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3112 LINCOLN ST; ; AS120051; Permit
3/8/24,12:37 PM AS120051 Permit Data City of Carlsbad Sprinkler Permit Job Address: 3112 LINCOLN ST Permit Type: SPRINK Parcel No: 2032601400 Lot #: 0 Reference No.: Permit No: AS120051 Status: ISSUED Applied 5/17/2012 Approved: 5/24/2012 Issued: 5/24/2012 PC #: Inspector: Project Title: LINCOLN & OAK NEW CONSTRUCTION Applicant: INNOVATIVE FIRE PROTECTION SUITE 101 8779 COTTONWOOD AV SANTEE, CA (619) 593-8200 (619)593-9133 Owner: LINCOLN&OAK L L C P0 BOX 356 SOLANA BEACH CA Fees ($) Add'I Fees ($) Total ($) Balance ($) 852 . 0 852 0 about:blank ill ;q Parsley Consulting 360 \Vcst 9d1 Avenue, Suite 206 Esconjido, California 92025-5053 T1011o110 (760) 745-6181 lFax(760) 741r. May 10, 2012 Fire Code Official City of Carlsbad Fire Department Office of Fire Protection Services 1635 Faraday Avenue Carlsbad, California 92008 RECEIVED MAY 14 2012 CARLSBAD FIRE DEPARTMENT Subject: Plan Review for Lincoln & Oak Mixed Use Building, 3112 Lincoln Street, Carlsbad, California Dear Sir: We have reviewed the submittal as prepared by Innovative Fire. Based on our review it is our opinion that the submittal is in substantial conformance with the applicable codes and standards in force at this time, including local adopted ordinances. There were some redline notes added to the plans, which were at the direction of the contractor in order to expedite the review. Further submittal should not be required. Sincerely, PA EYCONSULTJNG ti enneth W. agoneT Office Manager End (I) Working Drawings - 2 sets Hydraulic Calculations, Material Submittals - 2 sets Review Comments - 1 set Note: A copy of this letter has been transmitted via e-mail to Innovative Fire on May 10, 2012 file:\C:\Dociiments and Settings\Ken\Rev2 I2l9O.003.wpd Lincoln &Oak Mixed Use Building Review Comments. Page 2 Review Comments Lincoln & Oak Mixed Use Building, 3112 Lincoln Street, Carlsbad, California Main drain size was redlined to 2". The demand for the hydraulic design sign for the retail area was redlined to reflect the revised calculations. It reflects a flow of 507.8 gpm and a pressure of 68.5 psi at the base of the riser. Rated separation notes between floors were redlined on the section view. The check valve and the control valve on the riser were omitted, and this has been redlined. These functions are performed by the backflow prevention assembly and the attached OS&Y valves on either side of that device, per NFPA-13. The main on the ground floor from the top of the riser to reference point 2 has been redlined to show an increase to 4" for that segment. a C-, Parsley Consulting V 350 M-rest 96 Avenue, Suite 206 1IcondjJo, California 92025-5053 Telephone (760) 7415-63.81 Fa,(760) 7415-0537 May 10,.2012 Fire Code Official City of Carlsbad Fire Department Office of Fire Protection Services 1635 Faraday Avenue Carlsbad, California 92008 Subject: Plan Review for Lincoln & Oak Mixed Use Building, California 4, Carlsbad, Dear Sir: We have reviewed the submittal as prepared by Innovative Fire. Based on our review it is our opinion that the submittal is not in substantial conformance with the applicable codes and standards in force at this time, including local adopted ordinances. Further submittal should be required. Since this is not a recommendation for approval no drawings or calculations are being forwarded to you at this time. We have retained one set of submittals for our records, and all remaining sets have been discarded. Sincerely, X ~Wagone O5UL1)NO T Office Manager End (I) Working Drawings - sets Hydraulic Calculations - sets Review Comments - I set Note: A copy of this letter has been transmitted via e-mail to Innovative Fire on May 10, 2012 Is flle:\C:\Docunients and Se11iugs\Ken\Rev2 I 2190.002.wpd Lincoln & Oak Mixed Use Building Review Comments. Page 2 Review Comments MVII Lincoln & Oak Mixed Use Building, 3112 Lincoln Street, Carlsbad, California I. A 4" riser would require a 2" main drain, per Table 8.16.2.4.2. This can be redlined on the plans. C-, The calculations for the retail space -based on the reference numbers of the flowing sprinklers - are mislabeled as being for the "Garage" area, and indicate a density of 0.15 gpm/ft2. The delivered density is 0.20, however the label is incorrect, and should be revised. Retail area pipes ii, 13, 18 and 19 should include the equivalent for a branch tee in the segment. The calculations for the retail space show a demand which exceeds 90% of the available supply which is not allowed. The following comment is for information purposes only, and had no bearing on the recommendation. The system riser shows a control valve, and a check valve. In reviewing sections 8.16.1.1.3.2, and 8.16.1.1.4.3 would suggest that neither is required, as the backfiow valve is deemed to function as the system check valve, and the downstream OS&Y valve on the backflow is deemed to function as the system control valve. In order to minimize opportunity for the system to be taken out of service it might be best to eliminate the third control valve mounted on the riser, and in order to minimize the potential for maintenance work the riser mounted check valve as well. These pittis has',., hceii reviewed ltr apparent compliance with the current applicable codes and s:autdards in force in the jurimliction. The owutr or Contiact,. .r may ucit,,e his reviess in support of .in app1 ic1tion or a building perttitt with the c press understanding t tat this revtess in 11-1 Wtt%' relieves the owner or cotttraclor or their piolessitittal engineer or architect for stile rcspotisihlitv for liii! compliance with stid codes and standards. including the building code or for an respotisihilty lr deficiencies. errors. onlissloils or tiegIience in these plans whether or not noted in this review. l)aie: Reviewer: R!C()MMENI) APPROVAl. ri RICOMMENI) APPROVAl.. AS Nmm SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 5/lU,'2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4680-OHG2.SDF JOB TITLE: LINCOLN & OAK MIXED USE BLDG. RETAIL AREA .20/1506 sq.ft. (ORDINARY HAZARD, G2) WATER SUPPLY DAFA SOURCE STATIC RESID. FLOW AVAIL. TOTAL NODE PRESS. PRESS. 8 PRESS. 8 DEMAND TAG (PSI) (PSI) (GPM) (PSI) (GPM) S 83.7 75.6 1424.0 81.2 757.8 AGGREGATE FLOW ANALYSIS: PRESS. (PSI) 81.1 TOTAL FLOW AT SOURCE 757.8 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 250.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 507.8 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) S -3.0 SOURCE 81.1 507.8 RP 3.0 - - - - 77.5 DA 3.0 - - - - 68.5 DIP -3.0 - - - - 70.4 - - - BOR 1.0 - - - - 68.5 - - - TOR 9.2 - - - - 61.1 - - - 1 9.2 - - - - 58.6 - - - 2 9.2 - - - - 54.6 - - - Ri 9.2 - - - - 42.3 R2 9.2 - - - - 39.2 - - - R2A 9.2 - - - - 17.3 - - - R3 9.2 - - - - 38.1 - - - 201 9.2 K=11.20 34.0 65.3 202 9.2 K=11.20 32.7 64.1 203 9.2 K=11.20 23.6 54.4 204 9.2 K11.20 18.4 48.0 205 9.2 K=11.20 12.1 39.0 206 9.2 K=11.20 16.9 46.1 207 9.2 K=11.20 36.5 67.7 208 9.2 K=11.20 30.9 62.2 209 9.2 K=11.20 29.7 61.0 I Ar'_ I iff IT, SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 5/10/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4680-OHG2.SDF JOB TITLE: LINCOLN & OAK MIXED USE BLDG. RETAIL AREA .20/1506 sq.ft. (ORDINARY HAZARD, G2) PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 1 507.8 5.850 PL 20.00 PF 1.0 S -3.0 SRCE 81.1 (N/A) 6.1 150 FTG TLG PE -2.6 RP 3.0 0.0 77.5 0.0 0.008 TL 128.55 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE RP 3.0 0.0 77.5 0.0 9.0 psi, 507.8 gpm DA 3.0 0.0 68.5 0.0 Pipe: 3 507.8 5.850 PL 17.60 PF 0.7 DA 3.0 0.0 68.5 0.0 6.1 150 FTG 2E PE 2.6 DIP -3.0 0.0 70.4 0.0 0.008 TL 92.03 PV Pipe: 4 507.8 6.340 PL 5.00 PF 0.2 DIP -3.0 0.0 70.4 0.0 5.2 140 FTG E PE -1.7 BOR 1.0 0.0 68.5 0.0 0.006 TL 28.11 PV Pipet 5 507.8 4.310 PL 14.00 PF 3.8 BOR 1.0 0.0 68.5 0.0 11.2 120 FTG 2EC PE -3.6 TOR 9.2 0.0 61.1 0.0 0.053 TL 72.54 PV Pipe: 6 507.8 4.310 PL 19.00 PF 2.5 TOR 9.2 0.0 61.1 0.0 11.2 120 FTG D PE 0.0 1 9.2 0.0 58.6 0.0 0.053 TL 46.87 PV Pipe: 7 507.8 4.310 PL 33.50 PF 4.0 1 9.2 0.0 58.6 0.0 11.2 120 FTG ET PE 0.0 2 9.2 0.0 54.6 0.0 0.053 TL 75.31 PV Pipe: 8 507.8 3.314 PL 22.25 PF 12.3 2 9.2 0.0 54.6' 0.0 18.9 120 FTG 2ET PE 0.0 Ri 9.2 0.0 42.3 0.0 0.191 TL 64.47 PV Pipe: 9 507.8 3.314 PL 6.00 PF 3.1 Ri 9.2 0.0 42.3 0.0 18.9 120 FTG E PE 0.0 R2 9.2 0.0 39.2 0.0 0.191 TL 16.19 PV Pipe: 10 191.0 3.314 PL 14.00 PF 1.1 R2 9.2 0.0 39.2 0.0 7.1 120 FTG T PE 0.0 R3 9.2 0.0 38.1 0.0 0.031 TL 35.84 PV Pipe: ii 129.4 1.728 PL 3.00 PF 5.2 R2 9.2 0.0 39.2 0.0 17.7 120 FTG T PE 0.0 201 9.2 11.2 34.0 65.3 0.362 TL 14.29 PV Pipe: 12 64.1 1.728 PL 13.50 PF 1.3 201 9.2 11.2 34.0 65.3 8.8 120 FTG ---- PE 0.0 202 9.2 11.2 32.7 64.1 0.099 TL 13.50 PV L SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 5/10/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4680-OHG2.SDF JOB TITLE: LINCOLN & OAK MIXED USE BLDG. RETAIL AREA .20/1506 sq.ft. (ORDINARY HAZARD, G2) PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 13 187.5 1.728 PL 10.50 PF 15.7 R2 9.2 0.0 39.2 0.0 25.6 120 FTG T PE 0.0 203 9.2 11.2 23.6 54.4 0.719 TL 21.79 PV Pipe: 14 133.1 1.728 PL 13.50 PF 5.2 203 9.2 11.2 23.6 54.4 18.2 120 FTG ---- PE 0.0 204 9.2 11.2 18.4 48.0 0.382 TL 13.50 PV Pipe: 15 85.1 1.728 PL 6.75 PF 1.1 204 9.2 11.2 18.4 48.0 11.6 120 FTG ---- PE 0.0 R2A 9.2 0.0 17.3 0.0 0.167 TL 6.75 PV Pipe: 16 39.0 1.080 PL 7.50 PF 5.2 R2A 9.2 0.0 17.3 0.0 13.7 120 FTG T PE 0.0 205 9.2 11.2 12.1 39.0 0.388 TL 13.26 PV Pipei 17 46.1 1.728 PL 6.75 PF 0.4 R2A 9.2 0.0 17.3 0.0 6.3 120 FTG ---- PE 0.10 206 9.2 11.2 16.9 46.1 0.054 TL 6.75 PV Pipe: 18 67.7 1.728 PL 3.00 PF 1.6 R3 9.2 0.0 38.1 0.0 9.3 120 FTG T PE 0.0 207 9.2 11.2 36.5 67.7 0.109 TL 14.29 PV Pipe: 19 123.3 1.728 PL 10.50 PF 7.2 R3 9.2 0.0 38.1 0.0 16.9 120 FTG T PE 0.0 208 9.2 11.2 30.9 62.2 0.331 TL 21.79 PV Pipe: 20 61.0 1.728 PL 13.50 PF 1.2 208 9.2 11.2 30.9 62.2 8.3 120 FTG ---- PE 0.0 209 9.2 11.2 29.7 61.0 0.090 TL 13.50 PV NOTES (HASS) Calclations were performed by the HASS 8.2 computer program under license no. 16080621 granted by HRS Systems, Inc. 208 South Public Square Petersburg, TN 37144 (931) 659-9760 The system has been calculated to provide an average imbalance at each node of 0.010 gpm and a ma.imum imbalance at any node of 0.198 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 25.6 ft/sec at pipe 13. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. V SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 5/10/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4680-OHG2.SDF JOB TITLE: LINCOLN & OAK MIXED USE BLDG. RETAIL AREA .20/1506 sq.ft. (ORDINARY HAZARD, G2) (5) PIPE FITTINGS TABLE Pipe Table Name: FSS.PIP PAGE: * MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEii ChkViv BfyViv GatV].v AlmChk DPViv NPTee 1.080 2.30 5.76 2.30 5.76 6.91 1.15 11.52 11.52 5.76 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 4.310 13.94 27.87 8.36 30.66 16.72 2.79 27.87 27.87 27.87 5.850 24.63 51.31 16.42 55.42 18.47 4.10 43.10 43.10 51.31 6.340 17.37 37.23 11.17 39.71 12.41 3.72 34.75 34.75 37.23 100.0 80.0 G A U G E 60.0 P R E 40.0 S U R E 20.0 p S i 0.0 -14.7 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 5/10/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4680-OHG2.SDF JOB TITLE: LINCOLN & OAK MIXED USE BLDG. RETAIL AREA .20/1506 sq.ft. (ORDINARY HAZARD, G2) WATER SUPPLY ANALYSIS Static: 83.70 psi Resid: 75.60 psi Flow: 1424.0 gpm LEGEND Available pressure 81.18 psi @ 757.8 gpm Required pressure 81.13 psi 8 757.8 gpm Source Supply Curve System Demand Curve 4 00 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) Jf SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 5/4/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4680.SDF JOB TITLE: LINCOLN & OAK MIXED USE BLDG. GARAGE AREA .15/1542sq.ft. (ORDINARY HAZARD, Gi) WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) 5 83.7 75.6 1424.0 81.8 649.8 73.5 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 649.8 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 250.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 399.8 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) S -3.0 SOURCE 73.5 399.8 RP 3.0 - - - - 70.2 - - - DA 3.0 -- -- 61.2 DIP -3.0 - - - - 63.4 BOR 1.0 - - - - 61.5 TOR 9.7 - - - - 55.3 - - - 1 9.7 - - - - 50.6 2 9.7 - - - - 43.5 - - - 3 9.7 - - - - 40.7 - - - 4 9.7 - - - - 37.2 - - - 5 9.7 - - - - 33.1 6 9.7 - - - - 31.3 101 9.7 K=11.20 15.3 43.8 102 9.7 K=11.20 10.0 35.5 103 9.7 K=11.20 7.8 31.2 104 9.7 K=11.20 7.2 30.0 105 9.7 K=11.20 26.3 57.5 105A 9.7 K=11.20 28.5 59.8 106 9.7 K=11.20 15.6 44.3 107 9.7 K=11.20 10.3 35.9 108 9.7 K=11.20 8.0 31.6 109 9.7 K=11.20 7.3 30.3 1A 14.5 - - - - .48.4 - - - 7 19.5 - - - - 45.8 8 19.5 - - - - 42.4 - - - 9 19.5 - - - - 38.9 10 19.5 - - - - 37.6 11 29,5 - - - - 40.8 - - - 12 29.5 - - - - 37.8 13 29.5 - - - - 36.1 13A 29.0 - - - - 36.3 14 29.5 - - - - 35.7 - - - 15 29.5 - - - - 35.7 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 5/4/2012 C:\PROGRAN FILES\HRS SYSTEMS\HASS82\C4680.SDF JOB TITLE: LINCOLN & OAK MIXED USE BLDG. GARAGE AREA .15/1542sq.ft. (ORDINARY HAZARD, Gi) NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 15A 33.5 - - - - 34.0 16 29.5 - - - - 35.7 16A 40.0 - - - - 31.2 - - - 17 29.5 - - - - 35.7 17A 29.0 - - - - 35.9 18A 29.0 - - - - 35.9 19 29.5 - - - - 33.7 20 9.7 - - - - 38.3 20A 14.5 - - - - 37,5 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 5/4/2012 C:\PROGRAN FILES\HRS SYSTEMS\HASS82\C4680.SDF JOB TITLE: LINCOLN & OAK MIXED USE BLDG. GARAGE AREA .15/1542sq.ft. (ORDINARY HAZARD, Gi) PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 1 399.8 5.850 PL 20.00 PF 0.7 S -3.0 SRCE 73.5 (N/A) 4.8 150 FTG TLG FE -2.6 RP 3.0 0.0 70.2 0.0 0.005 TL 128.55 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE RP 3.0 0.0 70.2 0.0 9.0 psi, 399.8 gpm DA 3.0 0.0 61.2 0.0 Pipe: 3 399.8 5.850 PL 17.50 PF 0.5 DA 3.0 0.0 61.2 0.0 4.8 150 FTG 2E PE 2.6 DIP -3.0 0.0 63.4 0.0 0.005 TL 91.93 PV Pipe: 4 399.8 6.340 PL 5.00 PF 0.1 DIP -3.0 0.0 63.4 0.0 4.1 140 FTG E PE -1.7 BOR 1.0 0.0 61.5 0.0 0.004 TL 28.11 PV Pipe: 5 399.8 4.310 PL 14.00 PF 2.5 BOR 1.0 0.0 61.5 0.0 8.8 120 FTG 2EC PE -3.8 TOR 9.7 0.0 55.3 0.0 0.034 TL 72.54 PV Pipe: 6 399.8 3.314 FL 19.00 PF 4.6 TOR 9.7 0.0 55.3 0.0 14.9 120 FTG D PE 0.0 1 9.7 0.0 50.6 0.0 0.122 TL 37.93 PV Pipe: 7 375.4 3.314 PL 33.50 PF 7.1 1 9.7 0.0 50.6 0.0 14.0 120 FTG ET PE 0.0 2 9.7 0.0 43.5 0.0 0.109 TL 65.53 PV Pipe: 8 375.4 3.314 PL 4.00 PF 2.8 2 9.7 0.0 43.5 0.0 14.0 120 FTG T FE 0.0 3 9.7 0.0 40.7 0.0 0.109 TL 25.84 PV Pipe: 9 375.4 3.314 PL 10.00 PF 3.5 3 9.7 0.0 40.7 0.0 14.0 120 FTG T PE 0.0 4 9.7 0.0 37.2 0.0 0.109 TL 31.84 PV Pipe: 10 399.8 3.314 PL 11.50 PF 4.1 4 9.7 0.0 37.2 0.0 14.9 120 FTG T FE 0.0 5 9.7 0.0 33.1 0.0 0.122 TL 33.34 PV Pipe: 11 259.3 3.314 PL 11.00 PF 1.8 5 9.7 0.0 33.1 0.0 9.6 120 FTG T FE 0.0 6 9.7 0.0 31.3 0.0 0.055 TL 32.84 PV Pipe: 12 140.5 1.536 PL 17.50 PF 17.9 5 9.7 0.0 33.1 0.0 24.3 120 FTG T FE 0.0 101 9.7 11.2 15.3 43.8 0.748 TL 23.86 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 5/4/2012 C:\PROGRAN FILES\HRS SYSTEMS\HASS82\C4680.SDF JOB TITLE: LINCOLN & OAK MIXED USE BLDG. GARAGE AREA .15/1542sq.ft. (ORDINARY HAZARD, Gi) PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 13 96.7 1.536 PL 14.00 PF 5.2 101 9.7 11.2 15.3 43.8 16.7 120 FTG ---- PE 0.0 102 9.7 11.2 10.0 35.5 0.375 TL 14.00 PV Pipe: 14 61.2 1.536 PL 14.00 PF 2.3 102 9.7 11.2 10.0 35.5 10.6 120 FTG ---- PE .0.0 103 9.7 11.2 7.8 31.2 0.161 TL 14.00 PV Pipe: 15 30.0 1.536 PL 14.00 PF 0.6 103 9.7 11.2 7.8 31.2 5.2 120 FTG ---- PE 0.0 104 9.7 11.2 7.2 30.0 0.043 TL 14.00 PV Pipe: 15A 59.8 1.536 PL 12.00 PF 2.8 6 9.7 0.0 31.3 0.0 10.4 120 FTG T PE 0.0 105A 9.7 11.2 28.5 59.8 0.154 TL 18.36 PV Pipe: 16 199.5 1.536 PL 3.50 PF 5.0 6 9.7 0.0 31.3 0.0 34.5 120 FTG ---- PE 0.0 105 9.7 11.2 26.3 57.5 1.432. TL 3.50 PV Pipe: 17 142.1 1.536 PL 14.00 PF 10.7 105 9.7 11.2 26.3 57.5 24.6 120 FTG ---- PE 0.0 106 9.7 11.2 15.6 44.3 0.764 TL 14.00 PV Pipe: 18 97.8 1.536 PL 14.00 PF 5.4 106 9.7 11.2 15.6 44.3 16.9 120 FTG ---- PE 0.0 107 9.7 11.2 10.3 35.9 0.383 TL 14.00 PV Pipe: 19 61.9 1.536 PL 14.00 PF 2.3 107 9.7 11.2 10.3 35.9 10.7 120 FTG ---- PE 0.0 108 9.7 11.2 8.0 31.6 0.164 TL 14.00 PV Pipe: 20 30.3 1.536 PL 14.00 PF 0.6 108 9.7 11.2 8.0 31.6 5.3 120 FTG ---- PE 0.0 109 9.7 11.2 7.3 30.3 0.044 TL 14.00 PV Pipe: 21 24.4 2.203 PL 11.00 PF 0.2 1 9.7 0.0 50.6 0.0 2.1 120 FTG ET PE -2.1 1A 14.5 0.0 48.4 0.0 0.005 TL 31.46 PV Pipe: 22 24.4 1.394 PL 7.00 PF 0.5 1A 14.5 0.0 48.4 0.0 5.1 150 FTG E PE -2.2 7 19.5 0.0 45.8 0.0 0.031 TL 15.00 PV Pipe: 23 12.3 1.101 PL 91.50 PF 3.4 7 19.5 0.0 45.8 0.0 4.2 150 FTG 4T9R PE 0.0 8 19.5 0.0 42.4 0.0 0.028 TL 120.50 PV Pipe: 24 12.3 1.101 PL 107.00 PF 3.5 8 19.5 0.0 42.4 0.0 4.2 150 FTG 4T PE 0.0 9 19.5 0.0 38.9 0.0 0.028 TL 127.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 5/4/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4680.SDF JOB TITLE: LINCOLN & OAK MIXED USE BLDG. GARAGE AREA .15/1542sq.ft. (ORDINARY HAZARD, Gi) 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: 25 12.3 1.101 PL 30.00 PF 1.3 9 19.5 0.0 38.9 0.0 4.2 150 FTG 2T6R PE 0.0 10 19.5 0.0 37.6 0.0 0.028 TL 46.00 PV Pipe: 26 12.1 1.101 PL 14.00 PF 0.6 7 19.5 0.0 45.8 0.0 4.1 150 FTG E2R PE -4.3 11 29.5 0.0 40.8 0.0 0.027 TL 23.00 PV Pipe: 27 12.1 1.101 PL 80.00 PF 3.0 11 29.5 0.0 40.8 0.0 4.1 150 FTG EST PE 0.0 12 29.5 0.0 37.8 0.0 0.027 TL 112.00 PV Pipe: 28 12.1 1.101 PL 49.00 PF 1.7 12 29.5 0.0 37.8 0.0 4.1 150 FTG 3T PE 0.0 13 29.5 0.0 36.1 0.0 0.027 TL 64.00 PV Pipe: 29 0.0 1.101 PL 5.00 PF 0.0 13 29.5 0.0 36.1 0.0 0.0 150 FTG ETR PE 0.2 13A 29.0 0.0 36.3 0.0 0.000 TL 18.00 PV Pipe: 30 12.1 1.101 PL 12.50 PF 0.4 13 29.5 0.0 36.1 0.0 4.1 150 FTG 2R PE 0.0 14 29.5 0.0 35.7 0.0 0.027 TL 14.50 PV Pipe: 31 0.0 1.101 PL 4.50 PF 0.0 14 29.5 0.0 35.7 0.0 0.0 150 FTG T PE 0.0 15 29.5 0.0 35.7 0.0 0.000 TL 9.50 PV Pipe: 32 0.0 1.101 PL 15.50 PF 0.0 15 29.5 0.0 35.7 0.0 0.0 150 FTG 3ET2R PE -1.7 iSA 33.5 0.0 34.0 0.0 0.000 TL 43.50 PV Pipe: 33 0.0 1.101 PL 10.50 PF 0.0 15 29.5 0.0 35.7 0.0 0.0 150 FTG 2R PE 0.0 16 29.5 0.0 35.7 0.0 0.000 TL 12.50 PV Pipe: 34 0.0 1.101 PL 21.50 PF 0.0 16 29.5 0.0 35.7 0.0 0.0 150 FTG 3ET2R PE -4.5 16A 40.0 0.0 31.2 0.0 0.000 TL 49.50 PV Pipe: 35 0.0 1.101 PL 8.50 PF 0.0 16 29.5 0.0 35.7 0.0 0.0 150 FTG R PE 0.0 17 29.5 0.0 35.7 0.0 0.000 TL 9.50 PV Pipe: 36 0.0 1.101 PL 8.50 PF 0.0 17 29.5 0.0 35.7 0.0 0.0 150 FTG 2TR PE 0.2 17A 29.0 0.0 35.9 0.0 0.000 TL 19.50 PV Pipe: 37 0.0 1.101 PL 10.50 PF 0.0 17 29.5 0.0 35.7 0.0 0.0 150 FTG E3R PE 0.2 18A 29.0 0.0 35.9 0.0 0.000 TL 20.50 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 5/4/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4680.SDF JOB TITLE: LINCOLN & OAK MIXED USE BLDG. GARAGE AREA .15/1542sq.ft. (ORDINARY HAZARD, Gi) 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: 38 12.1 1.101 PL 59.00 PF 2.0 14 29.5 0.0 35.7 0.0 4.1 150 FTG T9R PE 0.0 19 29.5 0.0 33.7 0.0 0.027 TL 73.00 PV Pipe: 39 12.1 1.101 PL 9.00 PF 0.5 19 29.5 0.0 33.7 0.0 4.1 150 FTG E2R PE 4.3 10 19.5 0.0 37.6 0.0 0.027 TL 18.00 PV Pipe: 40 24.4 1.101 PL 11.00 PF 2.3 10 19.5 0.0 37.6 0.0 8.2 150 FTG ET PE 2.2 20A 14.5 0.0 37.5 0.0 0.099 TL 23.00 PV Pipe: 41 24.4 1.080 PL 5.50 PF 1.3 20A 14.5 0.0 37.5 0.0 8.6 120 FTG E PE 2.1 20 9.7 0.0 38.3 0.0 0.164 TL 7.80 PV Pipe: 42 24.4 1.725 PL 42.50 PF 1.1 20 9.7 0.0 38.3 0.0 3.4 120 FTG 2T PE 0.0 4 9.7 0.0 37.2 0.0 0.017 TL 64.89 PV NOTES (HASS): Calculations were performed by the HASS 8.2 computer program under license no. 16080621 granted by HRS Systems, Inc. 208 South Public Square Petersburg, TN 37144 (931) 659-9760 The system has been calculated to provide an average imbalance at each node of 0.002 gpm and a maximum imbalance at any node of 0.083 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 34.5 ft/sec at pipe 16. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. I., SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 5/4/2012 C:\PROGRAN FILES\HRS SYSTEMS\HASS82\C4680.SDF JOB TITLE: LINCOLN & OAK MIXED USE BLDG. GARAGE AREA .15/1542sq.ft. (ORDINARY HAZARD, Gi) (5) PIPE FITTINGS TABLE Pipe Table Name: FSS.PIP PAGE: * MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEii ChkViv BfyViv GatViv AimChk DPVlv NPTee 1.080 2.30 5.76 2.30 5.76 6.91 1.15 11.52 11.52 5.76 1.536 3.18 6.36 1.59 7.16 4.77 0.80 7.95 7.95 6.36 1.725 5.60 11.19 2.80 12.59 8.40 1.40 13.99 13.99 11.19 2.203 6.82 13.64 4.09 15.00 8.18 1.36 13.64 13.64 13.64 3.314 10.19 21.84 7.28 23.29 14.56 1.46 18.93 18.93 21.84 4.310 13.94 27.87 8.36 30.66 16.72 2.79 27.87 27.87 27.87 5.850 24.63 51.31 16.42 55.42 18.47 4.10 43.10 43.10 51.31 6.340 17.37 37.23 11.17 39.71 12.41 3.72 34.75 34.75 37.23 PAGE: H MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T R K C L B L Ell Tee TEERUN COUPLG EL45 1.101 7.00 5.00 1.00 0.00 1.00 1.00 0.00 1.00 1.394 8.00 6.00 1.00 0.00 1.00 2.00 0.00 2.00 I 80.OL 1 G 2 A U G E 60.0 P R E S 40.0 S U R E 20.0 p S 1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 5/4/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4680.SDF JOB TITLE: LINCOLN & OAK MIXED USE BLDG. GARAGE AREA .15/1542sq.ft. (ORDINARY HAZARD, Gi) WATER SUPPLY ANALYSIS Static: 83.70 psi Resid: 75.60 psi Flow: 1424.0 gpm 100. LEGEND Available pressure 81.80 psi @ 649.8 gpm Required pressure 73.48 psi @ 649.8 gpm Source Supply Curve System Demand Curve out I 400600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 5/4/2012 C:\PROGRAN FILES\HRS SYSTEMS\HASS82\C4680.SDF JOB TITLE: LINCOLN & OAK MIXED USE BLDG. FOUR HEAD CALC-NFPA 13R-2nd FLOOR WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) S 83.7 75.6 1424.0 83.6 163.6 68.1 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 163.6 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 63.6 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (PT) (PSI) (GPM) 5 -3.0 SOURCE 68.1 63.6 RP 3.0 -- -- 65.5 DA 3.0 -.--- 56.5 DIP -3.0 - - - - 59.0 BOR 1.0 - - - - 57.3 - - - TOR 9.7 - - - - 53.5 1 9.7 - - - - 53.3 - -- 2 9.7 - - -- 53.2 3 9.7 - - -- 53.2 - -- 4 9.7 - - - - 53.2 - - - 5 9.7 - - - - 53.2 - - - 6 9.7 - - - - 53.2 - - - 101 9.7 - - - - 53.2 - - - 102 9.7 - - - - 53.2 - - - 103 9.7 -- -- 53.2 - - - 104 9.7 - - - - 53.2 - - - 105 9.7 - - - - 53.2 - - - 105A 9.7 - - - - 53.2 - - - 106 9.7 - - - - 53.2 - - - 107 9.7 - - - - 53.2 - - - 108 9.7 - - - - 53.2 - - - 109 9.7 - - - - 53.2 - - - 1A 14.5 - -- - 50.9 7 19.5 - - - - 47.8 8 19.5 - - - - 45.9 - -- 9 19.5 - -. - - 43.9 - - - 10 19.5 - - - - 43.1 - - - 11 29.5 - - - - 40.7 - - - 12 29.5 - - - - 27.5 13 29.5 - - - - 20.0 - - - 13A 29.0 K= 4.30 19.1 18.8 14 29.5 - - - - 19.8 15 29.5 - - - - 16.9 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 5/4/2012 C:\PROGRAN FILES\HRS SYSTEMS\HASS82\C4680.SDF JOB TITLE: LINCOLN & OAK MIXED USE BLDG. FOUR HEAD CALC-NFPA 13R-2nd FLOOR NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 15A 33.5 K= 4.30 13.3 15.7 16 29.5 - - - - 15.2 - - - 16A 40.0 K= 4.30 9.1 13.0 17 29.5 - - - - 14.8 17A 29.0 K= 4.30 14.1 16.1 18A 29.0 - - - - 15.0 - - - 19 29.5 - - - - 35.1 - - - 20 9.7 -- -- 51.8 20A 14.5 - - - - 48.2 I 'I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 5/4/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4680.SDF JOB TITLE: LINCOLN & OAK MIXED USE BLDG. FOUR HEAD CALC-NFPA 13R-2nd FLOOR PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 1 63.6 5.850 PL 20.00 PF 0.0 S -3.0 SRCE 68.1 (N/A) 0.8 150 FTG TLG PE -2.6 RP 3.0 0.0 65.5 0.0 0.000 TL 128.55 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE RP 3.0 0.0 65.5 0.0 9.0 psi, 63.6 gpm DA 3.0 0.0 56.5 0.0 Pipe: 3 63.6 5.850 PL 17.50 PF 0.0 DA 3.0 0.0 56.5 0.0 0.8 150 FTG 2E PE 2.6 DIP -3.0 0.0 59.0 0.0 0.000 TL 91.93 PV Pipe: 4 63.6 6.340 PL 5.00 PF 0.0 DIP -3.0 0.0 59.0 0.0 0.6 140 FTG E PE -1.7 BOR 1.0 0.0 57.3 0.0 0.000 TL 28.11 PV Pipe: 5 63.6 4.310 PL 14.00 PF 0.1 BOR 1.0 0.0 57.3 0.0 1.4 120 FTG 2EC PE -3.8 TOR 9.7 A.0 53.5 0.0 0.001 TL 72.54 PV Pipe: 6 63.6 3.314 PL 19.00 PF 0.2 TOR 9.7 0.0 53.5 0.0 2.4 120 FTG D PE 0.0 1 9.7 0.0 53.3 0.0 0.004 TL 37.93 PV Pipe: 7 27.6 3.314 PL 33.50 PF 0.1 1 9.7 0.0 53.3 0.0 1.0 120 FTG ET PE 0.0 2 9.7 0.0 53.2 0.0 0.001 TL 65.53 PV Pipe: 8 27.6 3.314 PL 4.00 PF 0.0 2 9.7 0.0 53.2 0.0 1.0 120 FTG T PE 0.0 3 9.7 0.0 53.2 0.0 0.001 TL 25.84 PV Pipe: 9 27.6 3.314 PL 10.00 PF 0.0 3 9.7 0.0 53.2 0.0 1.0 120 FTG T PE 0.0 4 9.7 0.0 53.2 0.0 0.001 TL 31.84 PV Pipe: 10 0.0 3.314 PL 11.50 PF 0.0 4 9.7 0.0 53.2 0.0 0.0 120 FTG T PE 0.0 5 9.7 0.0 53.2 0.0 0.000 TL 33.34 PV Pipe: 11 0.0 3.314 PL 11.00 PF 0.0 5 9.7 0.0 53.2 0.0 0.0 120 FTG T PE 0.0 6 9.7 0.0 53.2 0.0 0.000 TL 32.84 PV Pipe: 12 0.0 1.536 PL 17.50 PF 0.0 5 9.7 0.0 53.2 0.0 0.0 120 FTG T PE 0.0 101 9.7 0.0 53.2 0.0 0.000 TL 23.86 PV 1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 5/4/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4680.SDF JOB TITLE: LINCOLN & OAK MIXED USE BLDG. FOUR HEAD CALC-NFPA 13R-2nd FLOOR PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 13 0.0 1.536 PL 14.00 PP 0.0 101 9.7 0.0 53.2 0.0 0.0 120 FTG ---- PE 0.0 102 9.7 0.0 53.2 0.0 0.000 TL 14.00 PV Pipe: 14 0.0 1.536 PL 14.00 PF 0.0 102 9.7 0.0 53.2 0.0 0.0 120 FTG ---- PE 0.0 103 9.7 0.0 53.2 0.0 0.000 -TL 14.00 PV Pipe: 15 0.0 1.536 PL 14.00 PF 0.0 103 9.7 0.0 53.2 0.0 0.0 120 FTG ---- PE 0.0 104 9.7 0.0 53.2 0.0 0.000 TL 14.00 PV Pipe: 15A 0.0 1.536 PL 12.00 PP 0.0 6 9.7 0.0 53.2 0.0 0.0 120 FTG T PE 0.0 105A 9.7 0.0 53.2 0.0 0.000 TL 18.36 PV Pipe: 16 0.0 1.536 PL 3.50 PF 0.0 6 9.7 0.0 53.2 0.0 0.0 120 FTG ---- PE 0.0 105 9.7 0.0 53.2 0.0 0.000 TL 3.50 PV Pipe: 17 0.0 1.536 PL 14.00 PF 0.0 105 9.7 0.0 53.2 0.0 0.0 120 FTG ---- PE 0.0 106 9.7 0.0 53.2 0.0 0.000 TL 14.00 PV Pipe: 18 0.0 1.536 PL 14.00 PF 0.0 106 9.7 0.0 53.2 0.0 0.0 120 FTG ---- PE 0.0 107 9.7 0.0 53.2 0.0 0.000 TL 14.00 PV Pipe: 19 0.0 1.536 PL 14.00 PF 0.0 107 9.7 0.0 53.2 0.0 0.0 120 FTG ---- PE 0.0 108 9.7 0.0 53.2 0.0 0.000 TL 14.00 PV Pipe: 20 0.0 1.536 PL 14.00 PP 0.0 108 9.7 0.0 53.2 0.0 0.0 120 FTG ---- PE 0.0 109 9.7 0.0 53.2 0.0 0.000 TL 14.00 PV Pipe: 21 36.0 2.203 PL 11.00 PP 0.3 1 9.7 0.0 53.3 0.0 3.0 120 FTG ET PE -2.1 1A 14.5 0.0 50.9 0.0 0.010 TL 31.46 PV Pipe: 22 36.0 1.394 PL 7.00 PF 1.0 1A 14.5 0.0 50.9 0.0 7.6 150 FTG E PE -2.2 7 19.5 0.0 47.8 0.0 0.064 TL 15.00 PV Pipe: 23 9.1 1.101 PL 91.50 PP 1.9 7 19.5 0.0 47.8 0.0 3.1 150 FTG 4T9R PE 0.0 8 19.5 0.0 45.9 0.0 0.016 TL 120.50 PV Pipe: 24 9.1 1.101 PL 107.00 PF 2.0 8 19.5 0.0 45.9 0.0 3.1 150 FTG 4T PE 0.0 9 19.5 0.0 43.9 0.0 0.016 TL 127.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 5/4/2012 C:\PROGRAN FILES\HRS SYSTEMS\HASS82\C4680.SDF JOB TITLE: LINCOLN & OAK MIXED USE BLDG. FOUR HEAD CALC-NFPA 13R-2nd FLOOR PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 25 9.1 1.101 FL 30.00 PF 0.7 9 19.5 0.0 43.9 0.0 3.1 150 FTG 2T6R PE 0.0 10 19.5 0.0 43.1 0.0 0.016 TL 46.00 PV Pipe: 26 26.9 1.101 FL 14.00 PF 2.7 7 19.5 0.0 47.8 0.0 9.1 150 FTG E2R FE -4.3 11 29.5 0.0 40.7 0.0 0.118 TL 23.00 PV Pipe: 27 26.9 1.101 FL 80.00 PF 13.2 11 29.5 0.0 40.7 0.0 9.1 150 FTG E5T FE 0.0 12 29.5 0.0 27.5 0.0 0.118 TL 112.00 PV Pipe: 28 26.9 1.101 FL 49.00 PF 7.5 12 29.5 0.0 27.5 0.0 9.1 150 FTG 3T FE 0.0 13 29.5 0.0 20.0 0.0 0.118 TL 64.00 PV Pipe: 29 18.8 1.101 FL 5.00 PF 1.1 13 29.5 0.0 20.0 0.0 6.3 150 FTG ETR FE 0.2 13A 29.0 4.3 19.1 18.8 0.061 TL 18.00 PV Pipe: 30 8.1 1.101 FL 12.50 PF 0.2 13 29.5 0.0 20.0 0.0 2.7 150 FTG 2R FE 0.0 14 29.5 0.0 19.8 0.0 0.013 TL 14.50 PV Pipe: 31 44.8 1.101 FL 4.50 PF 2.9 14 29.5 0.0 19.8 0.0 15.1 150 FTG T FE 0.0 15 29.5 0.0 16.9 0.0 0.303 TL 9.50 PV Pipe: 32 15.7 1.101 FL 15.50 PF 1.9 15 29.5 0.0 16.9 0.0 5.3 150 FTG 3ET2R FE -1.7 15A 33.5 4.3 13.3 15.7 0.043 TL 43.50 PV Pipe: 33 29.1 1.101 FL 10.50 PF 1.7 15 29.5 0.0 16.9 0.0 9.8 150 FTG 2R FE 0.0 16 29.5 0.0 15.2 0.0 0.137 TL 12.50 PV Pipe: 34 13.0 1.101 FL 21.50 PF 1.5 16 29.5 0.0 15.2 0.0 4.4 150 FTG 3ET2R FE -4.5 16A 40.0 4.3 9.1 13.0 0.031 TL 49.50 PV Pipe: 35 16.1 1.101 FL 8.50 PF 0.4 16 29.5 0.0 15.2 0.0 5.4 150 FTG R FE 0.0 17 29.5 0.0 14.8 0.0 0.046 TL 9.50 PV Pipe: 36 16.1 1.101 FL 8.50 PF 0.9 17 29.5 0.0 14.8 0.0 5.4 150 FTG 2TR FE 0.2 17A 29.0 4.3 14.1 16.1 0.046 TL 19.50 PV Pipe: 37 0.0 1.101 FL 10.50 PF 0.0 17 29.5 0.0 14.8 0.0 0.0 150 FTG E3R FE 0.2 18A 29.0 0.0 15.0 0.0 0.000 TL 20.50 FV I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 5/4/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4680.SDF JOB TITLE: LINCOLN & OAK MIXED USE BLDG. FOUR HEAD CALC-NFPA 13R-2nd FLOOR PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 38 -36.7 1.101 PL 59.00 PF 15.3 14 29.5 0.0 19.8 0.0 12.4 150 FTG T9R PE 0.0 19 29.5 0.0 35.1 0.0 0.209 TL 73.00 PV Pipe: 39 -36.7 1.101 PL 9.00 PF 3.8 19 29.5 0.0 35.1 0.0 12.4 150 FTG E2R FE 4.3 10 19.5 0.0 43.1 0.0 0.209 TL 18.00 PV Pipe: 40 -27.6 1.101 PL 11.00 PF 2.8 10 19.5 0.0 43.1 0.0 9.3 150 FTG ET PE 2.2 20A 14.5 0.0 48.2 0.0 0.124 TL 23.00 PV Pipe: 41 -27.6 1.080 PL 5.50 PF 1.6 20A 14.5 0.0 48.2 0.0 9.7 120 FTG E FE 2.1 20 9.7 0.0 51.8 0.0 0.205 TL 7.80 PV Pipe: 42 -27.6 1.725 PL 42.50 PF 1.4 20 9.7 0.0 51.8 0.0 3.8 120 FTG 2T PE 0.0 4 9.7 0.0 53.2 0.0 0.021 TL 64.89 PV NOTES (RASS): Calculations were performed by the HASS 8.2 computer program under license no. 16080621 granted by HRS Systems, Inc. 208 South Public Square Petersburg, TN 37144 (931) 659-9760 The system has been calculated to provide an average imbalance at each node of 0.002 gpm and a maximum imbalance at any node of 0.087 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 15.1 ft/sec at pipe 31. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. PAGE: H MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T R K C L Eli Tee TEERUN COUPLG EL45 1.101 7.00 5.00 1.00 0.00 1.00 1.00 1.394 8.00 6.00 1.00 0.00 1.00 2.00 B L 0.00 1.00 0.00 2.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 5/4/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4680.SDF JOB TITLE: LINCOLN & OAK MIXED USE BLDG. FOUR HEAD CALC-NFPA 13R-2nd FLOOR / (5) PIPE FITTINGS TABLE Pipe Table Name: FSS.PIP PAGE: * MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A Eli Tee LngEii ChkVlv BfyViv GatViv AimChk 1.080 2.30 5.76 2.30 5.76 6.93. 1.15 11.52 1.536 3.18 6.36 1.59 7.16 4.77 0.80 7.95 1.725 5.60 11.19 2.80 12.59 8.40 1.40 13.99 2.203 6.82 13.64 4.09 15.00 8.18 1.36 13.64 3.314 10.19 21.84 7.28 23.29 14.56 1.46 18.93 4.310 13.94 27.87 8.36 30.66 16.72 2.79 27.87 5.850 24.63 51.31 16.42 55.42 18.47 4.10 43.10 6.340 17.37 37.23 11.17 39.71 12.41 3.72 34.75 D N DPVlv NPTee 11.52 5.76 7.95 6.36 13.99 11.19 13.64 13.64 18.93 21.84 27.87 27.87 43.10 51.31 34.75 37.23 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 5/4/2012 C:\PROGRAN FILES\HRS SYSTEMS\HASS82\C4680.SDF JOB TITLE: LINCOLN & OAK MIXED USE BLDG. FOUR HEAD CALC-NFPA 13R-2nd FLOOR WATER SUPPLY ANALYSIS Static: 83.70 psi Resid: 75.60 psi Flow: 1424.0 gpm 100.( LEGEND 1 80.( Available pressure 83.55 psi @ 163.6 gpm G A U' 2 G E 60.0 P R E S 400 S U R E 20.0 p S :1. A Required pressure 68.09 psi 8 163.6 gpm Source Supply Curve System Demand Curve -14.71 I I I I I I I I I 400600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) / .0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 5/4/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4680.SDF JOB TITLE: LINCOLN & OAK MIXED USE BLDG. ONE HEAD CALC-NFPA 13R-2nd FLOOR WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) S 83.7 75.6 1424.0 83.6 121.0 53.9 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 121.0 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 21.0 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) S -3.0 SOURCE 53.9 21.0 RP 3.0 - - - - 51.3 DA 3.0 - - - - .42.3 DIP -3.0 - - - - 44.9 BOR 1.0 - - - - 43.2 TOR 9.7 - - - - 39.4 1 9.7 - - - - 39.4 2 9.7 - --- 39.4 3 9.7 - - - - 39.4 - - - 4 9.7 - - - - 39.4 - - - 5 9.7 - - - - 39.4 6 9.7 - - - - 39.4 101 9.7 - - - - 39.4 102 9.7 - - - - 39.4 - - - 103 9.7 - - - - 39.4 - - - 104 9.7 - - - - 39.4 105 9.7 - - - - 39.4 105A 9.7 - - - - 39.4 106 9.7 - - - - 39.4 - - - 107 9.7 - - - - 39.4 108 9.7 - - - - 39.4 - - - 109 97 . - - __ 39•4 1A 14.5 - - - - 37.3 7 19.5 - - - - 35.0 - - - 8 19.5 - - - - 34.7 9 19.5 - - - - 34.4 10 19.5 - - - - 34.3 11 29.5 - - - - 30.3 12 29.5 - - - - 28.7 13 29.5 - - - - 27.7 13A 29.0 - - - - 27.9 14 29.5 - - - - 27.5 15 29.5 - - - - 26.8 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 5/4/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4680.SDF JOB TITLE: LINCOLN & OAK MIXED USE BLDG. ONE HEAD CALC-NFPA 13R-2nd FLOOR NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 15A 33.5 - - - - 25.1 16 29.5 - - - - 25.9 16A 40.0 - - - - 21.3 - - - 17 29.5 - - - - 25.2 - - - 17A 29.0 - - - - 25.4 18A 29.0 K= 4.30 23.9 21.0 19 29.5 - - - - 29.5 - - - 20 9.7 - - - - 39.2 - - - 20A 14.5 - - - - 36.9 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 5/4/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4680.SDF JOB TITLE: LINCOLN & OAK MIXED USE BLDG. ONE HEAD CALC-NFPA 13R-2nd FLOOR PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 1 21.0 5.850 FL .20.00 PF 0.0 S -3.0 SRCE 53.9 (N/A) 0.3 150 FTG TLG PE -2.6 RP 3.0 0.0 51.3 0.0 0.000 TL 128.55 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE RP 3.0 0.0 51.3 0.0 9.0 psi, 21.0 gpm DA 3.0 0.0 42.3 0.0 Pipe 3 21.0 5.850 FL 17.50 PF 0.0 DA 3.0 0.0 42.3 0.0 0.3 150 FTG 2E PE 2.6 DIP -3.0 0.0 44.9 0.0 0.000 TL 91.93 PV Pipe: 4 21.0 6.340 PL 5.00 PF 0.0 DIP -3.0 0.0 44.9 0.0 0.2 . 140 FTG E PE -1.7 BOR 1.0 0.0 43.2 0.0 0.000 TL 28.11 PV Pipe: 5 21.0 4.310 PL 14.00 PF 0.0 BOR 1.0 0.0 43.2 0.0 0.5 120 FTG 2EC PE -3.8 TOR 9.7 0.0 39.4 0.0 0.000 TL 72.54 PV Pipe: 6 21.0 3.314 PL 19.00 PF 0.0 TOR 9.7 0.0 39.4 0.0 0.8 120 FTG D FE 0.0 1 9.7 0.0 39.4 0.0 0.001 TL 37.93 PV Pipe: 7 9.2 3.314 PL 33.50 PF 0.0 1 9.7 0.0 39.4 0.0 0.3 120 FTG ET FE 0.0 2 9.7 0.0 39.4 0.0 0.000 TL 65.53 PV Pipe: 8 9.2 3.314 FL 4.00 PF 0.0 2 9.7 0.0 39.4 0.0 0.3 120 FTG T PE 0.0 3 9.7 0.0 39.4 0.0 0.000 TL 25.84 PV Pipe: 9 9.2 3.314 FL 10.00 PF 0.0 3 9.7 0.0 39.4 0.0 0.3 120 FTG T FE 0.0 4 9.7 0.0 39.4 0.0 0.000 TL 31.84 PV Pipe: 10 0.0 3.314 FL 11.50 PF 0.0 4 9.7 0.0 39.4 0.0 0.0 120 FTG T PE 0.0 5 9.3 0.0 39.4 0.0 0.000 TL 33.34 PV Pipe: 11 0.0 3.314 FL 11.00 PF 0.0 5 9.7 0.0 39.4 0.0 0.0 120 FTG T PE 0.0 6 9.7 0.0 39.4 0.0 0.000 TL 32.84 PV Pipe: 12 0.0 1.536 PL 17.50 PF 0.0 5 9.7 0.0 39.4 0.0 0.0 120 FTG T FE 0.0 101 9.7 0.0 39.4 0.0 0.000 TL 23.86 PV a 10 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 5/4/2012 C:\PROGRAN FILES\HRS SYSTEMS\HASS82\C4680.SDF JOB TITLE: LINCOLN & OAK MIXED USE BLDG. ONE HEAD CALC-NFPA 13R-2nd FLOOR PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 13 0.0 1.536 PL 14.00 PF 0.0 101 9.7 0.0 39.4 0.0 0.0 120 FTG ---- PE 0.0 102 9.7 0.0 39.4 0.0 0.000 TL 14.00 PV Pipe: 14 0.0 1.536 PL 14.00 PF 0.0 102 9.7 0.0 39.4 0.0 0.0 120 FTG ---- PE 0.0 103 9.7 0.0 39.4 0.0 0.000 TL 14.00 PV Pipe: 15 0.0 1.536 PL 14.00 PF 0.0 103 9.7 0.0 39.4 0.0 0.0 120 FTG ---- PE 0.0 104 9.7 0.0 39.4 0.0 0.000 TL 14.00 PV Pipe: 15A 0.0 1.536 PL 12.00 PF 0.0 6 9.7 0.0 39.4 0.0 0.0 120 FTG T FE 0.0 105A 9.7 0.0 39.4 0.0 0.000 TL 18.36 PV Pipe: 16 0.0 1.536 FL 3.50 PF 0.0 6 9.7 0.0 39.4 0.0 0.0 120 FTG ---- FE 0.0 105 9.7 0.0 39.4 0.0 0.000 TL 3.50 PV Pipe: 17 0.0 1.536 FL 14.00 PF 0.0 105 9.7 0.0 39.4 0.0 0.0 120 FTG ---- PE 0.0 106 9.7 0.0 39.4 0.0 0.000 TL 14.00 PV Pipe: 18 0.0 1.536 PL 14.00 PF 0.0 106 9.7 0.0 39.4 0.0 0.0 120 FTG ---- PE 0.0 107 9.7 0.0 39.4 0.0 0.000 TL 14.00 PV Pipe: 19 0.0 1.536 PL 14.00 PF 0.0 107 9.7 0.0 39.4 0.0 0.0 120 FTG ---- PE 0.0 108 9.7 0.0 39.4 0.0 0.000 TL 14.00 PV Pipe: 20 0.0 1.536 PL 14.00 PF 0.0 108 9.7 0.0 39.4 0.0 0.0 120 FTG ---- PE 0.0 109 9.7 0.0 39.4 0.0 0.000 TL 14.00 PV Pipe: 21 11.8 2.203 PL 11.00 PF 0.0 1 9.7 0.0 39.4 0.0 1.0 120 FTG ET PE -2.1 1A 14.5 0.0 37.3 0.0 0.001 TL 31.46 PV Pipe: 22 11.8 1.394 FL 7.00 PF 0.1 1A 14.5 0.0 37.3 0.0 2.5 150 FTG E FE -2.2 7 19.5 0.0 35.0 0.0 0.008 TL 15.00 PV Pipe: 23 3.1 1.101 FL 91.50 PF 0.3 7 19.5 0.0 35.0 0.0 1.0 150 FTG 4T9R PE 0.0 8 19.5 0.0 34.7 0.0 0.002 TL 120.50 PV Pipe: 24 3.1 1.101 PL 107.00 FE' 0.3 8 19.5 0.0 34.7 0.0 1.0 150 FTG 4T PE 0.0 9 19.5 0.0 34.4 0.0 0.002 TL 127.00 PV 1 H' SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 5/4/2012 C:\PROGRAN FILES\HRS SYSTEMS\HASS82\C4680.SDF JOB TITLE: LINCOLN -& OAK MIXED USE BLDG. ONE HEAD CALC-NFPA 13R-2nd FLOOR PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 25 3.1 1.101 PL 30.00 PF 0.1 9 19.5 0.0 34.4 0.0 1.0 150 FTG 2T6R FE 0.0 10 19.5 0.0 34.3 0.0 0.002 TL 46.00 PV Pipe: 26 8.7 1.101 PL 14.00 PF 0.3 7 19.5 0.0 35.0 0.0 2.9 150 FTG E2R PE -4.3 11 29.5 0.0 30.3 0.0 0.015 TL 23.00 PV Pipe: 27 8.7 1.101 PL 80.00 PF 1.6 11 29.5 0.0 30.3 0.0 2.9 150 FTG E5T PE 0.0 12 29.5 0.0 28.7 0.0 0.015 TL 112.00 PV Pipe: 28 8.7 1.101 PL 49.00 PF 0.9 12 29.5 0.0 28.7 0.0 2.9 150 FTG 3T FE 0.0 13 29.5 0.0 27.7 0.0 0.015 TL 64.00 PV Pipe: 29 0.0 1.101 PL 5.00 PF 0.0 13 29.5 0.0 27.7 0.0 0.0 150 FTG ETR PE 0.2 13A 29.0 0.0 27.9 0.0 0.000 TL 18.00 PV Pipe: 30 8.7 1.101 FL 12.50 PF 0.2 13 29.5 0.0 27.7 0.0 2.9 150 FTG 2R PE 0.0 14 29.5 0.0 27.5 0.0 0.015 TL 14.50 PV Pipe: 31 21.0 1.101 PL 4.50 PF 0.7 14 29.5 0.0 27.5 0.0 7.1 150 FTG T PE 0.0 15 29.5 0.0 26.8 0.0 0.074 TL 9.50 PV Pipe: 32 0.0 1.101 PL 15.50 PF 0.0 15 29.5 0.0 26.8 0.0 0.0 150 FTG 3ET2R FE -1.7 15A 33.5 0.0 25.1 0.0 0.000 TL 43.50 PV Pipe: 33 21.0 1.101 FL 10.50 PF 0.9 15 29.5 0.0 26.8 0.0 7.1 150 FTG 2R FE 0.0 16 29.5 0.0 25.9 0.0 0.074 TL 12.50 PV Pipe: 34 0.0 1.101 FL 21.50 PF 0.0 16 29.5 0.0 25.9 0.0 0.0 150 FTG 3ET2R PE -4.5 16A 40.0 0.0 21.3 0.0 0.000 TL 49.50 PV Pipe: 35 21.0 1.101 FL 8.50 PF 0.7 16 29.5 0.0 25.9 0.0 7.1 150 FTG R PE 0.0 17 29.5 0.0 25.2 0.0 0.074 TL 9.50 PV Pipe: 36 0.0 1.101 FL 8.50 PF 0.0 17 29.5 0.0 25.2 0.0 0.0 150 FTG 2TR FE 0.2 17A 29.0 0.0 25.4 0.0 0.000 TL 19.50 PV Pipe: 37 21.0 1.101 FL 10.50 FE' 1.5 17 29.5 0.0 25.2 0.0 7.1 150 FTG E3R FE 0.2 18A 29.0 4.3 23.9 21.0 0.074 TL 20.50 PV 1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 5/4/2012 C:\PROGRAN FILES\HRS SYSTEMS\HASS82\C4680.SDF JOB TITLE: LINCOLN & OAK MIXED USE BLDG. ONE HEAD CALC-NFPA 13R-2nd FLOOR PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT). SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 38 -12.3 1.101 PL 59.00 PF 2.0 14 29.5 0.0 27.5 0.0 4.1 150 FTG T9R PE 0.0 19 29.5 0.0 29.5 0.0 0.028 TL 73.00 PV Pipe: 39 -12.3 1.101 PL 9.00 PF 0.5 19 29.5 0.0 29.5 0.0 4.1 150 FTG E2R PE 4.3 10 19.5 0.0 34.3 0.0 0.028 TL 18.00 PV Pipe: 40 -9.2 1.101 PL 11.00 PF 0.4 10 19.5 0.0 34.3 0.0 3.1 150 FTG ET PE 2.2 20A 14.5 0.0 36.9 0.0 0.016 TL 23.00 PV Pipe: 41 -9.2 1.080 PL 5.50 PF 0.2 20A 14.5 0.0 36.9 0.0 3.2 120 FTG E PE 2.1 20 9.7 0.0 39.2 0.0 0.027 TL 7.80 PV Pipe: 42 -9.2 1.725 PL 42.50 PF 0.2 20 9.7 0.0 39.2 0.0 1.3 120 FTG 2T PE 0.0 4 9.7 0.0 39.4 0.0 0.003 TL 64.89 PV NOTES (HASS): Calculations were performed by the HASS 8.2 computer program under license no. 16080621 granted by HRS Systems, Inc. 208 South Public Square Petersburg, TN 37144 (931) 659-9760 The system has been calculated to provide an average imbalance at each node of 0.003 gpm and a maximum imbalance at any node of 0.117 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 7.1 ft/sec at pipe 37. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. / SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 5/4/2012 C:\PROGRAN FILES\HRS SYSTEMS\HASS82\C4680.SDF JOB TITLE: LINCOLN & OAK MIXED USE BLDG. ONE HEAD CALC-NFPA 13R-2nd FLOOR (5) PIPE FITTINGS TABLE Pipe Table Name: FSS.PIP PAGE: * MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEii ChkViv BfyViv GatViv AimChk DPVlv NPTee 1.080 2.30 5.76 2.30 5.76 6.91 1.15 11.52 11.52 5.76 1.536 3.18 6.36 1.59 7.16 4.77 0.80 7.95 7.95 6.36 1.725 5.60 11.19 2.80 12.59 8.40 1.40 13.99 13.99 11.19 2.203 6.82 13.64 4.09 15.00 8.18 1.36 13.64 13.64 13.64 3.314 10.19 21.84 7.28 23.29 14.56 1.46 18.93 18.93 21.84 4.310 13.94 27.87 8.36 30.66 16.72 2.79 27.87 27.87 27.87 5.850 24.63 51.31 16.42 55.42 18.47 4.10 43.10 43.10 51.31 6.340 17.37 37.23 11.17 39.71 12.41 3.72 34.75 34.75 37.23 PAGE: H MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T R K C L B L Eli Tee TEERUN COUPLG EL45 1.101 7.00 5.00 1.00 0.00 1.00 1.00 0.00 1.00 1.394 8.00 6.00 1.00 0.00 1.00 2.00 0.00 2.00 ) I '1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 5/4/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4680.SDF JOB TITLE: LINCOLN & OAK MIXED USE BLDG. ONE HEAD CALC-NFPA 13R-2nd FLOOR WATER SUPPLY ANALYSIS Static: 83.70 psi Resid: 75.60 psi Flow: 1424.0 gpm LEGEND Available pressure 83.62 psi @ 121.0 gpm G A 1A Required pressure U 53.91 psi @ 121.0 gpm G E 60.0 A. Source Supply Curve P 2 B. System Demand Curve R E S 40.0 S U R E 20.0 p S 1 I 400600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) 100. 1 80.( Contractor's Material and Test Certificate for Aboveground Pipi PROCEDURE AS I O5i Upon completion of work, inspection and tests shall be made by the Contractor's representative and witnessed by an owner's representative. All defects shall be corrected and system left in service before contractor's personnel finally leave the job. A certificate shall be filled out and signed by both representatives. Copies shall be prepared for approving authorities, owners, and contractor. It is understood the owner's representative's signature in no way prejudices any claim against contractor for faulty material, poor workmanship, or failure to comply with approving authority's requirements or local ordinances. PROPERTY ADDRESS 3112 LINCOLN STREET ACCEPTED BY APPROVING AUTHORITIES (NAMES) CARLSBAD FIRE DEPT. ADDRESS 3112 PLANS INSTALLATION CONFORMS TO ACCEPTED PLANS EQUIPMENT USED IS APPROVED IF NO, EXPLAIN DEVIATIONS EYES 0 N YES ONO INSTRUCTIONS HAS PERSON IN CHARGE OF FIRE EQUIPMENT BEEN INSTRUCTED AS TO LOCATION 19 YES OF CONTROL VALVES AND CARE AND MAINTENANCE OF THEIS NEW EQUIPMENT? IF NO, EXPLAIN U NO HAVE COPIES OF THE FOLLOWING BEEN LEFT ON THE PREMISES 0 YES SYSTEM COMPONENTS INSTRUCTIONS 0 YES CARE AND MAINTENANCE INSTRUCTIONS 0 YES NFPA25 DYES 0 NO U NO 0 NO ONO LOCATION SUPPLIES BUILDINGS SPRINKLERS MAKE MODEL YEAR OF MANUFACTURE ORIFICE SIZE QUANTITY TEMPERATURE RATING Reliable J112 ECOH QR 2012 314 56 200 Reliable FIFR56 2012 112 41 200 Reliable F156 2012 12 12 155 Reliable I RFC 43 2012 1/2 1 192 1 165 PIPE AND FITTINGS TYPE OF PIPE STEEL and CPVC TYPE OF FITTINGS STEEL and CPVC ALARM VALVE OR FLOW INDICATOR ALARM DEVICE MAXIMUM TIME TO OPERATE THROUGH TEST CONNECTION TYPE I MAKE MODEL MIN SEC Flow I SYSTEM SENSOR WFD SERIES - 45 DRY PIPE OPERATING TEST MAKE MODEL SERIAL NO. MAKE MODEL SERIAL NO. TIME TO TRIP THROUGH TEST CONNECTION WATER PRESSURE AIR TRIP PRESSURE AIR POINT PRESSURE TIME WATER REACHED TEST OUTLET ALARM OPERATED PROPERLY MIN SEC I PSI PSI PSI MIN SEC YES I NO WITH Q.O.D. W/O Q.O.D. IF NO, EXPLAIN DELUGE & PREACTION VALVES OPERATION El PNEUMATIC El ELECTRIC El HYDRAULIC PIPING SUPERVISED El YES El NO DETECTING MEDIA SUPERVISED El YES El NO DOES THE VALVE OPERATE FROM THE MANUAL TRIP AND/OR REMOTE CONTROL STATIONS El YES El NO IS THERE AN ACCESSIBLE FACILITY IN EACH CIRCUIT IF NO, EXPLAIN FOR TESTING? El YES El NO MAKE MODE J DOES EACH CIRCUIT OPERATE SUPERVISION LOSS ALARM DOES EACH CIRCUIT OPERATE VALVE RELEASE MAXIMUM TIME TO OPERATE RELEASE YES NO YES NO MIN I SEC PRESSURE I LOCATION MAKE & SETTING STATIC PRESSURE RESIDUAL PRESSURE FLOW RATE REDUCING & FLOOR MODEL (FLOWING) VALVE TEST INLET (PSI) OUTLET (PSI) INLET (PSI) OUTLET (PSI) FLOW (GPM) CQ1? tTIJE COPY TEST DESCRIPTION HYDROSTATIC: Hydrostatic tests shall be made at not less than 2(0 psi (13.6 bars) for two hours or 50 psi (3.4 bars) above static pressure in excess of 150 psi (10.2 bars) for two hours. Differential dry-pipe valve clappers shall be left open during test to prevent damage. All aboveground piping leakage shall be stopped. PNEUMATIC: Establish 40 psi (2.7 bars) air pressure and measure drop, which shall not exceed 1Y2 psi (0.1 bars) in 24 hours. Test pressure tanks at normal water level and air pressure and measure air pressure drop which shall not exceed 11/2 psi in 24 hours. ALL PIPING HYDROSTATICALLY TESTED AT 200 PSI FOR 2 HOURS IF No; STATE REASON DRY PIPING PNEUMATICALLY TESTED 0 YES 0 NO EQUIPMENT OPERATES PROPERLY YES El NO DO YOU CERTIFY AS THE SPRINKLER CONTRACTOR THAT ADDITIVES AND CORROSIVE CHEMICALS, SODIUM SILICATE OR DERIVATIVES OF SODIUM SILICATE, BRINE, OR OTHER CORROSIVE CHEMICALS WERE NOT USED FOR TESTING SYSTEMS OR STOPPING LEAKS? R YES El NO DRAIN READING OF GAGE LOCATED NEAR WATER._ RESIDUAL PRESSURE WITH VALVE IN TEST TESTS TEST SUPPLY TEST CONNECTION PSI 7 > CONNECTION OPEN WIDE PSI 7o UNDERGROUND MAINS AND LEAD-IN CONNECTIONS TO SYSTEM RISERS FLUSHED BEFORE CONNECTION MADE TO SPRINKLER PIPING. VERIFIED BY COPY OF THE U FORM NO. 858 0 YES 0 NO OTHER EXPLAIN FLUSHED BY INSTALLER OF UNDERGROUND SPRINKER PIPING E51 YES DNO IF POWDER DRIVEN FASTENERS ARE USED IN CONCRETE IF NO, EXPLAIN HAS REPRESENTATIVE SAMPLE TESTING BEEN COMPLETED? El YES FI ND BLANK TEST NUMBER USED LOCATIONS NUMBER REMOVED GASKETS WELDED PIPING R YES El NO IF YES... DO YOU CERTIFY AS THE SPRINKLER CONTRACTOR THAT WELDING PROCEDURES COMPLY WITH THE REQUIREMENTS OF AT LEAST AWS D1 0.9. LEVEL AR 3? YES 0 NO DO YOU CERTIFY THAT THE WELDING WAS PERFORMED BY WELDERS QUALIFIED IN COMPLIANCE WELDING WITH THE REQUIREMENTS OF AT LEAST AWS D1 0.9. LEVEL AR 3? YES 0 NO DO YOU CERTIFY THAT WELDING WAS CARRIED OUT IN COMPLIANCE WITH A DOCUMENTED QUALITY CONTROL PROCEDURE TO INSURE THAT ALL DISCS ARE RETRIEVED, THAT OPENINGS IN PIPING ARE SMOOTH, THAT SLAG AND OTHER WELDING RESIDUE ARE REMOVED, AND THAT THE INTERNAL DIAMETERS OF PIPING ARE NOT PENETRATED? R YES El NO CUTOUTS DO YOU CERTIFY THAT YOU HAVE A CONTROL FEATURE TO ENSURE THAT ALL CUTOUTS (DISCS) (DISCS) ARE RETRIEVED? El YES El NO HYDRAULIC NAMEPLATE PROVIDED IF NO, EXPLAIN DATA NAMEPLATE ,..j,1j EYES [I NO DATE LEFT IN SERVICE WITH ALL CONTROL VALVES OPEN. REMARKS NAME OF SPRINKER CONTRACTOR: Innovative Fire Protection, Inc. 17 SIGNATURES TESTS WITNESSED BY FOR PROP RTY OWNER NED TITLE DATE FOR SPRINKLE O , IGNED) ADDITIONAL EXPLANATIONS 71) NOTES: -- Carlsbad Municipal Water District Potable Water Discharge Event Report Date: /i le Event: 14_ C0 N STP, mt: Initial ains t4 IA Estimated Discharge Flow: JC/Z 57 &('M and 11u5h1n9 JPc Start Time Discharge 1k End Time Pre-Dechiorinatlon Residual: 0. 1 Clear flow path ofj debris, surface contaminants materials. Do noti remove native an or hazardous (less than 0.1 mg/L) Post-DechlorInation Residual: 0. Qj.7 vegetation. I p11 within limits Of 6.0 and 9.0 Eroslofl control, ife. sandbgs, slit fércing, hay bales, gravel bags, decrasiflg the velocity of discharge watr. Upon completlonf of dewatering, ensure that the flow pauj Is-free of all temporary erosioi prevention materials. Upon completlor I of dewatering, ensure that any sedimer t or silted areas are cleared. Waté Sampling Performed by:____________________________________________ Comments: Submittc i by: Reviewd by: (Name & Date) (Name & Date) Reason for Type of Dewatering Watt Note: Indudes flow te Dewateiing Res Unscheduled W ..-..t_ 'a. Flow Test Record Test Hydrant Location I AL A"(4f, Hydrant-11) Ni . Size Main____________ Static............ Residual....... Pressure Drop. ________(PDI 1).....K factor for PDI .1 Hydrant I loci tion C?A'k A.1EtW. Hydrant 2 bc tion OA6 JBp.iU. Hydrant 3 bc tion Hydrant 1 Pitc t PSI GPM:4-4 Size of Orifice Z2. Hydrant 2 Pitc t PSI GPM: Size of Orifice__________ Hydrant 3 Pit' t PSI GPM: Size of Orifice.__________ Total:_______ (Q) Calculated tea and flow data - 0 x PD2 k =Q2 PDIk Static: Desired Resid ial ....... 20 Pressure Drop (PD 2).. K factor PD 2: x divided by equals GPM at 20 psi residual Qi PD2k PD1k Q2 Comments:_ Test conducte I for•: ~~_Ascw f Conducted by 1 Aid 'C- Date: 1HL4III?. Time :4AM: