.00 PV I Pipe: 171 -504.2 6.357 PL 10.00 PF 0.1 M14 30.8 0.0 33.1 0.0 5.1 120 FTG ---- FE 0.0 M16 30.8 0.0 33.2 0.0 0.008 TL 10.00 PV I SYSTEM HYDRAULIC ANALYSIS Page 18 DATE: I SPRINKLER 9/4/2009SENT\C -2625 LIFE TECHNOLOGIES RACKS\CALCULATIONS\AREA B.SDF JOB TITLE: Area B I PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. \TEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) I Pipe: 172 -533.5 6.357 PL 10.00 PF 0.1 M16 30.8 0.0 33.2 0.0 5.4 120 FTG ---- PE 0.0 I M18 30.8 0.0 33.3 0.0 0.009 TL 10.00 PV Pipe: 173 -559.0 6.357 PL 10.00 PF 0.1 M18 30.8 0.0 33.3 0.0 5.7 120 FTG ---- PE 0.0 M20 30.8 0.0 33.4 0.0 0.010 TL 10.00 PV Pipe: 174 -581.1 6.357 PL 10.00 PF 0.1 30.8 0.0 33.4 0.0 5.9 120 FTG ---- PE 0.0 I M20 M22 30.8 0.0 33.5 0.0 0.010 TL 10.00 PV I M22 Pipe: 175 30.8 0.0 33.5 0.0 -599.7 6.1 6.357 120 PL FTG 10.00 ---- PF PE 0.1 0.0 M24 30.8 0.0 33.6 0.0 0.011 TL 10.00 PV 176 -614.9 6.357 PL 10.00 PF 0.1 I Pipe: M24 30.8 0.0 33.6 0.0 6.2 120 FTG ---- PE 0.0 M26 30.8 0.0 33.7 0.0 0.011 TL 10.00 PV I Pipe: 178 -626.6 6.357 PL 10.00 PF 0.1 M26 30.8 0.0 33.7 0.0 6.3 120 FTG ---- PE 0.0 M28 30.8 0.0 33.8 0.0 0.012 TL 10.00 PV I Pipe: 179 -634.2 6.357 PL 10.00 PF 0.1 M28 30.8 0.0 33.8 0.0 6.4 120 FTG ---- PE 0.0 I M30 30.8 0.0 33.9 0.0 0.012 TL 10.00 PV Pipe: 180 -632.1 6.357 PL 10.00 PF 0.1 M30 30.8 0.0 33.9 0.0 6.4 120 FTG ---- PE 0.0 I M32 30.8 0.0 34.0 0.0 0.012 TL 10.00 PV Pipe: 181 -623.7 6.357 PL 10.00 PF 0.1 30.8 0.0 34.0 0.0 6.3 120 FTG ---- PE 0.0 I M32 M34 30.8 0.0 34.2 0.0 0.012 TL 10.00 PV Pipe: 182 -611.2 6.357 PL 10.00 PF 0.1 M34 30.8 0.0 34.2 0.0 6.2 120 FTG ---- PE 0.0 M36 30.8 0.0 34.3 0.0 0.011 TL 10.00 PV I Pipe: 183 -595.3 6.357 PL 10.00 PF 0.1 M36 30.8 0.0 34.3 0.0 6.0 120 FTG ---- PE 0.0 M38 30.8 0.0 34.4 0.0 0.011 TL 10.00 PV I Pipe: 184 -575.9 6.357 PL 10.00 PF 0.1 M38 30.8 0.0 34.4 0.0 5.8 120 FTG ---- PE 0.0 M40 30.8 0.0 34.5 0.0 0.010 TL 10.00 PV I Pipe: 185 -553.2 6.357 PL 10.00 PF 0.1 M40 30.8 0.0 34.5 0.0 5.6 120 FTG ---- PE 0.0 M42 30.8 0.0 34.6 0.0 0.009 TL 10.00 PV I SYSTEM HYDRAULIC ANALYSIS Page 19 DATE: I SPRINKLER 9/4/2009SENT\C -2625 LIFE TECHNOLOGIES RACKS\CALCULATIONS\AREA B.SDF JOB TITLE: Area B I 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) I Pipe: 186 -526.8 6.357 PL 10.00 PP 0.1 M42 30.8 0.0 34.6 0.0 5.3 120 FTG ---- PE 0.0 I M44 30.8 0.0 34.7 0.0 0.009 TL 10.00 PV Pipe: 187 -496.6 6.357 PL 10.00 PF 0.1 M44 30.8 0.0 34.7 0.0 5.0 120 FTG ---- PE 0.0 M46 30.8 0.0 34.7 0.0 0.008 TL 10.00 PV Pipe: 189 -462.4 6.357 PL 10.00 PF 0.1 • M46 30.8 0.0 34.7 0.0 4.7 120 FTG ---- PE 0.0 M48 30.8 0.0 34.8 0.0 0.007 TL 10.00 PV Pipe: 190 -423.8 6.357 PL 10.00 PF 0.1 I M48 30.8 0.0 34.8 0.0 4.3 120 FTG ---- PE 0.0 • M50 30.8 0.0 34.9 0.0 0.006 TL 10.00 PV 191 -380.5 6.357 PL 10.00 PF 0.0 I Pipe: M50 30.8 0.0 34.9 0.0 3.8 120 FTG ---- PE 0.0 M52 30.8 0.0 34.9 0.0 0.005 TL 10.00 PV I Pipe: 192 -332.3 6.357 PL 10.00 PP 0.0 M52 30.8 0.0 34.9 0.0 3.4 120 FTG ---- PE 0.0 M54 30.8 0.0 34.9 0.0 0.004 TL 10.00 PV I Pipe: 193 -278.6 6.357 PL 10.00 PP 0.0 M54 30.8 0.0 34.9 0.0 2.8 120 FTG ---- PE 0.0 I M56 30.8 0.0 35.0 0.0 0.003 TL 10.00 PV Pipe: 194 -219.0 6.357 PL 10.00 PF 0.0 M56 30.8 0.0 35.0 0.0 2.2 120 FTG ---- PE 0.0 M58 30.8 0.0 35.0 0.0 0.002 TL 10.00 PV Pipe: 195 -153.1 6.357 PL 10.00 PF 0.0 30.8 0.0 35.0 0.0 1.5 120 FTG ---- PE 0.0 I M58 M60 30.8 0.0 35.0 0.0 0.001 TL 10.00 PV 196 -80.3 6.357 PL 10.00 PF 0.0 I Pipe: M60 30.8 0.0 35.0 0.0 0.8 120 FTG ---- PE 0.0 M62 30.8 0.0 35.0 0.0 0.000 TL 10.00 PV I Pipe: 197 -965.0 6.357 PL 18.58 PP 2.4 M61 30.8 0.0 44.5 0.0 9.8 120 FTG 2ET PE 0.0 TOR 30.8 0.0 46.9 0.0 0.026 TL 92.58 PV I Pipe: 198 -965.0 6.357 PL 27.75 PF 2.5 TOR 30.8 0.0 46.9 0.0 9.8 120 FTG ETB PE 12.0 G 3.0 0.0 61.4 0.0 0.026 TL 96.75 PV I Pipe: 198A -23.5 1.728 PL 5.00 PP 0.1 1 8.8 5.6 17.7 23.5 3.2 120 FTG ---- PE 0.0 2 8.8 5.6 17.7 23.6 0.015 TL 5.00 PV I SYSTEM HYDRAULIC ANALYSIS Page 20 DATE: I SPRINKLER 9/4/2009SENT\C -2625 LIFE TECHNOLOGIES RACKS\CALCULATIONS\AREA B.SDF JOB TITLE: Area B I 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) I Pipe: 198B -47.1 1.728 FL 10.00 PF 0.6 2 8.8 5.6 17.7 23.6 6.4 120 FTG ---- PE 0.0 ' 3 8.8 5.6 18.3 24.0 0.056 TL 10.00 PV Pipe: 198C -71.1 1.728 FL 10.00 PF 1.2 3 8.8 5.6 18.3 24.0 9.7 120 FTG ---- PE 0.0 4 8.8 5.6 19.5 24.7 0.119 TL 10.00 PV Pipe: 198D -95.8 1.728 FL 10.00 PF 2.1 5.6 19.5 24.7 13.1 120 FTG ---- PE 0.0 5 I 8.8 8.8 5.6 21.6 26.0 0.208 TL 10.00 FV Pipe: 198E -121.8 1.728 FL 3.00 PF 4.6 5 8.8 5.6 21.6 26.0 16.7 120 FTG T FE 0.0 A 8.8 0.0 26.2 0.0 0.324 TL 14.29 PV 198E1 -21.7 1.728 FL 6.50 PP 0.1 I Pipe: 6 16.5 5.6 15.0 21.7 3.0 120 FTG ---- PE 0.0 7 16.5 5.6 15.1 21.8 0.013 TL 6.50 PV I Pipe: 198F -43.4 1.728 FL 10.00 PP 0.5 7 16.5 5.6 15.1 21.8 5.9 120 FTG ---- FE 0.0 8 16.5 5.6 15.6 22.1 0.048 TL 10.00 PV I Pipe: 198G -65.5 1.728 FL 9.50 PF 1.0 8 16.5 5.6 15.6 22.1 9.0 120 FTG ---- FE 0.0 I 9 16.5 5.6 16.5 22.8 0.103 TL 9.50 PV Pipe: 198H -88.3 1.728 FL 10.00 PP 1.8 9 16.5 5.6 16.5 22.8 12.1 120 FTG ---- FE 0.0 10 16.5 5.6 18.3 24.0 0.179 TL 10.00 PV Pipe: 1981 -112.3 1.728 FL 5.00 PP 1.4 16.5 5.6 18.3 24.0 15.4 120 FTG ---- FE 0.0 I 10 11 16.5 0.0 19.7 0.0 0.279 TL 5.00 PV 198J -112.3 1.728 PL 0.50 PP 3.3 I Pipe: 11 16.5 0.0 19.7 0.0 15.4 120 FTG T PE 0.0 B 16.5 0.0 23.0 0.0 0.279 TL 11.79 PV I Pipe: 198K -121.8 3.314 FL 11.50 PP 0.2 A 8.8 0.0 26.2 0.0 4.5 120 FTG ---- PE -3.3 B 16.5 0.0 23.0 0.0 0.014 TL 11.50 PV I Pipe: 198L -234.1 3.314 FL 15.25 PP 2.1 B 16.5 0.0 23.0 0.0 8.7 120 FTG ET PE -5.8 I C30.0 0.0 19.3 0.0 0.045 TL 47.28 PV Pipe: 198N -234.1 3.314 FL 20.00 PP 1.4 C 30.0 0.0 19.3 0.0 8.7 120 FTG E FE 0.0 D 30.0 0.0 20.7 0.0 0.045 TL 30.19 PV I SYSTEM HYDRAULIC ANALYSIS Page 21 DATE: I SPRINKLER 9/4/2009SENT\C -2625 LIFE TECHNOLOGIES RACKS\CALCULATIONS\AREA B.SDF JOB TITLE: Area B I 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) I Pipe: 198N -234.1 3.314 PL 97.00 PF 5.9 D 30.0 0.0 20.7 0.0 8.7 120 FTG ET PE 0.0 I E 30.0 0.0 26.5 0.0 0.045 TL 129.03 PV Pipe: 1980 -234.1 3.314 PL 375.50 PF 21.5 E 30.0 0.0 26.5 0.0 8.7 120 FTG 6ETB PE 0.0 F 30.0 0.0 48.1 0.0 0.045 TL 473.05 PV Pipe: 1988 -234.1 3.314 PL 27.00 PF 1.7 30.0 0.0 48.1 0.0 8.7 120 FTG E PE 11.7 I F G 3.0 0.0 61.4 0.0 0.045 TL 37.19 PV I G Pipe: 198Q 3.0 0.0 61.4 -1199.1 0.0 12.1 6.357 120 PL FTG 4.50 2E PF PE 1.6 1.1 BOR 0.5 0.0 64.1 0.0 0.039 TL 40.50 PV 199 -1199.1 7.980 PL 10.00 PF 0.4 I Pipe: BOR 0.5 0.0 64.1 0.0 7.7 150 FTG 2L PE 1.5 DI -3.0 0.0 66.1 0.0 0.009 TL 50.00 PV I Pipe: 200 -1199.1 7.980 PL 40.00 PF 0.6 DI -3.0 0.0 66.1 0.0 7.7 150 FTG E PE 0.0 UG1 -3.0 0.0 66.6 0.0 0.009 TL 67.00 PV I Pipe: 201 -1199.1 7.980 PL 644.50 PP 6.0 UG1 -3.0 0.0 66.6 0.0 7.7 150 FTG T PE 0.0 I UG4 -3.0 0.0 72.6 0.0 0.009 TL 697.50 PV Pipe: 202 -1199.1 7.980 PL 25.50 PF 0.6 UG4 -3.0 0.0 72.6 0.0 7.7 150 FTG 2L PE 0.0 UGS -3.0 0.0 73.2 0.0 0.009 TL 65.50 PV Pipe: 203 -1199.1 8.390 PL 6.00 PP 0.4 UG5 -3.0 0.0 73.2 0.0 7.0 140 FTG 2L PS -2.6 I SF1 3.0 0.0 70.9 0.0 0.008 TL 50.00 PV Pipe: 204 FIXED PRESSURE LOSS DEVICE I BF2 3.0 0.0 78.9 0.0 8.0 psi, 1199.1 gpm BF1 3.0 0.0 70.9 0.0 I Pipe: 205 -1199.1 8.390 PL 6.00 PF 0.4 SF2 3.0 0.0 78.9 0.0 7.0 140 FTG 2L PE 2.6 UG6 -3.0 0.0 81.9 0.0 0.008 TL 50.00 PV I Pipe: 206 -1199.1 7.980 PL 16.83 PP 0.8 UG6 -3.0 0.0 81.9 0.0 7.7 150 FTG TL PE 0.0 UG7 -3.0 0.0 82.7 0.0 0.009 TL 89.83 PV I Pipe: 207 -1199.0 7.980 PL 126.00 PP 2.0 UG7 -3.0 0.0 82.7 0.0 7.7 150 FTG 2ETG PS -1.3 SRC 0.0 SRCE 83.4 (N/A) 0.009 TL 239.00 PV P1 Li I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 22 DATE: 9/4/2009SENT\C -2625 LIFE TECHNOLOGIES RACKS\CALCULATIONS\AREA B.SDF JOB TITLE: Area B NOTES (HASS) I (1) Calculations were performed by the HASS 8.0 computer program under license no. 50040828 granted by HRS Systems, Inc. I 208 South Public Square Petersburg, TN 37144 (2) The system has been calculated to provide an average I imbalance at each node of 0.001 gpm and a maximum imbalance at any node of 0.194 gpm. I (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 19.9 ft/sec at pipe 164. l (4) a. System remote area HAS been proven or 'peaked'. b. Minimum pressure at any sprinkler: 17.655 psi I c. Minimum pressure with remote area shifted one sprinkler space toward left cross main: 17.678 psi d. Remote area is located adjacent to right cross main (5) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: * MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet ' (in) B T L C B G A D N Eli Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPVlv NPTee 1.728 5.64 11.29 2.82 12.70 8.47 1.41 14.11 14.11 11.29 3.314 10.19 21.84 7.28 23.29 14.56 1.46 18.93 18.93 21.84 PAGE: B MATERIAL: THNWL HWC: 120 Diameter Equivalent Fitting Lengths in Feet B T L C B G A D N (in) Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPV1v NPTee 2.157 6.00 12.00 3.00 14.00 8.00 1.00 12.00 12.00 12.00 4.260 13.00 26.00 8.00 29.00 16.00 3.00 26.00 26.00 26.00 6.357 18.00 38.00 11.00 40.00 13.00 4.00 35.00 35.00 38.00 I ri I I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 23 DATE: 9/4/2009SENT\C -2625 LIFE TECHNOLOGIES RACKS\CALCULATIONS\AREA B.SDF JOB TITLE: Area B I PAGE: D Diameter (in) 8.390 I PAGE: E Diameter (in) 7.980 I Li I I I I Li I I I I I I I MATERIAL: DIRON HWC: 140 Equivalent Fitting Lengths in Feet E T L C B G N Ell Tee LngEll ChkVlv BfyVlv GatVlv NPTee 31.00 59.00 22.00 76.00 20.00 7.00 59.00 MATERIAL: PVC150 HWC: 150 Equivalent Fitting Lengths in Feet E T L C B G N Eli Tee LngEll ChkVlv BfyVlv GatVlv NPTee 27.00 53.00 20.00 68.00 18.00 6.00 53.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 24 0 0 o 0 0 -1 0 C) QQ CD 0 IT 0 0 0 0 0 0 0 • • ••• • 0 0 0 0 0• 0 0 (N 0 0 (N I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 25 DATE: 9/4/2009SENT\C -2625 LIFE TECHNOLOGIES RACKS \CALCULAT IONS \AREA P,.SDF JOB TITLE: Area B WATER SUPPLY CURVE 120+ I I 110+ \\\\\ \\\\\ \\\\\ I * <-102.6 psi @ 1060 gpm 100+ Flow Test Point I 0 I P 80+ R I I EI S I 5 70+ I UI R I E 60+ I (I P I 150+ I 40+ 30+ 20+-. = = = = = = = = = = LEGEND= = = = = = = = = = = IT I x = Required Water Supply IF I 83.44 psi @ 1699.0 gprn if 10+ if I I 0 = Available Water Supply U I 90.06 psi @ 1699.0 gpm IT I 0++---------------------------------------------------------------- ---+----+-----+------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) I I WESTERN FIRE PROTECTION, INC. DENSITY UPGRADE 13630 DANIELSON STREET POWAY,CA 92064 HYDRAULIC CALCULATIONS FOR LIFE TECHNOLOGIES 5781 VAN ALLEN WAY CARLSBAD CA 92008 FILE NUMBER: DATE: SEP 4, 2009 -DESIGN DATA- OCCUPANCY CLASSIFICATION: EXTRA HAZARD GRP I DENSITY: 0.30 GPM PER SQ.FT. AREA OF APPLICATION: 1545 SQ.FT. ENTIRE AREA COVERAGE PER SPRINKLER: 80 SQ. FT. MAX NUMBER OF SPRINKLERS CALCULATED: 25 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 691.8 gprn TOTAL WATER REQUIRED (including hose) : 1191.8 gpm FLOW AND PRESSURE (8 BOR): 691.8 GPM 8 53.9 PSI SPRINKLER K-FACTOR: 8.1 K NAME OF CONTRACTOR: WESTERN FIRE PROTECTION DESIGN/LAYOUT BY: G.Ruiz AUTHORITY HAVING JURISDICTION: CARLSBAD FIRE DEPT. CONTRACTOR CERTIFICATION NUMBER: CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE # 50040828 HRS SYSTEMS, INC. TUCKER, GA 30084 TUCKER, GA 30084 I I I I I I I I I I I I I I I I I I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 I DATE: 9/4/2009IFE TECHNOLOGIES RACKS\CALCULATIONS\DENSITY UPGRADE-REV.SDF JOB TITLE: Density Upgrade Area C WATER SUPPLY DATA SOURCE STATIC NODE TAG PRESS. (PSI) SRC 111.6 I RESID. FLOW PRESS. @ (PSI) (GPM) 102.6 1060.0 AVAIL. TOTAL REQ'D PRESS. @ DEMAND PRESS. (PSI) (GPM) (PSI) 100.4 1191.8 66.1 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 1191.8 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 500.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 691.8 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE I (FT) (PSI) (GPM) Si 11.0 K= 8.10 9.1 24.4 S2 11.0 K= 8.10 9.4 24.8 I S3 11.0 K= 8.10 10.5 26.2 S4 11.0 K= 8.10 13.0 29.2 S5 11.0 K= 8.10 17.5 33.9 11.0 K= 8.10 9.0 24.3 I S6 S7 11.0 K= 8.10 9.3 24.7 S8 11.0 K= 8.10 10.4 26.1 11.0 K= 8.10 12.8 28.9 I S9 S1O 11.0 K= 8.10 17.1 33.5 Sli 11.0 K= 8.10 9.0 24.3 S12 11.0 K= 8.10 9.3 24.7 110 K= 8.10 10.3 26.0 I S13 S14 11.0 K= 8.10 12.6 28.8 S15 11.0 K= 8.10 16.9 33.3 11.0 K= 8.10 9.2 24.5 I S16 S17 11.0 K= 8.10 9.5 24.9 S18 11.0 K= 8.10 10.6 26.3 S19 11.0 K= 8.10 13.0 29.2 I S20 11.0 K= 8.10 17.4 33.8 S21 11.0 K= 8.10 9.3 24.7 S22 11.0 K= 8.10 9.6 25.1 11.0 K= 8.10 10.7 26.5 I S23 S24 11.0 K= 8.10 13.2 29.4 S25 11.0 K= 8.10 17.7 34.1 I A B 12.5 12.5 - - - - - - - - 10.1 10.5 - - - - - - C 12.5 - - - - 11.8 - - - D 12.5 - - - - 14.7 - - - • E 12.5 - - - - 20.0 - - - • F 12.5 - - - - 10.4 - - - G 12.5 - - - - 10.8 - - - • H 12.5 - - - - 12.1 - - - I 12.5 - - - - 14.9 - - - I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 I DATE: 9/4/20091FE TECHNOLOGIES RACKS\CALCULATIONS\DENSITY UPGRADE-REV.SDF JOB TITLE: Density Upgrade Area C NODE TYPE PRESSURE DISCHARGE (PSI) (GPM) - - - 20.2 - - - - - - - 10.7 - - - - - - - 12.4 - - - - - - - 15.2 - - - - - - - 20.5 - - - - - - - 10.6 - - - - - - - 11.0 - - - - - - - 12.3 - - - - - - - 15.2 - - - - - - - 20.5 - - - - - - 10.5 - - - - - - - 10.9 - - - - - - - 12.2 - - - - - - - 15.2 - - - - - - - 20.6 - - - - - - - 29.7 - - - - - - - 29.8 - - - - - - - 30.0 - - - - - - - 30.3 - - - - - - - 30.5 - - - - - - - 32.5 - - - - - - - 30.3 - - - - - - - 27.7 - - - - - - - 27.8 - - - - - - - 28.0 - - - - - - 28.3 - - - - - - - 28.4 - - - - - - - 31.3 - - - - - - - 30.2 - - - - - - - 31.3 - - - - - - - 30.2 - - - - - - - 31.3 - - - - - - - 30.2 - - - - - - - 31.3 - - - - - - - 30.2 - - - - - - - 31.4 - - - - - - - 30.1 - - - - - - - 31.4 - - - - - - - 30.1 - - - - - - - 31.5 - - - - - - - 30.0 - - - - - - - 31.6 - - - - - - - 30.4 - - - - - - 31.7 - - - - - - - 30.9 - - - - - - - 31.9 - - - - - - - 31.3 - - - - - - - 32.1 - - - - - - - 31.7 - - - - - - - 32.3 - - - - - - - 32.0 - - - NODE ANALYSIS DATA I NODE TAG ELEVATION (PT) I - J 12.5 K 12.5 L 12.5 I M 12.5 N 12.5 0 12.5 P 12.5 I Q 12.5 R 12.5 12.5 I 5 T 12.5 U 12.5 V 12.5 I W 12.5 • x 12.5 Y 12.5 I Ml M2 12.5 12.5 M3 12.5 M4 12.5 I MS 12.5 M5A 12.5 M6 30.8 Ti 13.0 I T2 13.0 T3 13.0 T4 13.0 I - TS 13.0 Ri 31.8 R2 31.8 R3 31.8 I R4 31.8 RS 31.8 I R6 R7 31.8 31.8 R8 31.8 R9 31.8 I RiO 31.8 R11. 31.8 R12 31.8 R13 31.8 I R14 31.8 R15 31.8 R16 31.8 I R17 31.8 R18 31.8 R19 31.8 R20 31.8 I R21 31.8 R22 31.8 I R23 R24 31.8 31.8 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 9/4/20091FE TECHNOLOGIES RACKS\CALCULATIONS\DENSITY UPGRADE-REV.SDF JOB TITLE: Density Upgrade Area C I NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (PT) (PSI) (GPM) R25 31.8 - - - - 32.5 - - - R26 31.8 - - - - 32.4 - - - R27 31.8 - - - - 32.8 - - - I R28 31.8 - - - - 32.7 - - - R29 31.8 - - - - 33.0 - - - R30 31.8 - - - - 33.0 - - - I R31 31.8 - - - - 33.2 - - - R32 31.8 - - - - 33.3 - - - R33 31.8 - - - - 33.5 - - - I R34 31.8 - - - - 33.6 - - - R35 31.8 - - - - 33.7 - - - R36 31.8 - - - - 34.0 - - - R37 31.8 - - - - 33.9 - - - I R38 31.8 - - - - 34.3 - - - R39 31.8 - - - - 34.1 - - - R40 31.8 - - - - 34.7 - - - I R41 31.8 - - - - 34.3 - - - R42 31.8 - - - - 35.1 - - - R43 31.8 - - - - 34.4 - - - R44 31.8 - - - - 35.2 - - - I R45 31.8 - - - - 34.5 - - - R46 31.8 - - - - 35.3 - - - R47 31.8 - - - - 34.7 - - - I R48 31.8 - - - - 35.4 - - - R49 31.8 - - - - 34.8 - - - R50 31.8 - - - 35.5 - - - R51 31.8 - - - - 34.8 - - - I R52 31.8 - - - - 35.6 - - - R53 31.8 - - - - 34.9 - - - R54 31.8 - - - - 35.7 - - - I R55 31.8 - - - - 34.9 - - - R56 31.8 - - - - 35.8 - - - R57 31.8 - - - - 35.0 - - - I R58 31.8 - - - 35.9 - - - R59 31.8 - - - - 35.0 - - - R60 31.8 - - - - 36.0 - - - R61 31.8 - - - - 35.0 - - - I R62 31.8 - - - - 36.1 - - - 1 30.8 - - - - 31.8 - - 2 30.8 - - - - 30.5 - - - I 3 30.8 - - - - 31.8 - - - 4 30.8 - - - - 30.5 - - - 5 30.8 - - - - 31.8 - - - I 6 30.8 - - - - 30.5 - - - 7 30.8 - - - - 31.9 - - - 8 30.8 - - - - 30.5 - - - 9 30.8 - - - - 31.9 - - - I 10 30.8 - - - - 30.5 - - - 11 30.8 - - - - 31.9 - - - 12 30.8 - - - - 30.4 - - - I 13 30.8 - - - - 32.0 - - - 14 30.8 - - - - 30.4 - - - I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 9/4/20091FE TECHNOLOGIES RACKS\CALCULATIONS\DENSITY UPGRADE-REV.SDF JOB TITLE: Density Upgrade Area C I NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 15 30.8 - - - 32.1 - - - 16 30.8 - - - - 30.8 - - 17 30.8 - - - - 32.2 - - - I 18 30.8 - - - - 31.2 - - - 19 30.8 - - - - 32.4 - - - 20 30.8 - - - - 31.7 - - - I 21 30.8 - - - - 32.6 - - - 22 30.8 - - - - 32.1 - - - 23 30.8 - - - 32.8 - - - I 24 30.8 - - - - 32.4 - - - 25 30.8 - - - - 33.0 - - - 26 30.8 - - - 32.8 - - 27 30.8 - - - - 33.2 - - - I 28 30.8 - - - - 33.1 - - - 29 30.8 - - - - 33.4 - - - 30 30.8 - - - - 33.4 - - - I 31 30.8 - - - - 33.7 - - - 32 30.8 - - - - 33.8 - - 33 30.8 - - - - 33.9 - - - 34 30.8 - - - - 34.1 - - - I 35 30.8 - - - - 34.1 - - - 36 30.8 - - - - 34.4 - - - 37 30.8 - - - - 34.3 - - - I 38 30.8 - - - - 34.8 - - - 39 30.8 - - - - 34.5 - - - 40 30.8 - - - - 35.2 - - - I 41 30.8 - - - - 34.7 - - - 42 30.8 - - - - 35.6 - - - 42A 30.8 - - - - 35.7 - - - 43 30.8 - - - - 34.8 - - - I 44 30.8 - - - - 35.7 - - - 45 30.8 - - - - 34.9 - - - 46 30.8 - - - - 35.8 - - - I 47 30.8 - - - - 35.1 - - - 48 30.8 - - - - 35.9 - - - 49 30.8 - - - - 35.2 - - - I 50 30.8 - - - - 36.0 - - - 51 30.8 - - - - 35.2 - - - 52 30.8 - - - - 36.1 - - - 53 30.8 - - - - 35.3 - - - I 54 30.8 - - - - 36.1 - - - 55 30.8 - - - - 35.3 - - - 56 30.8 - - - - 36.3 - - I 57 30.8 - - - - 35.3 - - - 58 30.8 - - - - 36.4 - - - 59 30.8 - - - - 35.3 - - - 60 30.8 - - - - 36.5 - - - I 61 30.8 - - - - 35.3 - - - 62 30.8 - - - - 36.6 - - - TOR 30.8 - - - - 38.0 - - - I BOR 0.5 - - - - 53.9 DI -3.0 - - - - 55.5 - - - I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 9/4/20091FE TECHNOLOGIES RACKS\CALCULATIONS\DENSITY UPGRADE-REV.SDF JOB TITLE: Density Upgrade Area C ELEVATI ON NODE TYPE PRESSURE DISCHARGE (PSI) (GPM) - - - 55.8 - - - - - - - 55.8 - - - - - - - 56.5 - - - - - - - 58.0 - - - - - - - 58.2 - - - - - - - 66.4 - - - - - - - 66.7 - - - - - - - 55.7 - - - - - - - 63.7 - - - 0.0 SOURCE 66.1 691.8 I d L- I I I I I I I NODE ANALYSIS DATA I I NODE TAG (FT) I - UG -3.0 UG1 -3.0 UG2 -3.0 I UG4 -3.0 UG5 -3.0 UG6 -3.0 UG7 -3.0 I BFI 3.0 BF2 3.0 SRC I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 9/4/20091FE TECHNOLOGIES RACKS\CALCULATIONS\DENSITY UPGRADE-REV.SDF JOB TITLE: Density Upgrade Area C PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. I END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 1 -24.4 1.080 PL 2.50 PF 1.7 I 51 11.0 8.1 9.1 24.4 8.5 120 FTG ET PE -0.6 A 12.5 0.0 10.1 0.0 0.163 TL 10.57 PV I Pipe: 2 -24.8 1.080 PL 2.50 PF 1.8 S2 11.0 8.1 9.4 24.8 8.7 120 FTG ET PE -0.6 B 12.5 0.0 10.5 0.0 0.168 TL 10.57 PV I Pipe: 3 -26.2 1.080 PL 2.50 PF 2.0 - S3 11.0 8.1 10.5 26.2 9.2 120 FTG ET PE -0.6 I C12.5 0.0 11.8 0.0 0.187 TL 10.57 PV Pipe: 4 -29.2 1.080 PL 2.50 PF 2.4 S4 11.0 8.1 13.0 29.2 10.2 120 FTG ET PE -0.6 I D12.5 0.0 14.7 0.0 0.227 TL 10.57 PV Pipe: 5 -33.9 1.080 PL 2.50 PF 3.2 S5 11.0 8.1 17.5 33.9 11.9 120 FTG ET PE -0.6 E 12.5 0.0 20.0 0.0 0.299 TL 10.57 PV Pipe: 6 -24.3 1.080 PL 4.50 PF 2.0 I S6 11.0 8.1 9.0 24.3 8.5 120 FTG ET PE -0.6 F 12.5 0.0 10.4 0.0 0.162 TL 12.57 PV Pipe: 7 -24.7 1.080 PL 4.50 PF 2.1 S7 11.0 8.1 9.3 24.7 8.7 120 FTG ET PE -0.6 G 12.5 0.0 10.8 0.0 0.167 TL 12.57 PV I Pipe: 8 -26.1 1.080 PL 4.50 PF 2.3 R S8 11.0 8.1 10.4 26.1 9.1 120 FTG ET PE -0.6 H 12.5 0.0 12.1 0.0 0.185 TL 12.57 PV I Pipe: 9 -28.9 1.080 PL 4.50 PF 2.8 S9 11.0 8.1 12.8 28.9 10.1 120 FTG ET PE -0.6 I I12.5 0.0 14.9 0.0 0.224 TL 12.57 PV Pipe: 10 -33.5 1.080 FL 4.50 PF 3.7 S1O 11.0 8.1 17.1 33.5 11.7 120 FTG ET PE -0.6 I J 12.5 0.0 20.2 0.0 0.294 TL 12.57 PV Pipe: 11 -24.3 1.080 PL 6.50 PF 2.4 I Sli 11.0 8.1 9.0 24.3 8.5 120 FTG ET PE -0.6 K 12.5 0.0 10.7 0.0 0.162 TL 14.57 PV Pipe: 12 -24.7 1.080 PL 6.50 PF 2.4 I S12 11.0 8.1 9.3 24.7 8.6 120 FTG ET PE -0.6 L 12.5 0.0 11.1 0.0 0.167 TL 14.57 PV I I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 9/4/2009IFE TECHNOLOGIES RACKS\CALCULATIONS\DENSITY UPGRADE-REV.SDF JOB TITLE: Density Upgrade Area C I 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) I Pipe: 13 -26.0 1.080 PL 6.50 PF 2.7 S13 11.0 8.1 10.3 26.0 9.1 120 FTG ET PE -0.6 I M 12.5 0.0 12.4 0.0 0.184 TL 14.57 PV Pipe: 14 -28.8 1.080 PL 6.50 PF 3.2 S14 11.0 8.1 12.6 28.8 10.1 120 FTG ET PE -0.6 I N12.5 0.0 15.2 0.0 0.222 TL 14.57 PV Pipe: 15 -33.3 1.080 PL 6.50 PF 4.2 S15 11.0 8.1 16.9 33.3 11.7 120 FTG ET PE -0.6 I 0 12.5 0.0 20.5 0.0 0.290 TL 14.57 PV Pipe: 16 -24.5 1.080 PL 4.50 PF 2.1 I S16 11.0 8.1 9.2 24.5 8.6 120 FTG ET PE -0.6 P 12.5 0.0 10.6 0.0 0.165 TL 12.57 PV Pipe: 17 -24.9 1.080 PL 4.50 PF 2.1 S17 11.0 8.1 9.5 24.9 8.7 120 FTG ET PE -0.6 Q 12.5 0.0 11.0 0.0 0.170 TL 12.57 PV I Pipe: 18 -26.3 1.080 PL 4.50 PF 2.4 S18 11.0 8.1 10.6 26.3 9.2 120 FTG ET PE -0.6 R 12.5 0.0 12.3 0.0 0.188 TL 12.57 PV I Pipe: 19 -29.2 1.080 PL 4.50 PF 2.9 S19 11.0 8.1 13.0 29.2 10.2 120 FTG ET PE -0.6 I S12.5 0.0 15.2 0.0 0.227 TL 12.57 PV Pipe: 20 -33.8 1.080 PL 4.50 PF 3.7 S20 11.0 8.1 17.4 33.8 11.8 120 FTG ET PE -0.6 I T12.5 0.0 20.5 0.0 0.298 TL 12.57 PV Pipe: 21 -24.7 1.080 PL 3.50 PF 1.9 I S21 11.0 8.1 9.3 24.7 8.6 120 FTG ET PE -0.6 U 12.5 0.0 10.5 0.0 0.166 TL 11.57 PV Pipe: 22 -25.1 1.080 PL 3.50 PF 2.0 I S22 11.0 8.1 9.6 25.1 8.8 120 FTG ET PS -0.6 '1 12.5 0.0 10.9 0.0 0.171 TL 11.57 PV Pipe: 23 -26.5 1.080 PL 3.50 PF 2.2 S23 11.0 8.1 10.7 26.5 9.3 120 FTG ET PE -0.6 W 12.5 0.0 12.2 0.0 0.190 TL 11.57 PV I Pipe: 24 -29.4 1.080 PL 3.50 PF 2.7 S24 11.0 8.1 13.2 29.4 10.3 120 FTG ET PE -0.6 X 12.5 0.0 15.2 0.0 0.230 TL 11.57 PV Pipe: 25 -34.1 1.080 PL 3.50 PF 3.5 S25 11.0 8.1 17.7 34.1 11.9 120 FTG ET PE -0.6 Y 12.5 0.0 20.6 0.0 0.303 TL 11.57 PV I DATE: 9/4/20091FE SPRINKLER SYSTEM HYDRAULIC ANALYSIS TECHNOLOGIES RACKS\CALCULATIONS\DENSITY UPGRADE-REV.SDF Page 9 JOB TITLE: Density Upgrade Area C I 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) I Pipe: 26 -24.4 1.408 PL 8.00 PF 0.4 A 12.5 0.0 10.1 0.0 5.0 120 FTG ---- FE 0.0 B 12.5 0.0 10.5 0.0 0.045 TL 8.00 PV I Pipe: 27 -49.2 1.408 PL 8.00 PF 1.3 B 12.5 0.0 10.5 0.0 10.1 120 FTG ---- FE 0.0 I C12.5 0.0 11.8 0.0 0.164 TL 8.00 PV Pipe: 28 -75.5 1.408 PL 8.00 PF 2.9 I C D 12.5 12.5 0.0 0.0 11.8 14.7 0.0 0.0 15.5 120 0.362 FTG TL ---- 8.00 FE PV 0.0 Pipe: 29 -104.6 1.408 PL 8.00 PF 5.3 I D 12.5 0.0 14.7 0.0 21.6 120 FTG ---- PE 0.0 E 12.5 0.0 20.0 0.0 0.663 TL 8.00 PV Pipe: 30 -138.5 1.408 PL 0.50 PF 7.9 E 12.5 0.0 20.0 0.0 28.5 120 FTG T PE -0.2 Ti 13.0 0.0 27.7 0.0 1.113 TL 7.12 PV I Pipe: 31 -24.3 1.408 PL 8.00 PF 0.4 • F 12.5 0.0 10.4 0.0 5.0 120 FTG ---- FE 0.0 G 12.5 0.0 10.8 0.0 0.045 TL 8.00 PV I Pipe: 32 -49.0 1.408 FL 8.00 PF 1.3 G 12.5 0.0 10.8 0.0 10.1 120 FTG ---- FE 0.0 I H 12.5 0.0 12.1 0.0 0.163 TL 8.00 PV Pipe: 33 -75.1 1.408 PL 8.00 PF 2.9 H 12.5 0.0 12.1 0.0 15.5 120 FTG ---- FE 0.0 I I 12.5 0.0 14.9 0.0 0.359 TL 8.00 PV Pipe: 34 -104.1 1.408 PL 8.00 PF 5.3 0.0 14.9 0.0 21.4 120 FTG ---- PE 0.0 J I I12.5 12.5 0.0 20.2 0.0 0.656 TL 8.00 PV - Pipe: 35 -137.6 1.408 FL 0.50 PF 7.8 I 12.5 0.0 20.2 0.0 28.4 120 FTG T FE -0.2 T2 13.0 0.0 27.8 0.0 1.100 TL 7.12 PV I Pipe: 36 -24.3 1.408 FL 8.00 PF 0.4 K 12.5 0.0 10.7 0.0 5.0 120 FTG ---- FE 0.0 L 12.5 0.0 11.1 0.0 0.044 TL 8.00 PV I Pipe: 37 -49.0 1.408 FL 8.00 PF 1.3 - L 12.5 0.0 11.1 0.0 10.1 120 FTG ---- FE 0.0 M 12.5 0.0 12.4 0.0 0.163 TL 8.00 PV I Pipe: 38 -75.0 1.408 FL 8.00 PF 2.9 M 12.5 0.0 12.4 0.0 15.5 120 FTG ---- FE 0.0 N 12.5 0.0 15.2 0.0 0.358 TL 8.00 PV I DATE: I SPRINKLER 9/4/20091FE SYSTEM HYDRAULIC ANALYSIS TECHNOLOGIES RACKS\CALCULATIONS\DENSITY UPGRADE-REV.SDF Page 10 JOB TITLE: Density Upgrade Area C I 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) I Pipe: 39 -103.8 1.408 PL 8.00 PF 5.2 N 12.5 0.0 15.2 0.0 21.4 120 FTG ---- PE 0.0 O 12.5 0.0 20.5 0.0 0.653 TL 8.00 PV U Pipe: 40 -137.1 1.408 PL 0.50 PF 7.8 O 12.5 0.0 20.5 0.0 28.3 120 FTG T PE -0.2 T3 13.0 0.0 28.0 0.0 1.093 TL 7.12 PV Pipe: 41 -24.5 1.408 FL 8.00 PF 0.4 P 12.5 12.5 0.0 0.0 10.6 11.0 0.0 0.0 5.1 120 0.045 FTG TL ---- 8.00 PE Pv 0.0 I Q Pipe: 42 -49.5 1.408 FL 8.00 PF 1.3 I 12.5 0.0 11.0 0.0 10.2 120 FTG ---- PE 0.0 R 12.5 0.0 12.3 0.0 0.166 TL 8.00 PV • Pipe: 43 -75.8 1.408 PL 8.00 PF 2.9 R 12.5 0.0 12.3 0.0 15.6 120 FTG ---- PE 0.0 5 12.5 0.0 15.2 0.0 0.365 TL 8.00 PV I Pipe: 44 -105.0 1.408 PL 8.00 PF 5.3 • 5 12.5 0.0 15.2 0.0 21.6 120 FTG ---- PE 0.0 T 12.5 0.0 20.5 0.0 0.667 TL 8.00 PV I Pipe: 45 -138.8 1.408 PL 0.50 PF 8.0 T 12.5 0.0 20.5 0.0 28.6 120 FTG T FE -0.2 I T4 13.0 0.0 28.3 0.0 1.118 TL 7.12 PV Pipe: 46 -24.7 1.408 PL 8.00 PF 0.4 U 12.5 0.0 10.5 0.0 5.1 120 FTG ---- FE 0.0 V 12.5 0.0 10.9 0.0 0.046 TL 8.00 PV Pipe: 47 -49.7 1.408 PL 8.00 PF 1.3 0.0 10.9 0.0 10.2 120 FTG ---- PE 0.0 W I v12.5 12.5 0.0 12.2 0.0 0.167 TL 8.00 PV Pipe: 48 -76.2 1.408 PL 8.00 PF 3.0 I 12.5 0.0 12.2 0.0 15.7 120 FTG ---- PE 0.0 x 12.5 0.0 15.2 0.0 0.369 TL 8.00 Pv • Pipe: 49 -105.6 1.408 PL 8.00 PF 5.4 I x 12.5 0.0 15.2 0.0 21.8 120 FTG ---- PE 0.0 Y 12.5 0.0 20.6 0.0 0.674 TL 8.00 Pv 1 Pipe: 50 -139.7 1.408 FL 0.50 PF 8.1 Y 12.5 0.0 20.6 0.0 28.8 120 FTG T FE -0.2 T5 13.0 0.0 28.4 0.0 1.132 TL 7.12 Pv I Pipe: 51 -138.5 2.203 FL 0.50 PF 1.8 Ti 13.0 0.0 27.7 0.0 11.7 120 FTG IT FE 0.2 Ml 12.5 0.0 29.7 0.0 0.126 TL 14.14 PV P 'DATE: 9/4/20091FE SPRINKLER SYSTEM HYDRAULIC ANALYSIS TECHNOLOGIES RACKS\CALCULATIONS\DENSITY UPGRADE-REV.SDF Page 11 JOE TITLE: Density Upgrade Area C I 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) I Pipe: 52 -137.6 2.203 PL 0.50 PF 1.8 - T2 13.0 0.0 27.8 0.0 11.6 120 FTG T PE 0.2 M2 12.5 0.0 29.8 0.0 0.124 TL 14.14 PV I Pipe: 53 -137.1 2.203 PL 0.50 PF 1.7 T3 13.0 0.0 28.0 0.0 11.5 120 FTG T PE 0.2 I M3 12.5 0.0 30.0 0.0 0.124 TL 14.14 PV Pipe: 54 -138.8 2.203 PL 0.50 PF 1.8 T4 M4 13.0 12.5 0.0 0.0 28.3 30.3 0.0 0.0 11.7 120 0.126 FTG TL T 14.14 PE PV 0.2 Pipe: 54A -139.7 2.203 PL 0.50 PF 1.8 I T5 13.0 0.0 28.4 0.0 11.8 120 FTG T PE 0.2 MS 12.5 0.0 30.5 0.0 0.128 TL 14.14 PV 55 -138.5 4.310 PL 12.00 PF 0.1 I Pipe: Ml 12.5 0.0 29.7 0.0 3.0 120 FTG ---- PE 0.0 M2 12.5 0.0 29.8 0.0 0.005 TL 12.00 PV I Pipe: 56 -276.1 4.310 PL 12.00 PF 0.2 M2 12.5 0.0 29.8 0.0 6.1 120 FTG ---- PE 0.0 M3 12.5 0.0 30.0 0.0 0.017 TL 12.00 PV Pipe: 57 -413.3 4.310 PL 8.00 PF 0.3 M3 12.5 0.0 30.0 0.0 9.1 120 FTG ---- PE 0.0 I M4 12.5 0.0 30.3 0.0 0.036 TL 8.00 PV Pipe: 58 -552.0 4.310 PL 3.00 PF 0.2 M4 12.5 0.0 30.3 0.0 12.1 120 FTG ---- PE 0.0 MS 12.5 0.0 30.5 0.0 0.062 TL 3.00 PV Pipe: 58A -691.8 4.310 PL 8.00 PF 2.1 12.5 0.0 30.5 0.0 15.2 120 FTG E PE 0.0 I M5 MSA 12.5 0.0 32.5 0.0 0.094 TL 21.94 PV Pipe: 59 -691.8 4.310 PL 19.25 PF 5.7 I M5A 12.5 0.0 32.5 0.0 15.2 120 FTG ET PE -7.9 M6 30.8 0.0 30.3 0.0 0.094 TL 61.06 PV 60 27.2 2.157 PL 136.33 PF 1.1 I Pipe: Ri 31.8 0.0 31.3 0.0 2.4 120 FTG 2T PE 0.0 R2 31.8 0.0 30.2 0.0 0.007 TL 160.33 PV Pipe: 61 27.3 2.157 PL 136.33 PF 1.1 R3 31.8 0.0 31.3 0.0 2.4 120 FTG 2T PE 0.0 R4 31.8 0.0 30.2 0.0 0.007 TL 160.33 PV I Pipe: 62 27.5 2.157 PL 136.33 PF 1.1 RS 31.8 0.0 31.3 0.0 2.4 120 FTG 2T PE 0.0 R6 31.8 0.0 30.2 0.0 0.007 TL 160.33 PV I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 I DATE: 9/4/20091FE TECHNOLOGIES RACKS\CALCULATIONS\DENSITY UPGRADE-REV.SDF JOB TITLE: Density Upgrade Area C PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. I END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) I Pipe: 63 27.9 2.157 PL 136.33 PF 1.2 R7 31.8 0.0 31.3 0.0 2.4 120 FTG 2T PE 0.0 R8 31.8 0.0 30.2 0.0 0.007 TL 160.33 PV I Pipe: 64 28.6 2.157 PL 136.33 PF 1.2 R9 31.8 0.0 31.4 0.0 2.5 120 FTG 2T PE 0.0 I RiO 31.8 0.0 30.1 0.0 0.008 TL 160.33 PV Pipe: 65 29.7 2.157 PL 136.33 PF 1.3 Rll 31.8 0.0 31.4 0.0 2.6 120 FTG 2T PE 0.0 R12 31.8 0.0 30.1 0.0 0.008 TL 160.33 PV Pipe: 66 31.2 2.157 PL 136.33 PF 1.4 31.8 0.0 31.5 0.0 2.7 120 FTG 2T PE 0.0 I R13 R14 31.8 0.0 30.0 0.0 0.009 TL 160.33 PV 67 28.0 2.157 PL 136.33 PF 1.2 I Pipe: R15 31.8 0.0 31.6 0.0 2.5 120 FTG 2T PE 0.0 R16 31.8 0.0 30.4 0.0 0.007 TL 160.33 PV I Pipe: 68 23.8 2.157 PL 136.33 PF 0.9 R17 31.8 0.0 31.7 0.0 2.1 120 FTG 2T PE 0.0 R18 31.8 0.0 30.9 0.0 0.005 TL 160.33 PV Pipe: 69 19.9 2.157 PL 136.33 PF 0.6 R19 31.8 0.0 31.9 0.0 1.8 120 FTG 2T PE 0.0 R20 31.8 0.0 31.3 0.0 0.004 TL 160.33 PV I Pipe: 70 16.4 2.157 PL 136.33 PF 0.4 R21 31.8 0.0 32.1 0.0 1.4 120 FTG 2T PE 0.0 R22 31.8 0.0 31.7 0.0 0.003 TL 160.33 pv Pipe: 71 13.0 2.157 PL 136.33 PF 0.3 I R23 R24 31.8 31.8 0.0 0.0 32.3 32.0 0.0 0.0 1.1 120 0.002 FTG TL 2T 160.33 PE PV 0.0 Pipe: 72 9.8 2.157 PL 136.33 PF 0.2 I R25 31.8 0.0 32.5 0.0 0.9 120 FTG 2T PE 0.0 R26 31.8 0.0 32.4 0.0 0.001 TL 160.33 PV • Pipe: 73 6.5 2.157 PL 136.33 PF 0.1 R27 31.8 0.0 32.8 0.0 0.6 120 FTG 2T PE 0.0 R28 31.8 0.0 32.7 0.0 0.000 TL 160.33 PV I Pipe: 74 1.3 2.157 PL 136.33 PF 0.0 • R29 31.8 0.0 33.0 0.0 0.1 120 FTG 2T PE 0.0 R30 31.8 0.0 33.0 0.0 0.000 TL 160.33 PV I Pipe: 75 -6.0 2.157 PL 136.33 PF 0.1 R31 31.8 0.0 33.2 0.0 0.5 120 FTG 2T PE 0.0 R32 31.8 0.0 33.3 0.0 0.000 TL 160.33 PV I I DATE: 9/4/20091FE SPRINKLER SYSTEM HYDRAULIC ANALYSIS TECHNOLOGIES RACKS\CALCULATIONS\DENSITY UPGRADE-REV.SDF Page 13 JOB TITLE: Density Upgrade Area C I 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: 76 -9.3 2.157 PL 136.33 PF 0.2 - R33 31.8 0.0 33.5 0.0 0.8 120 FTG 2T PE 0.0 R34 31.8 0.0 33.6 0.0 0.001 TL 160.33 PV I Pipe: 77 -12.5 2.157 PL 136.33 PF 0.3 R35 31.8 0.0 33.7 0.0 1.1 120 FTG 2T PE 0.0 I R36 31.8 0.0 34.0 0.0 0.002 TL 160.33 PV Pipe: 78 -15.8 2.157 PL 136.33 PF 0.4 R37 31.8 0.0 33.9 0.0 1.4 120 FTG 2T PE 0.0 R38 31.8 0.0 34.3 0.0 0.003 TL 160.33 PV Pipe: 79 -19.3 2.157 PL 136.33 PF 0.6 I R39 31.8 0.0 34.1 0.0 1.7 120 FTG 2T PE 0.0 R40 31.8 0.0 34.7 0.0 0.004 TL 160.33 PV 80 -23.1 2.157 PL 136.33 PF 0.8 I Pipe: R41 31.8 0.0 34.3 0.0 2.0 120 FTG 2T PE 0.0 R42 31.8 0.0 35.1 0.0 0.005 TL 160.33 PV I Pipe: 81 -23.0 2.157 PL 136.33 PF 0.8 R43 31.8 0.0 34.4 0.0 2.0 120 FTG 2T PE 0.0 R44 31.8 0.0 35.2 0.0 0.005 TL 160.33 PV I Pipe: 82 -22.5 2.157 PL 136.33 PF 0.8 R45 31.8 0.0 34.5 0.0 2.0 120 FTG 2T PE 0.0 R46 31.8 0.0 35.3 0.0 0.005 TL 160.33 PV I Pipe: 83 -20.8 2.157 PL 136.33 PF 0.7 R47 31.8 0.0 34.7 0.0 1.8 120 FTG 2T PE 0.0 R48 31.8 0.0 35.4 0.0 0.004 TL 160.33 PV Pipe: 84 -21.0 2.157 PL 136.33 PF 0.7 I R49 R50 31.8 31.8 0.0 0.0 34.8 35.5 0.0 0.0 1.8 120 0.004 FTG TL 2T 160.33 PE PV 0.0 Pipe: 85 -21.5 2.157 PL 136.33 PF 0.7 I R51 31.8 0.0 34.8 0.0 1.9 120 FTG 2T PE 0.0 R52 31.8 0.0 35.6 0.0 0.004 TL 160.33 PV 86 -22.3 2.157 PL 136.33 PF 0.8 I Pipe: R53 31.8 0.0 34.9 0.0 2.0 120 FTG 2T PE 0.0 R54 31.8 0.0 35.7 0.0 0.005 TL 160.33 PV I Pipe: 87 -23.3 2.157 PL 136.33 PF 0.8 R55 31.8 0.0 34.9 0.0 2.0 120 FTG 2T PE 0.0 R56 31.8 0.0 35.8 0.0 0.005 TL 160.33 PV I Pipe: 88 -24.6 2.157 PL 136.33 PF 0.9 R57 31.8 0.0 35.0 0.0 2.2 120 FTG 2T PE 0.0 R58 31.8 0.0 35.9 0.0 0.006 TL 160.33 PV I I DATE: 9/4/20091FE SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 14 TECHNOLOGIES RACKS \CALCULATIONS\ DENS ITY UPGRADE-REV.SDF JOB TITLE: Density Upgrade Area C I 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: 89 -25.9 2.157 PL 136.33 PF 1.0 R59 31.8 0.0 35.0 0.0 2.3 120 FTG 2T PE 0.0 R60 31.8 0.0 36.0 0.0 0.006 TL 160.33 PV I Pipe: 90 -27.4 2.157 PL 136.33 PF 1.1 R61 31.8 0.0 35.0 0.0 2.4 120 FTG 2T FE 0.0 I R62 31.8 0.0 36.1 0.0 0.007 TL 160.33 PV Pipe: 91 -27.2 2.157 PL 1.00 PF 0.1 Ri 31.8 0.0 31.3 0.0 2.4 120 FTG T PE 0.4 1 30.8 0.0 31.8 0.0 0.007 TL 13.00 PV Pipe: 92 27.2 2.157 FL 1.00 PF 0.1 I R2 31.8 0.0 30.2 0.0 2.4 120 FTG T PE 0.4 2 30.8 0.0 30.5 0.0 0.007 TL 13.00 PV • Pipe: 93 -27.3 2.157 PL 1.00 PF 0.1 I R3 31.8 0.0 31.3 0.0 2.4 120 FTG T FE 0.4 3 30.8 0.0 31.8 0.0 0.007 TL 13.00 PV • Pipe: 94 27.3 2.157 FL 1.00 PF 0.1 • R4 31.8 0.0 30.2 0.0 2.4 120 FTG T FE 0.4 4 30.8 0.0 30.5 0.0 0.007 TL 13.00 FV I Pipe: 95 -27.5 2.157 FL 1.00 PF 0.1 R5 31.8 0.0 31.3 0.0 2.4 120 FTG T FE 0.4 I S30.8 0.0 31.8 0.0 0.007 TL 13.00 PV Pipe: 96 27.5 2.157 FL 1.00 PF 0.1 R6 31.8 0.0 30.2 0.0 2.4 120 FTG T FE 0.4 I 6 30.8 0.0 30.5 0.0 0.007 TL 13.00 PV Pipe: 97 -27.9 2.157 FL 1.00 PF 0.1 I R7 7 31.8 30.8 0.0 0.0 31.3 31.9 0.0 0.0 2.4 120 0.007 FTG TL T 13.00 FE PV 0.4 Pipe: 98 27.9 2.157 PL 1.00 PF 0.1 I R8 31.8 0.0 30.2 0.0 2.4 120 FTG T FE 0.4 8 30.8 0.0 30.5 0.0 0.007 TL 13.00 PV • Pipe: 99 -28.6 2.157 PL 1.00 PF 0.1 • R9 31.8 0.0 31.4 0.0 2.5 120 FTG T FE 0.4 9 30.8 0.0 31.9 0.0 0.008 TL 13.00 PV I Pipe: 100 28.6 2.157 FL 1.00 PF 0.1 RiO 31.8 0.0 30.1 0.0 2.5 120 FTG T FE 0.4 10 30.8 0.0 30.5 0.0 0.008 TL 13.00 PV I Pipe: 101 -29.7 2.157 FL 1.00 PP 0.1 Rll 31.8 0.0 31.4 0.0 2.6 120 FTG T FE 0.4 ii 30.8 0.0 31.9 0.0 0.008 TL 13.00 PV I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 15 I DATE: 9/4/20091FE TECHNOLOGIES RACKS\CALCULATIONS\DENSITY UPGRADE-REV.SDF JOB TITLE: Density Upgrade Area C PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. I END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 102 29.7 2.157 PL 1.00 PF 0.1 - R12 31.8 0.0 30.1 0.0 2.6 120 FTG T PE 0.4 12 30.8 0.0 30.4 0.0 0.008 TL 13.00 PV I Pipe: 103 -31.2 2.157 PL 1.00 PF 0.1 R13 31.8 0.0 31.5 0.0 2.7 120 FTG T PE 0.4 I 13 30.8 0.0 32.0 0.0 0.009 TL 13.00 PV Pipe: 104 31.2 2.157 FL 1.00 PF 0.1 R14 31.8 0.0 30.0 0.0 2.7 120 FTG T FE 0.4 14 30.8 0.0 30.4 0.0 0.009 TL 13.00 PV Pipe: 105 -28.0 2.157 FL 1.00 PF 0.1 31.8 0.0 31.6 0.0 2.5 120 FTG T FE 0.4 I R15 15 30.8 0.0 32.1 0.0 0.007 TL 13.00 PV • Pipe: 106 28.0 2.157 FL 1.00 PF 0.1 I R16 31.8 0.0 30.4 0.0 2.5 120 FTG T FE 0.4 16 30.8 0.0 30.8 0.0 0.007 TL 13.00 PV I Pipe: 107 -23.8 2.157 FL 1.00 PF 0.1 U R17 31.8 0.0 31.7 0.0 2.1 120 FTG T FE 0.4 17 30.8 0.0 32.2 0.0 0.005 TL 13.00 PV I Pipe: 108 23.8 2.157 FL 1.00 PF 0.1 R18 31.8 0.0 30.9 0.0 2.1 120 FTG T PE 0.4 18 30.8 0.0 31.2 0.0 0.005 TL 13.00 PV I Pipe: 109 -19.9 2.157 FL 1.00 PF 0.1 R19 31.8 0.0 31.9 0.0 1.8 120 FTG T PE 0.4 I 19 30.8 0.0 32.4 0.0 0.004 TL 13.00 PV Pipe: 110 19.9 2.157 FL 1.00 PF 0.1 I R20 20 31.8 30.8 0.0 0.0 31.3 31.7 0.0 0.0 1.8 120 0.004 FTG TL T 13.00 FE PV 0.4 Pipe: 111 -16.4 2.157 FL 1.00 PF 0.0 I R21 31.8 0.0 32.1 0.0 1.4 120 FTG T FE 0.4 21 30.8 0.0 32.6 0.0 0.003 TL 13.00 PV • Pipe: 112 16.4 2.157 PL 1.00 PF 0.0 R22 31.8 0.0 31.7 0.0 1.4 120 FTG T PE 0.4 22 30.8 0.0 32.1 0.0 0.003 TL 13.00 PV I Pipe: 113 -13.0 2.157 FL 1.00 PF 0.0 • R23 31.8 0.0 32.3 0.0 1.1 120 FTG T FE 0.4 23 30.8 0.0 32.8 0.0 0.002 TL 13.00 PV I Pipe: 114 13.0 2.157 FL 1.00 PF 0.0 R24 31.8 0.0 32.0 0.0 1.1 120 FTG T PR 0.4 24 30.8 0.0 32.4 0.0 0.002 TL 13.00 PV I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 16 I DATE: 9/4/20091FE TECHNOLOGIES RACKS\CALCULATIONS\DENSITY UPGRADE-REV.SDF JOB TITLE: Density Upgrade Area C PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. I END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) I Pipe: 115 -9.8 2.157 PL 1.00 PF 0.0 - R25 31.8 0.0 32.5 0.0 0.9 120 FTG T PE 0.4 25 30.8 0.0 33.0 0.0 0.001 TL 13.00 PV I Pipe: 116 9.8 2.157 PL 1.00 FE' 0.0 R26 31.8 0.0 32.4 0.0 0.9 120 FTG T PE 0.4 I 26 30.8 0.0 32.8 0.0 0.001 TL 13.00 PV Pipe: 117 -6.5 2.157 PL 1.00 FE' 0.0 R27 31.8 0.0 32.8 0.0 0.6 120 FTG T FE 0.4 1 27 30.8 0.0 33.2 0.0 0.000 TL 13.00 PV Pipe: 118 6.5 2.157 PL 1.00 PF 0.0 31.8 0.0 32.7 0.0 0.6 120 FTG T PE 0.4 I R28 28 30.8 0.0 33.1 0.0 0.000 TL 13.00 PV • Pipe: 119 -1.3 2.157 FL 1.00 FE' 0.0 R29 31.8 0.0 33.0 0.0 0.1 120 FTG T FE 0.4 29 30.8 0.0 33.4 0.0 0.000 TL 13.00 PV 1 Pipe: 120 1.3 2.157 FL 1.00 FE' 0.0 • R30 31.8 0.0 33.0 0.0 0.1 120 FTG T PE 0.4 30 30.8 0.0 33.4 0.0 0.000 TL 13.00 PV I Pipe: 121 6.0 2.157 PL 1.00 PF 0.0 R31 31.8 0.0 33.2 0.0 0.5 120 FTG T FE 0.4 31 30.8 0.0 33.7 0.0 0.000 TL 13.00 PV I Pipe: 122 -6.0 2.157 PL 1.00 FE' 0.0 R32 31.8 0.0 33.3 0.0 0.5 120 FTG T FE 0.4 I 32 30.8 0.0 33.8 0.0 0.000 TL 13.00 PV Pipe: 123 9.3 2.157 FL 1.00 PF 0.0 1 R33 33 31.8 30.8 0.0 0.0 33.5 33.9 0.0 0.0 0.8 120 0.001 FTG TL T 13.00 FE PV 0.4 Pipe: 124 -9.3 2.157 FL 1.00 FE' 0.0 I R34 31.8 0.0 33.6 0.0 0.8 120 FTG T FE 0.4 34 30.8 0.0 34.1 0.0 0.001 TL 13.00 FV • Fipe: 125 12.5 2.157 FL 1.00 FE' 0.0 R35 31.8 0.0 33.7 0.0 1.1 120 FTG T FE 0.4 35 30.8 0.0 34.1 0.0 0.002 TL 13.00 PV I Pipe: 126 -12.5 2.157 FL 1.00 FE' 0.0 R36 31.8 0.0 34.0 0.0 1.1 120 FTG T FE 0.4 36 30.8 0.0 34.4 0.0 0.002 TL 13.00 PV I Pipe: 127 15.8 2.157 FL 1.00 FE' 0.0 R37 31.8 0.0 33.9 0.0 1.4 120 FTG T FE 0.4 37 30.8 0.0 34.3 0.0 0.003 TL 13.00 PV I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 17 I DATE: 9/4/2009IFE TECHNOLOGIES RACKS\CALCULATIONS\DENSITY UPGRADE-REV.SDF JOB TITLE: Density Upgrade Area C PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. I END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) I Pipe: 128 -15.8 2.157 PL 1.00 PF 0.0 - R38 31.8 0.0 34.3 0.0 1.4 120 FTG T PE 0.4 38 30.8 0.0 34.8 0.0 0.003 TL 13.00 PV I Pipe: 129 19.3 2.157 PL 1.00 PF 0.0 R39 31.8 0.0 34.1 0.0 1.7 120 FTG T PE 0.4 I 39 30.8 0.0 34.5 0.0 0.004 TL 13.00 PV Pipe: 130 -19.3 2.157 PL 1.00 PF 0.0 R40 31.8 0.0 34.7 0.0 1.7 120 FTG T PE 0.4 40 30.8 0.0 35.2 0.0 0.004 TL 13.00 PV Pipe: 131 23.1 2.157 PL 1.00 PF 0.1 31.8 0.0 34.3 0.0 2.0 120 FTG T PE 0.4 I R41 41 30.8 0.0 34.7 0.0 0.005 TL 13.00 PV - Pipe: 132 -23.1 2.157 PL 1.00 PF 0.1 I R42 31.8 0.0 35.1 0.0 2.0 120 FTG T PE 0.4 42 30.8 0.0 35.6 0.0 0.005 TL 13.00 PV • Pipe: 133 23.0 2.157 PL 1.00 PF 0.1 I R43 31.8 0.0 34.4 0.0 2.0 120 FTG T PE 0.4 43 30.8 0.0 34.8 0.0 0.005 TL 13.00 PV I Pipe: 134 -23.0 2.157 PL 1.00 PF 0.1 R44 31.8 0.0 35.2 0.0 2.0 120 FTG T PE 0.4 44 30.8 0.0 35.7 0.0 0.005 TL 13.00 PV I Pipe: 135 22.5 2.157 PL 1.00 PF 0.1 R45 31.8 0.0 34.5 0.0 2.0 120 FTG T PE 0.4 I 45 30.8 0.0 34.9 0.0 0.005 TL 13.00 PV Pipe: 136 -22.5 2.157 PL 1.00 PF 0.1 31.8 0.0 35.3 0.0 2.0 120 FTG T PE 0.4 I R46 46 30.8 0.0 35.8 0.0 0.005 TL 13.00 PV Pipe: 137 20.8 2.157 PL 1.00 PF 0.1 I R47 31.8 0.0 34.7 0.0 1.8 120 FTG T FE 0.4 47 30.8 0.0 35.1 0.0 0.004 TL 13.00 PV • Pipe: 138 -20.8 2.157 PL 1.00 PF 0.1 R48 31.8 0.0 35.4 0.0 1.8 120 FTG T PE 0.4 48 30.8 0.0 35.9 0.0 0.004 TL 13.00 PV I Pipe: 139 21.0 2.157 FL 1.00 PF 0.1 5 R49 31.8 0.0 34.8 0.0 1.8 120 FTG T PE 0.4 49 30.8 0.0 35.2 0.0 0.004 TL 13.00 PV I Pipe: 140 -21.0 2.157 FL 1.00 PF 0.1 R50 31.8 0.0 35.5 0.0 1.8 120 FTG T PE 0.4 50 30.8 0.0 36.0 0.0 0.004 TL 13.00 PV I SYSTEM HYDRAULIC ANALYSIS Page 18 DATE: I SPRINKLER 9/4/20091F5 TECHNOLOGIES RACKS\CALCULATIONS\DENSITY UPGRADE-REV.SDF JOB TITLE: Density Upgrade Area C I 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) I Pipe: 141 21.5 2.157 PL 1.00 PF 0.1 R51 31.8 0.0 34.8 0.0 1.9 120 FTG T PE 0.4 51 30.8 0.0 35.2 0.0 0.004 TL 13.00 PV I Pipe: 142 -21.5 2.157 PL 1.00 PF 0.1 R52 31.8 0.0 35.6 0.0 1.9 120 FTG T PE 0.4 I 52 30.8 0.0 36.1 0.0 0.004 TL 13.00 PV Pipe: 143 22.3 2.157 PL 1.00 PF 0.1 I R53 53 31.8 30.8 0.0 0.0 34.9 35.3 0.0 0.0 2.0 120 0.005 FTG TL T 13.00 PE PV 0.4 Pipe: 144 -22.3 2.157 PL 1.00 PF 0.1 I R54 31.8 0.0 35.7 0.0 2.0 120 FTG T PS 0.4 54 30.8 0.0 36.1 0.0 0.005 TL 13.00 PV • Pipe: 145 23.3 2.157 PL 1.00 PF 0.1 R55 31.8 0.0 34.9 0.0 2.0 120 FTG T PE 0.4 55 30.8 0.0 35.3 0.0 0.005 TL 13.00 PV Pipe: 146 -23.3 2.157 PL 1.00 PF 0.1 - R56 31.8 0.0 35.8 0.0 2.0 120 FTG T PE 0.4 56 30.8 0.0 36.3 0.0 0.005 TL 13.00 PV Pipe: 147 24.6 2.157 PL 1.00 PF 0.1 R57 31.8 0.0 35.0 0.0 2.2 120 FTG T PE 0.4 I 57 30.8 0.0 35.3 0.0 0.006 TL 13.00 PV Pipe: 148 -24.6 2.157 PL 1.00 PF 0.1 R58 31.8 0.0 35.9 0.0 2.2 120 FTG T PS 0.4 58 30.8 0.0 36.4 0.0 0.006 TL 13.00 PV Pipe: 149 25.9 2.157 PL 1.00 PF 0.1 31.8 0.0 35.0 0.0 2.3 120 FTG T PE 0.4 I R59 59 30.8 0.0 35.3 0.0 0.006 TL 13.00 PV Pipe: 150 -25.9 2.157 PL 1.00 PF 0.1 R60 31.8 0.0 36.0 0.0 2.3 120 FTG T PE 0.4 60 30.8 0.0 36.5 0.0 0.006 TL 13.00 PV I Pipe: 151 27.4 2.157 PL 1.00 PF 0.1 I R61 31.8 0.0 35.0 0.0 2.4 120 FTG T PR 0.4 61 30.8 0.0 35.3 0.0 0.007 TL 13.00 PV I Pipe: 152 -27.4 2.157 PL 1.00 PF 0.1 R62 31.8 0.0 36.1 0.0 2.4 120 FTG T PR 0.4 62 30.8 0.0 36.6 0.0 0.007 TL 13.00 PV 1 Pipe: 153 -27.2 4.260 PL 10.00 PF 0.0 1 30.8 0.0 31.8 0.0 0.6 120 FTG ---- PE 0.0 3 30.8 0.0 31.8 0.0 0.000 TL 10.00 PV I I SPRINKLER DATE: 9/4/20091FE SYSTEM HYDRAULIC ANALYSIS Page 19 TECHNOLOGIES RACKS\CALCULATIONS\DENSITY UPGRADE-REV.SDF JOB TITLE: Density Upgrade Area C I 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) I Pipe: 154 -54.5 4.260 PL 10.00 PF 0.0 3 30.8 0.0 31.8 0.0 1.2 120 FTG ---- PE 0.0 I 30.8 0.0 31.8 0.0 0.001 TL 10.00 PV Pipe: 155 -81.9 4.260 PL 10.00 PF 0.0 5 30.8 0.0 31.8 0.0 1.8 120 FTG ---- PE 0.0 I 7 30.8 0.0 31.9 0.0 0.002 TL 10.00 PV Pipe: 156 -109.8 4.260 PL 10.00 PF 0.0 - 7 9 30.8 30.8 0.0 0.0 31.9 31.9 0.0 0.0 2.5 120 0.003 FTG TL ---- 10.00 PE 0.0 PV Pipe: 157 -138.4 4.260 FL 10.00 PF 0.1 I 30.8 0.0 31.9 0.0 3.1 120 FTG ---- PE 0.0 11 30.8 0.0 31.9 0.0 0.005 TL 10.00 PV 158 -168.2 4.260 PL 10.00 PF 0.1 I Pipe: 11 30.8 0.0 31.9 0.0 3.8 120 FTG ---- PE 0.0 13 30.8 0.0 32.0 0.0 0.007 TL 10.00 PV I Pipe: 159 -199.4 4.260 FL 10.00 PF 0.1 13 30.8 0.0 32.0 0.0 4.5 120 FTG ---- PE 0.0 15 30.8 0.0 32.1 0.0 0.010 TL 10.00 PV I Pipe: 160 -227.4 4.260 PL 10.00 PF 0.1 15 30.8 0.0 32.1 0.0 5.1 120 FTG ---- PE 0.0 I 17 30.8 0.0 32.2 0.0 0.013 TL 10.00 PV Pipe: 161 -251.2 4.260 PL 10.00 PF 0.2 17 30.8 0.0 32.2 0.0 5.7 120 FTG ---- PE 0.0 19 30.8 0.0 32.4 0.0 0.015 TL 10.00 PV Pipe: 162 -271.1 4.260 PL 10.00 PF 0.2 30.8 0.0 32.4 0.0 6.1 120 FTG ---- PE 0.0 I 19 21 30.8 0.0 32.6 0.0 0.018 TL 10.00 PV I 21 Pipe: 163 30.8 0.0 32.6 0.0 -287.5 6.5 4.260 120 PL FTG 10.00 ---- PF PE 0.2 0.0 23 30.8 0.0 32.8 0.0 0.020 TL 10.00 PV I Pipe: 164 -300.6 4.260 PL 10.00 PF 0.2 23 30.8 0.0 32.8 0.0 6.8 120 FTG ---- PE 0.0 25 30.8 0.0 33.0 0.0 0.021 TL 10.00 PV I Pipe: 165 -310.4 4.260 PL 10.00 PF 0.2 25 30.8 0.0 33.0 0.0 7.0 120 FTG ---- PE 0.0 27 30.8 0.0 33.2 0.0 0.023 TL 10.00 PV I Pipe: 166 -316.9 4.260 PL 10.00 PF 0.2 27 30.8 0.0 33.2 0.0 7.1 120 FTG ---- PE 0.0 29 30.8 0.0 33.4 0.0 0.023 TL 10.00 PV I I SPRINKLER DATE: 9/4/20091FE SYSTEM HYDRAULIC ANALYSIS Page 20 TECHNOLOGIES RACKS\CALCULATIONS\DENSITY UPGRADE-REV.SDF JOB TITLE: Density Upgrade Area C I 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) I Pipe: 167 -318.2 4.260 PL 10.00 PF 0.2 29 30.8 0.0 33.4 0.0 7.2 120 FTG ---- PE 0.0 31 30.8 0.0 33.7 0.0 0.024 TL 10.00 PV I Pipe: 168 -312.2 4.260 PL 10.00 PF 0.2 31 30.8 0.0 33.7 0.0 7.0 120 FTG ---- PE 0.0 33 30.8 0.0 33.9 0.0 0.023 TL 10.00 PV Pipe: 169 -302.9 4.260 PL 10.00 PF 0.2 I 33 35 30.8 30.8 0.0 0.0 33.9 34.1 0.0 0.0 6.8 120 0.022 FTG TL ---- 10.00 PE PV 0.0 Pipe: 170 -290.4 4.260 PL 10.00 PF 0.2 I 35 30.8 0.0 34.1 0.0 6.5 120 FTG ---- PE 0.0 37 30.8 0.0 34.3 0.0 0.020 TL 10.00 PV 171 -274.7 4.260 PL 10.00 PF 0.2 37 I Pipe: 30.8 0.0 34.3 0.0 6.2 120 FTG ---- PE 0.0 39 30.8 0.0 34.5 0.0 0.018 TL 10.00 PV I Pipe: 172 -255.4 4.260 PL 10.00 PF 0.2 39 30.8 0.0 34.5 0.0 5.7 120 FTG ---- PE 0.0 41 30.8 0.0 34.7 0.0 0.016 TL 10.00 PV I Pipe: 173 -232.3 4.260 PL 10.00 PF 0.1 41 30.8 0.0 34.7 0.0 5.2 120 FTG ---- PE 0.0 I 43 30.8 0.0 34.8 0.0 0.013 TL 10.00 PV Pipe: 174 -209.3 4.260. PL 10.00 PF 0.1 43 30.8 0.0 34.8 0.0 4.7 120 FTG ---- PE 0.0 I s 30.8 0.0 34.9 0.0 0.011 TL 10.00 PV Pipe: 175 -186.8 4.260 PL 10.00 PF 0.2 30.8 0.0 34.9 0.0 4.2 120 FTG E PE 0.0 I 45 47 30.8 0.0 35.1 0.0 0.009 TL 23.00 PV Pipe: 176 -166.0 4.260 PL 10.00 PF 0.1 I 47 30.8 0.0 35.1 0.0 3.7 120 FTG ---- PE 0.0 49 30.8 0.0 35.2 0.0 0.007 TL 10.00 PV 177 -145.0 4.260 PL 10.00 PF 0.1 49 I Pipe: 30.8 0.0 35.2 0.0 3.3 120 FTG ---- PE 0.0 51 30.8 0.0 35.2 0.0 0.006 TL 10.00 PV I Pipe: 178 -123.5 4.260 PL 10.00 PF 0.0 51 30.8 0.0 35.2 0.0 2.8 120 FTG ---- FE 0.0 53 30.8 0.0 35.3 0.0 0.004 TL 10.00 PV 1 Pipe: 179 -101.3 4.260 PL 10.00 PF 0.0 53 30.8 0.0 35.3 0.0 2.3 120 FTG ---- FE 0.0 55 30.8 0.0 35.3 0.0 0.003 TL 10.00 PV I I SPRINKLER DATE: 9/4/20091FE SYSTEM HYDRAULIC ANALYSIS TECHNOLOGIES RACKS\CALCULATIONS\DENSITY UPGRADE-REV.SDF Page 21 JOB TITLE: Density Upgrade Area C I PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GEM) FL/FT (PSI) I Pipe: 180 -77.9 4.260 PL 10.00 PF 0.0 55 30.8 0.0 35.3 0.0 1.8 120 FTG ---- PE 0.0 57 30.8 0.0 35.3 0.0 0.002 TL 10.00 PV I Pipe: 181 -53.4 4.260 EL 10.00 PF 0.0 57 30.8 0.0 35.3 0.0 1.2 120 FTG ---- PE 0.0 I 59 30.8 0.0 35.3 0.0 0.001 TL 10.00 EV Pipe: 182 -27.4 4.260 PL 10.00 PF 0.0 I 59 61 30.8 30.8 0.0 0.0 35.3 35.3 0.0 0.0 0.6 120 0.000 FTG TL ---- 10.00 PE PV 0.0 Pipe: 183 27.2 4.260 EL 10.00 PF 0.0 I 2 30.8 0.0 30.5 0.0 0.6 120 FTG ---- PE 0.0 4 30.8 0.0 30.5 0.0 0.000 TL 10.00 PV 184 54.5 4.260 EL 10.00 PF 0.0 I Pipe: 4 30.8 0.0 30.5 0.0 1.2 120 FTG ---- PE 0.0 6 30.8 0.0 30.5 0.0 0.001 TL 10.00 PV I Pipe: 185 81.9 4.260 EL 10.00 PF 0.0 6 30.8 0.0 30.5 0.0 1.8 120 FTG ---- PE 0.0 8 30.8 0.0 30.5 0.0 0.002 TL 10.00 PV I Pipe: 186 109.8 4.260 EL 10.00 PF 0.0 8 30.8 0.0 30.5 0.0 2.5 120 FTG ---- PE 0.0 I 10 30.8 0.0 30.5 0.0 0.003 TL 10.00 PV Pipe: 187 138.4 4.260 EL 10.00 PF 0.1 10 30.8 0.0 30.5 0.0 3.1 120 FTG ---- PE 0.0 12 30.8 0.0 30.4 0.0 0.005 TL 10.00 PV Pipe: 188 168.2 4.260 EL 10.00 PF 0.1 30.8 0.0 30.4 0.0 3.8 120 FTG ---- PE 0.0 I 12 14 30.8 0.0 30.4 0.0 0.007 TL 10.00 PV Pipe: 189 199.4 4.260 EL 2.00 PF 0.0 14 30.8 0.0 30.4 0.0 4.5 120 FTG ---- PE 0.0 M6 30.8 0.0 30.3 0.0 0.010 TL 2.00 PV 190 -492.4 4.260 EL 8.00 PF 0.4 I Pipe: M6 30.8 0.0 30.3 0.0 11.1 120 FTG ---- PE 0.0 16 30.8 0.0 30.8 0.0 0.053 TL 8.00 PV I Pipe: 191 -464.4 4.260 EL 10.00 PF 0.5 16 30.8 0.0 30.8 0.0 10.5 120 FTG ---- EE 0.0 18 30.8 0.0 31.2 0.0 0.048 TL 10.00 PV I Pipe: 192 -440.6 4.260 EL 10.00 PF 0.4 18 30.8 0.0 31.2 0.0 9.9 120 FTG ---- PE 0.0 20 30.8 0.0 31.7 0.0 0.043 TL 10.00 PV Li DATE: I SPRINKLER 9/4/20091FE SYSTEM HYDRAULIC ANALYSIS TECHNOLOGIES RACKS\CALCULATIONS\DENSITY UPGRADE-REV.SDF Page 22 JOB TITLE: Density Upgrade Area C I 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) I Pipe: 193 -420.7 4.260 FL 10.00 PF 0.4 20 30.8 0.0 31.7 0.0 9.5 120 FTG ---- FE 0.0 22 30.8 0.0 32.1 0.0 0.040 TL 10.00 PV I Pipe: 194 -404.3 4.260 PL 10.00 PF 0.4 22 30.8 0.0 32.1 0.0 9.1 120 FTG ---- FE 0.0 24 30.8 0.0 32.4 0.0 0.037 TL 10.00 PV Pipe: 195 -391.2 4.260 FL 10.00 PF 0.3 I 24 26 30.8 30.8 0.0 0.0 32.4 32.8 0.0 0.0 8.8 120 0.035 FTG TL ---- 10.00 PE PV 0.0 Pipe: 196 -381.4 4.260 FL 10.00 PF 0.3 I 26 30.8 0.0 32.8 0.0 8.6 120 FTG ---- FE 0.0 28 30.8 0.0 33.1 0.0 0.033 TL 10.00 PV 197 -374.9 4.260 FL 10.00 PF 0.3 I Pipe: 28 30.8 0.0 33.1 0.0 8.4 120 FTG ---- FE 0.0 30 30.8 0.0 33.4 0.0 0.032 TL 10.00 PV I Pipe: 198 -373.6 4.260 FL 10.00 PF 0.3 30 30.8 0.0 33.4 0.0 8.4 120 FTG ---- FE 0.0 32 30.8 0.0 33.8 0.0 0.032 TL 10.00 PV 1 Pipe: 199 -379.6 4.260 PL 10.00 PF 0.3 32 30.8 0.0 33.8 0.0 8.5 120 FTG ---- PE 0.0 I 34 30.8 0.0 34.1 0.0 0.033 TL 10.00 PV Pipe: 500 -388.9 4.260 FL 10.00 PP 0.3 34 30.8 0.0 34.1 0.0 8.8 120 FTG ---- FE 0.0 36 30.8 0.0 34.4 0.0 0.034 TL 10.00 FV Pipe: 201 -401.4 4.260 FL 10.00 PP 0.4 36 30.8 0.0 34.4 0.0 9.0 120 FTG ---- FE 0.0 I 38 30.8 0.0 34.8 0.0 0.036 TL 10.00 PV Pipe: 202 -417.1 4.260 FL 10.00 PP 0.4 38 30.8 0.0 34.8 0.0 9.4 120 FTG ---- FE 0.0 40 30.8 0.0 35.2 0.0 0.039 TL 10.00 PV I Pipe: 203 -436.4 4.260 FL 10.00 PF 0.4 40 30.8 0.0 35.2 0.0 9.8 120 FTG ---- FE 0.0 42 30.8 0.0 35.6 0.0 0.042 TL 10.00 PV I Pipe: 204 -459.5 4.260 FL 1.50 PF 0.1 42 30.8 0.0 35.6 0.0 10.3 120 FTG ---- FE 0.0 42A 30.8 0.0 35.7 0.0 0.047 TL 1.50 PV I Pipe: 204A -459.5 6.357 FL 8.50 PP 0.1 42A 30.8 0.0 35.7 0.0 4.6 120 FTG ---- FE 0.0 44 30.8 0.0 35.7 0.0 0.007 TL 8.50 PV P1 DATE: I SPRINKLER 9/4/2009IFE SYSTEM HYDRAULIC ANALYSIS Page 23 TECHNOLOGIES RACKS\CALCULATIONS\DENSITY UPGRADE-REV.SDF JOB TITLE: Density Upgrade Area C I 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) I Pipe: 205 -482.5 6.357 PL 10.00 PF 0.1 44 30.8 0.0 35.7 0.0 4.9 120 FTG ---- PE 0.0 46 30.8 0.0 35.8 0.0 0.007 TL 10.00 PV I Pipe: 206 -505.0 6.357 PL 10.00 PF 0.1 46 30.8 0.0 35.8 0.0 5.1 120 FTG ---- PE 0.0 I 48 30.8 0.0 35.9 0.0 0.008 TL 10.00 Pv Pipe: 207 -525.8 6.357 PL 10.00 PF 0.1 I 48 50 30.8 30.8 0.0 0.0 35.9 36.0 0.0 0.0 5.3 120 0.009 FTG TL ---- 10.00 PE PV 0.0 Pipe: 208 -546.7 6.357 PL 10.00 PF 0.1 I 50 30.8 0.0 36.0 0.0 5.5 120 FTG ---- PE 0.0 52 30.8 0.0 36.1 0.0 0.009 TL 10.00 PV 209 -568.2 6.357 PL 10.00 PF 0.1 I Pipe: 52 30.8 0.0 36.1 0.0 5.7 120 FTG ---- PE 0.0 54 30.8 0.0 36.1 0.0 0.010 TL 10.00 PV I Pipe: 210 -590.5 6.357 PL 10.00 PF 0.1 54 30.8 0.0 36.1 0.0 6.0 120 FTG ---- PE 0.0 56 30.8 0.0 36.3 0.0 0.011 TL 10.00 PV 1 Pipe: 212 -613.9 6.357 PL 10.00 PF 0.1 56 30.8 0.0 36.3 0.0 6.2 120 FTG ---- PE 0.0 I 58 30.8 0.0 36.4 0.0 0.011 TL 10.00 PV Pipe: 213 -638.4 6.357 PL 10.00 PF 0.1 58 30.8 0.0 36.4 0.0 6.5 120 FTG ---- PE 0.0 60 30.8 0.0 36.5 0.0 0.012 TL 10.00 PV Pipe: 214 -664.3 6.357 PL 10.00 PF 0.1 30.8 0.0 36.5 0.0 6.7 120 FTG ---- PE 0.0 I 60 62 30.8 0.0 36.6 0.0 0.013 TL 10.00 PV Pipe: 215 -691.8 6.357 PL 42.92 PF 1.4 62 30.8 0.0 36.6 0.0 7.0 120 FTG 3E PE 0.0 TOR 30.8 0.0 38.0 0.0 0.014 TL 96.92 PV 216 -691.8 6.357 PL 30.25 PF 2.8 I Pipe: TOR 30.8 0.0 38.0 0.0 7.0 120 FTG 3TCB PE 13.1 BOR 0.5 0.0 53.9 0.0 0.014 TL 197.25 PV I Pipe: 217 -691.8 7.980 PL 5.00 PF 0.1 BOR 0.5 0.0 53.9 0.0 4.4 150 FTG 2L PE 1.5 DI -3.0 0.0 55.5 0.0 0.003 TL 45.00 PV I Pipe: 218 -691.8 7.980 PL 40.00 PF 0.2 DI -3.0 0.0 55.5 0.0 4.4 150 FTG E FE 0.0 UG -3.0 0.0 55.8 0.0 0.003 TL 67.00 PV I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 24 DATE: 9/4/2009IFE TECHNOLOGIES RACKS\CALCULATIONS\DENSITY UPGRADE-REV.SDF JOB TITLE: Density Upgrade Area C I 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) I Pipe: 219 -691.8 7.980 PL 15.00 PF 0.0 UG -3.0 0.0 55.8 0.0 4.4 150 FTG ---- PE 0.0 I UG1 -3.0 0.0 55.8 0.0 0.003 TL 15.00 PV Pipe: 219A -691.8 7.980 FL 237.50 PF 0.7 UG1 -3.0 0.0 55.8 0.0 4.4 150 FTG ---- FE 0.0 I UG2 -3.0 0.0 56.5 0.0 0.003 TL 237.50 PV Pipe: 220 -691.8 7.980 PL 406.50 PF 1.4 I UG2 -3.0 0.0 56.5 0.0 4.4 150 FTG T PE 0.0 UG4 -3.0 0.0 58.0 0.0 0.003 TL 459.50 PV Pipe: 221 -691.8 7.980 PL 25.50 PF 0.2 I II UG4 -3.0 0.0 58.0 0.0 4.4 150 FTG 2L FE 0.0 UG5 -3.0 0.0 58.2 0.0 0.003 TL 65.50 PV Pipe: 222 -691.8 8.390 FL 6.00 PF 0.1 UGS -3.0 0.0 58.2 0.0 4.0 140 FTG 2L FE -2.6 EF1 3.0 0.0 55.7 0.0 0.003 TL 50.00 PV Pipe: 223 FIXED PRESSURE LOSS DEVICE BF2 3.0 0.0 63.7 0.0 8.0 psi, 691.8 gpm BF1 3.0 0.0 55.7 0.0 I Pipe: 224 -691.8 8.390 FL 6.00 PF 0.1 BF2 3.0 0.0 63.7 0.0 4.0 140 FTG 2L PE 2.6 I UG6 -3.0 0.0 66.4 0.0 0.003 TL 50.00 PV Pipe: 225 -691.8 7.980 FL 16.83 PF 0.3 UG6 -3.0 0.0 66.4 0.0 4.4 150 FTG TL FE 0.0 UG7 -3.0 0.0 66.7 0.0 0.003 TL 89.83 PV Pipe: 226 -691.8 7.980 PL 126.00 PF 0.7 UG7 -3.0 0.0 66.7 0.0 4.4 150 FTG 2ETG FE -1.3 SRC 0.0 SRCE 66.1 (N/A) 0.003 TL 239.00 PV NOTES (HASS) Calculations were performed by the HASS 8.0 computer program I under license no. 50040828 granted by HRS Systems, Inc. 208 South Public Square I Petersburg, TN 37144 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 0.116 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 28.8 ft/sec at pipe 50. I I I I I I I I I 1 I I I I I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 25 DATE: 9/4/20091FE TECHNOLOGIES RACKS\CALCULATIONS\DENSITY UPGRADE-REV.SDF JOB TITLE: Density Upgrade Area C I (4) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP MATERIAL: S40 HWC: 120 Equivalent Fitting Lengths in Feet E T L C B G A D N Eli Tee LngEli ChkViv BfyVlv GatVlv AlmChk DPVlv 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 2.203 6.82 13.64 4.09 15.00 8.18 1.36 13.64 13.64 13.64 4.310 13.94 27.87 8.36 30.66 16.72 2.79 27.87 27.87 27.87 PAGE: B MATERIAL: THNWL HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEfl ChkVlv BfyVlv GatVlv AimChk DPVlv NPTee 2.157 6.00 12.00 3.00 14.00 8.00 1.00 12.00 12.00 12.00 4.260 13.00 26.00 8.00 29.00 16.00 3.00 26.00 26.00 26.00 6.357 18.00 38.00 11.00 40.00 13.00 4.00 35.00 35.00 38.00 PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Eli Tee LngEii ChkViv BfyVlv GatVlv NPTee 8.390 31.00 59.00 22.00 76.00 20.00 7.00 59.00 PAGE: E MATERIAL: PVC150 HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Ell Tee LngEfl ChkViv BfyVlv GatVlv NPTee 7.980 27.00 53.00 20.00 68.00 18.00 6.00 53.00 PAGE: * ' Diameter (in) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 26 DATE: 9/4/20091FE TECHNOLOGIES RACKS\CALCULATIONS\DENSITY UPGRADE-REV.SDF JOB TITLE: Density Upgrade Area C I E Q Ea —04 Y' I a) u o o a H a) H Q a) a) 04 70 H H ri HQa)Oa) Q 04 P a)( U) H Ha).HLt) o >, 1 H • -1 U) U) raD Y tolo CD co 04 H CD 04 on 0 0 C'] ) ) 0 0 0 0 H 0 CD 0 0 U 0 0 0 0 0 0 0 H I D 0 0 0 0 0 0 I (N 0 00 Q0 C'] H H 1(O-H--- I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 27 I DATE: 9/4/2009IFE TECHNOLOGIES RACKS\CALCULATIONS\DENSITY UPGRADE-REV.SDF JOB TITLE: Density Upgrade Area C WATER SUPPLY CURVE 120+ I 110+ \\\\\ I I \\\\\ • I \\\\\ * <-102.6 psi @ 1060 gpm 100+ Olow Test Point 1 90+ I I P 80+ R I S 70+ U I I R I X E I 60+ I (I P I 150+ • 40+ 30+ I 20+ = = = = = = = LEGEND X = Required Water Supply I I I 66.15 psi @ 1191.8 gpm 10+ 0 = Available Water Supply I I I 100.42 psi @ 1191.8 gpm 0++-+---+----+-----+ ------+ --------+ --------+ ---------+ -----------+ 400 600 800 1000 1200 1400 1600 1800 2000 I FLOW (GPM) I I