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• McKinstry Fire Protection 5400 NE Columbia. Portland, OR 97218 Hydraulic Calculations for Romano's Macaroni Grill Tigard, Or Contract Number:7278 Date: 01/26/96 9:16 AM -Design Data- Occupancy Classification: {Light Hazard} Density: {.10} Area of Application: {1500 Sq Ft} Coverage per Sprinkler: {225} Max. SQ. FT. Number of Sprinklers Calculated: {16} Total Sprinkler Water Flow Required: {315.2} Total Water Required(Including Hose): {415.2} Flow and Pressure(@ BOR): {315.2 GPM @ 36.6 PSI) Sprinkler Orifice Size: 1/2 inch Name of Contractor: McKinstry Co Designer: Richard A. Gordon Jr. Authority Having Jurisdiction: City of TUALATIN Calculations by HASS Computer Program HRS Systems, Inc. Atlanta, GA The issuance of a permit based on the plans, specifications, and other data shall not prevent the Building RECEIVEOfficial from C''YOF 'U `A I � thereafter requiring the correction of errors in said plans, specifications and other data, or from preventing building DEC 1 3 2004 operations being carried on there under when in violation of this code or any other ordinances of this jurisdiction. ENGINEERING & See Section 105.3.1 of IBC. BUILDING DEPARTMENT By Permit No. JOB: � , /�S try ROMANOS MACARONI GRILL TIGARD, OR WATER FLOW TEST: SYSTEM DEMAND: DATE: 11-5 STATIC: 55 G.P.M.: RESIDUAL: 32 P.S.I.: SPRINKLER CALC. BY:RAG G.P.M.: 2049 SYSTEM: JOB #: 7278 SCALE: A 175 170 = 165 160 155 150 145 140 135 130 125 120 = 115 : 110 105 100 d 95_ � 90 to 85 w 80 75 70 65: 60 STATIC ss E. LOW @ 50 PSI = 538 54 50 45- ao = RESIDUAL 32 0 2049 35 30 25] _ 20 15 10 = 5. 0 1.85 GPM i i nn ilii i111 1 1 1i i i i i i i i i i i i i i i i i a 1 1 1 1 1 1 1 1 1 1iiiiiiii � i i � � i i � i i i i i i i � � i i i i i i i i i i ANA. 0 £00 100 000 000 1000 If00 I I Scale C 400 800 1200 1600 2000 2400 2800 3200 3600 4000 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE : 12/8/2004 C: \HASS DATA\ROMANOS\LIGHT HAZARD. SDF JOB TITLE: ROMANOS MACARONI GRILL WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ' D NODE PRESS . PRESS. @ PRESS . @ DEMAND PRESS . TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SOURCE 54 . 0 50 . 0 838 . 0 52 . 9 415 . 2 44 . 6 AGGREGATE FLOW ANALYSIS : TOTAL FLOW AT SOURCE 415 . 2 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100 . 0 GPM OTHER HOSE STREAM ALLOWANCES 0 . 0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 315 . 2 GPM NODE ANALYSIS DATA PRESSURE NODE TAG ELEVATION NODE TYPE TOTAL NORMAL DISCHARGE (FT) (PSI) (PSI) (GPM) 1 12 . 5 K= 5 . 30 9 . 3 9. 3 16. 1 1A 13 . 5 - - - - 9. 2 8 . 9 - - - 5 10 . 8 K= 5 . 30 10. 9 10. 9 17 . 5 5A 13 . 5 - - - - 10 . 2 9. 2 - - - 10 9 . 5 K= 5 . 30 12 . 7 12 . 7 18 . 9 10A 13 . 5 - - - - 11. 5 10. 6 - - - 15 12 . 0 K= 5 . 30 12 . 6 12 . 6 18 . 8 15A 13 . 5 - - - - 12 . 2 10 . 6 - - - 20 9 . 5 K= 5 . 30 17 . 4 17 . 4 22 . 1 20A 13 . 5 - - - - 16. 2 14 . 8 - - - 25 12 . 0 K= 5 . 30 16. 8 16. 8 21 . 7 25A 13 . 5 - - - - 16. 4 15 . 6 - - - 30 10 . 8 K= 5 . 30 10 . 2 10 . 2 16. 9 30A 13 . 5 - - - - 9. 5 9.2 - - - 35 12 . 0 K= 5 . 30 11. 5 11 . 5 18 . 0 35A 13 . 5 - - - - 11 . 3 10 . 2 - - - 40 9. 5 K= 5 . 30 18 . 3 18 . 3 22 . 7 40A 13 . 5 - - - - 17 . 1 16. 1 - - - 40B 13 . 5 - - - - 19. 8 19 . 2 - - - 45 9 . 5 K= 5 . 30 10 . 0 10 . 0 16. 8 45A 13 . 5 - - - - 8 . 6 8 . 3 - - - 50 9. 5 K= 5 . 30 11 . 4 11 . 4 17 . 9 50A 13 . 5 - - - - 9. 8 8 . 7 - 55 10 . 8 K= 5 . 30 11 .2 11 . 2 17 . 8 55A 13 . 5 - - - - 10 . 5 9 . 6 - - - 60 9 . 5 K= 5 . 30 13 . 7 13 . 7 19 . 6 60A 13 . 5 - - - - 12 . 4 10 . 7 - - - 65 9 . 5 K= 5 . 30 17 . 9 17 . 9 22 . 4 65A 13 . 5 - - - - 16. 3 14 . 8 - - - 65B 13 . 5 - - - - 19 . 4 18 . 8 - - - 70 13 . 5 K= 5 . 60 18 . 3 18 . 3 24 . 0 75 13 . 5 K= 5 . 60 18 . 8 18 . 1 23 . 8 75A 13 . 5 - - - - 20 . 7 20 . 3 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 12/8/2004 C: \HASS DATA\ROMANOS\LIGHT HAZARD. SDF JOB TITLE: ROMANOS MACARONI GRILL NODE ANALYSIS DATA PRESSURE NODE TAG ELEVATION NODE TYPE TOTAL NORMAL DISCHARGE (FT) (PSI) (PSI) (GPM) 100 11 . 7 - - - - 22 . 1 22 . 0 - - - 105 11 . 7 - - - - 22 . 2 22 . 0 - - - 110 11 . 7 - - - - 22 . 5 21 . 8 - - - 115 11 . 7 - - - - 22 . 9 21 . 9 - - - 200 13 . 5 - - - - 19. 9 19 . 1 - - - 205 13 . 5 - - - - 21 . 1 20 . 9 - - - 210 13 . 5 - - - - 20 . 7 20 . 2 - - - 215 13 . 5 - - - - 21. 8 21 . 7 - - - TOR 11 . 0 - - - - 30 . 2 29 . 2 - - - BOR 1 . 0 - - - - 36. 6 36. 5 - - - DCOUT -3 . 0 - - - - 38 . 6 38 . 6 - - - DCIN -3 . 0 - - - - 44 . 6 44 . 6 - - - SOURCE -3 . 0 SOURCE 44 . 6 44 . 6 315 . 2 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 . DATE : 12/8/2004 C: \HASS DATA\ROMANOS\LIGHT HAZARD. SDF JOB TITLE : ROMANOS MACARONI GRILL PIPE DATA PIPE TAG Q (GPM) DIA(IN) LENGTH PRESS . END ELEV. PT PN DISC. VEL (FPS) HW (C) (FT) SUM. NODES (FT) (PSI) (PSI) (GPM) FL/FT (PSI) Pipe: 1 16 . 1 1 . 049 PL 3 . 67 PF 0 . 3 1A 13 . 5 9.2 8 . 9 0 . 0 6. 0 120 FTG ---- PE 0 . 4 1 12 . 5 9 . 3 9. 3 16 . 1 0 . 087 TL 3 . 67 PV 0 . 2 Pipe: 1A 16. 1 1 . 049 PL 12 . 33 PF 1 . 1 5A 13 . 5 10 .2 9. 2 0 . 0 6. 0 120 FTG ---- PE 0 . 0 1A 13 . 5 9 .2 8 . 9 0 . 0 0 . 087 TL 12 . 33 PV 0 . 2 Pipe : 5 17 . 5 1 . 049 PL 4 . 83 PF 0 . 5 5A 13 . 5 10 .2 9. 2 0 . 0 6. 5 120 FTG ---- PE 1 . 2 5 10 . 8 10 . 9 10. 9 17 . 5 0 . 102 TL 4 . 83 PV 0 . 3 ....._...... Pipe : 5A 33 . 6 1 . 049 PL 3 . 58 PF 1 . 2 10A 13 . 5 11 . 5 10 . 6 0 . 0 12 . 5 120 FTG ---- PE 0 . 0 5A 13 . 5 10 .2 9. 2 0 . 0 0 . 340 TL 3 . 58 PV 1 . 0 Pipe: 10 18 . 9 1 . 049 PL 3 . 92 PF 0 . 5 10A 13 . 5 11 . 5 10. 6 0 . 0 7 . 0 120 FTG ---- PE 1 . 7 10 9. 5 12 . 7 12 . 7 18 . 9 0. 117 TL 3 . 92 PV 0 . 3 Pipe : 10A 52 . 5 1 . 380 PL 3 . 42 PF 0 . 7 15A 13 . 5 12 .2 10. 6 0 . 0 11 . 3 120 FTG ---- PE 0 . 0 10A 13 . 5 11 . 5 10 . 6 0 . 0 0 . 204 TL 3 . 42 PV 0 . 9 Pipe : 15 18 . 8 1 . 049 PL 1 . 75 PF 0 . 2 15A 13 . 5 12 .2 10 . 6 0 . 0 7 . 0 120 FTG ---- PE 0 . 6 15 12 . 0 12 . 6 12 . 6 18 . 8 0 . 116 TL 1 . 75 PV 0 . 3 Pipe: 15A 71 . 4 1 . 380 PL 11 . 33 PF 4 . 1 20A 13 . 5 16. 2 14 . 8 0 . 0 15 . 3 120 FTG ---- PE 0 . 0 15A 13 . 5 12 .2 10. 6 0 . 0 0. 360 TL 11 . 33 PV 1 . 6 Pipe : 20 22 . 1 1 . 049 PL 3 . 83 PF 0 . 6 20A 13 . 5 16. 2 14 . 8 0 . 0 8 . 2 120 FTG ---- PE 1 . 7 20 9. 5 17 . 4 17 . 4 22 . 1 0. 156 TL 3 . 83 PV 0 . 5 Pipe : 20A 93 . 4 1 . 610 PL 0 . 75 PF 0 . 2 25A 13 . 5 16. 4 15 . 6 0 . 0 14 . 7 120 FTG ---- PE 0 . 0 20A 13 . 5 16. 2 14 . 8 0 . 0 0 . 280 TL 0 . 75 PV 1 . 5 Pipe: 25 21 . 7 1 . 049 PL 1 . 75 PF 0 . 3 25A 13 . 5 16. 4 15 . 6 0 . 0 8 . 1 120 FTG ---- PE 0 . 6 25 12 . 0 16. 8 16. 8 21 . 7 0 . 152 TL 1 . 75 PV 0 . 4 Pipe: 25A 115 . 2 2 . 067 PL 18 . 17 PF 3 . 4 200 13 . 5 19. 9 19. 1 0 . 0 11 . 0 120 FTG T PE 0 . 0 25A 13 . 5 16. 4 15 . 6 0 . 0 0. 122 TL 28 . 17 PV 0 . 8 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 12/8/2004 C: \HASS DATA\ROMANOS\LIGHT HAZARD. SDF JOB TITLE: ROMANOS MACARONI GRILL PIPE TAG Q (GPM) DIA(IN) LENGTH PRESS . END ELEV. PT PN DISC. VEL (FPS) HW (C) (FT) SUM. NODES (FT) (PSI) (PSI) (GPM) FL/FT (PSI) Pipe : 30 16. 9 1 . 049 PL 4 . 08 PF 0 . 4 30A 13 . 5 9. 5 9. 2 0 . 0 6. 3 120 FTG ---- PE 1 . 2 30 10 . 8 10 . 2 10 . 2 16. 9 0 . 096 TL 4 . 08 PV 0 . 3 Pipe : 30A 16. 9 1 . 049 PL 19.25 PF 1 . 8 35A 13 . 5 11 . 3 10 . 2 0 . 0 6. 3 120 FTG ---- PE 0 . 0 30A 13 . 5 9 . 5 9 . 2 0 . 0 0 . 096 TL 19 . 25 PV 0 . 3 Pipe: 35 18 . 0 1 . 049 PL 3 . 75 PF 0 . 4 35A 13 . 5 11 . 3 10. 2 0 . 0 6. 7 120 FTG ---- PE 0 . 6 35 12 . 0 11 . 5 11 . 5 18 . 0 0 . 107 TL 3 . 75 PV 0. 3 Pipe: 35A 35 . 0 1 . 049 PL 15 . 83 PF 5 . 8 40A 13 . 5 17 . 1 16. 1 0 . 0 13 . 0 120 FTG ---- PE 0 . 0 35A 13 . 5 11 . 3 10 . 2 0. 0 0. 365 TL 15 . 83 PV 1 . 1 Pipe : 40 22 . 7 1 . 049 PL 3 . 00 PF 0 . 5 40A 13 . 5 17 . 1 16. 1 0. 0 8 . 4 120 FTG ---- PE 1 . 7 40 9 . 5 18 . 3 18 . 3 22 . 7 0 . 164 TL 3 . 00 PV 0 . 5 Pipe : 40A 57 . 6 1 . 380 PL 11 . 08 PF 2 . 7 40B 13 . 5 19. 8 19. 2 0 . 0 12 . 4 120 FTG ---- PE 0 . 0 40A 13 . 5 17 . 1 16. 1 0 . 0 0. 242 TL 11 . 08 PV 1 . 0 Pipe : 40B 57 . 6 1 . 610 PL 3 .25 PF 1 . 3 205 13 . 5 21 . 1 20. 9 0 . 0 9 . 1 120 FTG T PE 0 . 0 40B 13 . 5 19. 8 19. 2 0 . 0 0 . 114 TL 11 . 25 PV 0 . 6 Pipe : 45 16. 8 1 . 049 PL 2 . 75 PF 0 . 3 45A 13 . 5 8 . 6 8 . 3 0 . 0 6. 2 120 FTG ---- PE 1 . 7 45 9 . 5 10 . 0 10. 0 16. 8 0. 094 TL 2 . 75 PV 0 . 3 Pipe : 45A 16. 8 1 . 049 PL 13 . 09 PF 1 . 2 50A 13 . 5 9 . 8 8 . 7 0 . 0 6. 2 120 FTG ---- PE 0 . 0 45A 13 . 5 8 . 6 8 . 3 0. 0 0 . 094 TL 13 . 09 PV 0. 3 Pipe: 50 17 . 9 1 . 049 PL 1 . 08 PF 0 . 1 50A 13 . 5 9 . 8 8 . 7 0 . 0 6. 7 120 FTG ---- PE 1 . 7 50 9 . 5 11 . 4 11. 4 17 . 9 0 . 106 TL 1 . 08 PV 0 . 3 Pipe : 50A 34 . 7 1 . 049 PL 1 . 92 PF 0 . 7 55A 13 . 5 10 . 5 9. 6 0 . 0 12 . 9 120 FTG ---- PE 0 . 0 50A 13 . 5 9 . 8 8 . 7 0 . 0 0 . 361 TL 1 . 92 PV 1 . 1 Pipe : 55 17 . 8 1 . 049 PL 4 . 00 PF 0 . 4 55A 13 . 5 10 . 5 9. 6 0 . 0 6. 6 120 FTG ---- PE 1 . 2 55 10 . 8 11 . 2 11. 2 17 . 8 0 . 105 TL 4 . 00 PV 0 . 3 Pipe : 55A 52 . 5 1 . 380 PL 9. 08 PF 1 . 9 60A 13 . 5 12 . 4 10. 7 0 . 0 11. 3 120 FTG ---- PE 0 . 0 55A 13 . 5 10 . 5 9. 6 0 . 0 0 .204 TL 9. 08 PV 0 . 9 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 . DATE: 12/8/2004 C: \HASS DATA\ROMANOS\LIGHT HAZARD. SDF JOB TITLE: ROMANOS MACARONI GRILL PIPE TAG Q (GPM) DIA(IN) LENGTH PRESS . END ELEV. PT PN DISC. VEL (FPS) HW (C) (FT) SUM. NODES (FT) (PSI) (PSI) (GPM) FL/FT (PSI) Pipe : 60 19 . 6 1 . 049 PL 2 . 92 PF 0 . 4 60A 13 . 5 12 . 4 10 . 7 0 . 0 7 . 3 120 FTG ---- PE 1 . 7 60 9. 5 13 . 7 13 . 7 19 . 6 0 . 126 TL 2 . 92 PV 0. 4 Pipe : 60A 72 . 1 1 . 380 PL 10 . 75 PF 3 . 9 65A 13 . 5 16. 3 14 . 8 0 . 0 15 . 5 120 FTG ---- PE 0 . 0 60A 13 . 5 12 . 4 10 . 7 0 . 0 0 . 367 TL 10 . 75 PV 1 . 6 Pipe : 65 22 . 4 1 . 049 PL 1 . 08 PF 0 . 2 65A 13 . 5 16. 3 14 . 8 0 . 0 8 . 3 120 FTG ---- PE 1 . 7 65 9 . 5 17 . 9 17 . 9 22 . 4 0 . 160 TL 1 . 08 PV 0 . 5 Pipe : 65A 94 . 5 1 . 610 PL 10 . 75 PF 3 . 1 65B 13 . 5 19 . 4 18 . 8 0 . 0 14 . 9 120 FTG ---- PE 0 . 0 65A 13 . 5 16. 3 14 . 8 0 . 0 0 . 286 TL 10 . 75 PV 1 . 5 Pipe : 65B 94 . 5 2 . 067 PL 6. 17 PF 1 . 4 210 13 . 5 20 . 7 20 . 2 0 . 0 9 . 0 120 FTG T PE 0 . 0 65B 13 . 5 19 . 4 18 . 8 0 . 0 0 . 085 TL 16. 17 PV 0 . 5 Pipe: 70 24 . 0 1 . 380 PL 10 . 75 PF 0 . 5 75 13 . 5 18 . 8 18 . 1 23 . 8 5 . 1 120 FTG ---- PE 0 . 0 70 13 . 5 18 . 3 18 . 3 24 . 0 0 . 048 TL 10 . 75 PV 0 . 2 Pipe : 75 47 . 8 1 . 380 PL 10 . 75 PF 1 . 8 75A 13 . 5 20 . 7 20 . 3 0 . 0 10 . 3 120 FTG ---- PE 0 . 0 75 13 . 5 18 . 8 18 . 1 23 . 8 0 . 172 TL 10 . 75 PV 0 . 7 Pipe: 75A 47 . 8 1 . 610 PL 6. 17 PF 1 . 1 215 13 . 5 21 . 8 21 . 7 0 . 0 7 . 5 120 FTG T PE 0 . 0 75A 13 . 5 20 . 7 20 . 3 0 . 0 0 . 081 TL 14 . 17 PV 0 . 4 Pipe : 200 115 . 2 2 . 067 PL 1 . 83 PF 1 . 4 100 11 . 7 22 . 1 22 . 0 0 . 0 11 . 0 120 FTG T PE -0 . 8 200 13 . 5 19 . 9 19. 1 0 . 0 0. 122 TL 11 . 83 PV 0 . 8 Pipe : 205 57 . 6 2 . 067 PL 1 . 83 PF 0 . 4 105 11 . 7 22 . 2 22 . 0 0 . 0 5 . 5 120 FTG T PE -0 . 8 205 13 . 5 21 . 1 20 . 9 0 . 0 0 . 034 TL 11 . 83 PV 0 . 2 Pipe : 210 94 . 5 2 . 067 PL 1 . 83 PF 1 . 0 110 11 . 7 22 . 5 21 . 8 0 . 0 9 . 0 120 FTG T PE -0 . 8 210 13 . 5 20 . 7 20 . 2 0 . 0 0 . 085 TL 11 . 83 PV 0 . 5 Pipe: 215 47 . 8 2 . 067 PL 1 . 83 PF 0 . 3 115 11 . 7 22 . 9 21 . 9 0 . 0 4 . 6 120 FTG T PE -0 . 8 215 13 . 5 21 . 8 21 . 7 0 . 0 0 . 024 TL 11 . 83 PV 0 . 1 Pipe : 100 115 . 2 3. 260 PL 10 . 00 PF 0 . 1 105 11 . 7 22 .2 22 . 0 0 . 0 4 . 4 120 FTG ---- PE 0 . 0 100 11 . 7 22 . 1 22 . 0 0 . 0 0 . 013 TL 10 . 00 PV 0 . 1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 . DATE : 12/8/2004 C: \HASS DATA\ROMANOS\LIGHT HAZARD. SDF JOB TITLE : ROMANOS MACARONI GRILL PIPE TAG Q (GPM) DIA(IN) LENGTH PRESS . END ELEV. PT PN DISC. VEL (FPS) HW (C) (FT) SUM. NODES (FT) (PSI) (PSI) (GPM) FL/FT (PSI) Pipe: 105 172 . 8 3 . 260 PL 10 . 17 PF 0 . 3 110 11 . 7 22 . 5 21 . 8 0 . 0 6. 6 120 FTG ---- PE 0 . 0 105 11 . 7 22 . 2 22 . 0 0 . 0 0 . 028 TL 10. 17 PV 0 . 3 Pipe : 110 267 . 3 3 . 260 PL 6. 00 PF 0 . 4 115 11 . 7 22 . 9 21 . 9 0 . 0 10 . 3 120 FTG ---- PE 0 . 0 110 11 . 7 22 . 5 21 . 8 0 . 0 0 . 063 TL 6. 00 PV 0 . 7 Pipe: 115 315 . 2 3 . 260 PL 61. 33 PF 7 . 0 TOR 11 . 0 30 . 2 29 . 2 0 . 0 12 . 1 120 FTG 3L PE -0 . 3 115 11 . 7 22 . 9 21 . 9 0 . 0 0 . 085 TL 82 . 33 PV 1 . 0 Pipe : tor 315 . 2 3 . 260 PL 10 . 00 PF 2 . 0 BOR 1 . 0 36. 6 36. 5 0 . 0 12 . 1 120 FTG B PE -4 . 3 TOR 11 . 0 30 . 2 29. 2 0 . 0 0 . 085 TL 24 . 00 PV 1 . 0 Pipe : BOR 315 . 2 6. 280 PL 45 . 00 PF 0 . 2 DCOUT -3 . 0 38 . 6 38 . 6 0 . 0 3 . 3 140 FTG 3L PE -1 . 7 BOR 1 . 0 36. 6 36. 5 0 . 0 0 . 003 TL 87 . 00 PV 0 . 1 Pipe : DCOUT FIXED PRESSURE LOSS DEVICE DCIN -3 . 0 0 . 0 44 . 6 0 . 0 6. 0 psi, 315 . 2 gpm DCOUT -3 . 0 0 . 0 38 . 6 0 . 0 Pipe: DCIN 315 . 2 6. 280 PL 1 . 00 PF 0 . 0 SOURCE -3 . 0 44 . 6 44 . 6 (N/A) 3 . 3 140 FTG ---- PE 0 . 0 DCIN -3 . 0 44 . 6 44 . 6 0 . 0 0 . 003 TL 1 . 00 PV 0 . 1 NOTES : (1) Calculations were performed by the HASS 7 . 6 computer program under license no. 3806024810 granted by HRS Systems, Inc. 4792 LaVista Road Tucker, GA 30084 (2) 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 . 069 gpm. (3) Velocity pressures have been included in the calculation of the system pressures and flows . Maximum water velocity is 15 . 5 ft/sec at pipe 60A. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 . DATE: 12/8/2004 C: \HASS DATA\ROMANOS\LIGHT HAZARD. SDF JOB TITLE: ROMANOS MACARONI GRILL (4 ) PIPE FITTINGS TABLE Pipe Table Name : STANDARD. PIP PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Ell Tee LngEll ChkVly BfyVly GatVly AlmChk DPV1v NPTee 1 . 049 2 . 00 5 . 00 2 . 00 5 . 00 6. 00 1 . 00 10 . 00 10 . 00 5 . 00 1 . 380 3 . 00 6. 00 2 . 00 7 . 00 6. 00 1 . 00 10 . 00 10 . 00 6. 00 1 . 610 4 . 00 8 . 00 2 . 00 9. 00 6. 00 1 . 00 10 . 00 10 . 00 8 . 00 2 . 067 5 . 00 10. 00 3 . 00 11 . 00 6. 00 1 . 00 10 . 00 10 . 00 10 . 00 PAGE: B MATERIAL: THNWL HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D_ ___ _ N Ell Tee LngEll ChkVly BfyVly GatViv AlmChk DPV1v NPTee 3 . 260 10 . 00 20 . 00 7 . 00 22 . 00 14 . 00 1 . 00 18 . 00 18 . 00 20. 00 PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Ell Tee LngEll ChkVly BfyVly GatV1v NPTee 6 .280 22 . 00 47 . 00 14 . 00 51 . 00 16. 00 5 . 00 47 . 00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 . DATE : 12/8/2004 C: \HASS DATA\ROMANOS\LIGHT HAZARD. SDF JOB TITLE: ROMANOS MACARONI GRILL WATER SUPPLY CURVE 60+ 1 55+ *\\\\\\\\\\\\\\\ 0 \\\\\\\\\\\\\\\\ \\\\\\\\\\\\\\\ 50+ 50 . 0 psi @ 838 gpm-> * Flow Test Point 45+ X 1 P 40+ R I E I S 1 S 35+ U I R 1 E 1 30+ ( 1 P 1 S I I 25+ I 1 20+ 1 15+ 10+ LEGEND " I X = Required Water Supply 1 44 . 58 psi @ 415 . 2 gpm /I 5+ II I 0 = Available Water Supply " 1 52 . 91 psi @ 415 . 2 gpm 1 0++-+---+ 200 300 400 500 600 700 800 900 1000 FLOW (GPM) O• > w H WATER SUPPLY ANALYSIS H 60.0 Static: 54. 00 psi Resid: 50.00 psi Flow: 838 . 0 gpm H LEGEND • N.) to .. m A Available pressure 7z1N o 1 1 52.91 psi @ 415.2 gpm 0 Required pressure gy• A 50.0 _ 2 -44.58 psi @ 415.2 gpm Z O G A. Source Supply Curve--- m A 2 B. System Demand Curve > m U O ro G 40. 0 • H o Z E Z90 to P G1 7d R H m E 30. 0 N m S H to S X U n x 1-C E 20.0 m m t+ ( U n p H > s > Z i 10.0 o 1-< Z• m 0 m 0.0 B H H N 90• rd 0 • tQ -14 .7 200 300 400 500 600 700 800 900 1000 FLOW (GPM) McKinstry Fire Protection 5400 NE Columbia. Portland, OR 97218 Hydraulic Calculations for Romano's Macaroni Grill Tigard, Or Contract Number:7278 Date: 01/26/96 9:16 AM -Design Data- Occupancy Classification: {Ordinary Hazard Gp I} Density: {.15} Area of Application: {ENTIRE AREA} Coverage per Sprinkler: {130} Max. SQ. FT. Number of Sprinklers Calculated: {9} Total Sprinkler Water Flow Required: {173.9} Total Water Required(Including Hose): {423.9} Flow and Pressure(@ BOR): {273.9 GPM @ 21.7 PSI) Sprinkler Orifice Size: 1/2 inch Name of Contractor: McKinstry Co Designer: Richard A. Gordon Jr. Authority Having Jurisdiction: City of TUALATIN Calculations by HASS Computer Program HRS Systems, Inc. Atlanta, GA JOB: ROMANOS MACARONI GRILL TIGARD, OR �n WATER FLOW TEST: SYSTEM DEMAND: �l l S try DATE: 11-5 STATIC: 55 G.P.M.: RESIDUAL: 32 P.S.I.: SCPRINKLER CALC. BY:RAG G.P.M.: 2049 SYSTEM: JOB #: 7278 SCALE: A 175 _ 170 165 160 155 150 145 140 - 135 130 - 125 120 115 110 - 105= 100 - d 95 Li 90 85 W 80 D: 0 75 _ 70 - 65- 60 STATIC :rz .. 01 = €38 40 = RESIDUAL 32 0 2049 35 30 25_ 20 7. 15 = 10 5- 0 nnnWI 01.85 GPM i �i i ii �� ii � � i i i i i 1 i i i 1 i 1 i l i i 111111111 111111111 1111111i1 111111ii i 1 1 i 1 i i i i i i 1 1 1 (1.1 & 0 290 199 809 896 1008 1200 1188 1000 1888 2000 Scala C 400 800 1200 1600 2000 2400 2800 3200 3600 4000 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 . DATE: 12/8/2004 C: \HASS DATA\ROMANOS\ORD HAZARD. SDF JOB TITLE: Ramonos Kitchen WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ' D NODE PRESS. PRESS . @ PRESS . @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SOURCE 54 . 0 50 . 0 838 . 0 52 . 9 423 . 9 27 . 0 AGGREGATE FLOW ANALYSIS : TOTAL FLOW AT SOURCE 423 . 9 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 150 . 0 GPM OTHER HOSE STREAM ALLOWANCES 100 . 0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 173 . 9 GPM NODE ANALYSIS DATA PRESSURE NODE TAG ELEVATION NODE TYPE TOTAL NORMAL DISCHARGE (FT) (PSI) (PSI) (GPM) 500 9. 0 K= 5 . 38 14 . 1 14 . 1 20 . 2 505 9 . 0 K= 5 . 38 14 . 4 14 . 1 20 . 2 510 9. 0 K= 5 . 38 15 . 0 14 . 8 20 . 7 515 9 . 0 K= 5 . 38 15 . 4 15 . 0 20 . 8 520 9. 0 K= 5 . 30 11 . 5 11 . 5 18 . 0 520A 12 . 5 - - - - 10. 6 10 . 5 - - - 525 9 . 0 K= 5 . 30 11 . 7 11 . 7 18 . 1 525A 12 . 5 - - - - 10 . 9 10 . 6 - - - 530 9 . 0 K= 5 . 38 11 . 7 11 . 7 18 . 4 530A 12 . 5 - - - - 11 . 0 10 . 8 - - - 535 9. 0 K= 5 . 30 12 . 3 12 . 3 18 . 6 535A 12 . 5 - - - - 11 . 5 11 . 2 - - - 540 9. 0 K= 5 . 30 12 . 7 12 . 7 18 . 9 540A 12 . 5 - - - - 11 . 9 11 . 4 - - - 150 12 . 5 - - - 15 . 8 15 . 7 - - - 155 12 . 5 - - - - 15 . 8 15 . 5 - - - TOR 12 .5 - - - - 16. 0 15 . 7 - - - BOR 1 . 0 HOSE STREAM 21. 7 21 . 7 100 . 0 DCOUT -3 . 0 - - - - 23 . 6 23 . 6 - - - DCIN -3 . 0 - - - - 29 . 6 29 . 6 - - - SOURCE 3 . 0 SOURCE 27 . 0 27 . 0 273 . 9 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 12/8/2004 C: \HASS DATA\ROMANOS\ORD HAZARD. SDF JOB TITLE: Ramonos Kitchen PIPE DATA PIPE TAG Q (GPM) DIA(IN) LENGTH PRESS . END ELEV. PT PN DISC. VEL (FPS) HW (C) (FT) SUM. NODES (FT) (PSI) (PSI) (GPM) FL/FT (PSI) Pipe: 500 20 . 2 1 . 380 PL 10 . 00 PF 0 . 3 505 9. 0 14 . 4 14 . 1 20 . 2 4 . 3 120 FTG ---- PE 0 . 0 500 9. 0 14 . 1 14 . 1 20 . 2 0 . 035 TL 10 . 00 PV 0 . 1 Pipe: 505 40 . 4 1 . 610 PL 10 . 00 PF 0 . 6 510 9 .0 15 . 0 14 . 8 20 . 7 6. 4 120 FTG ---- PE 0 . 0 505 9. 0 14 . 4 14 . 1 20 . 2 0 . 059 TL 10 . 00 PV 0 . 3 Pipe: 510 61 . 1 2 . 067 PL 10 . 00 PF 0 . 4 515 9 . 0 15 . 4 15 . 0 20 . 8 5 . 8 120 FTG ---- PE 0 . 0 510 9. 0 15 . 0 14 . 8 20 . 7 0 . 038 TL 10 . 00 PV 0 . 2 Pipe: 515 81 . 9 2 . 067 PL 19 . 58 PF 1 . 9 150 12 . 5 15 . 8 15 . 7 0 . 0 7 . 8 120 FTG T PE 1 . 5 515 9 . 0 15 . 4 15 . 0 20 . 8 0 . 065 TL 29 . 58 PV 0 . 4 Pipe: 520 18 . 0 1 . 049 PL 5 . 50 PF 0 . 6 520A 12 . 5 10 . 6 10 . 5 0 . 0 6 . 7 120 FTG ---- PE 1 . 5 520 9. 0 11 . 5 11 . 5 18 . 0 0 . 107 TL 5 . 50 PV 0 . 3 Pipe: 520a 18 . 0 1 . 380 PL 9. 25 PF 0 . 3 525A 12 . 5 10 . 9 10 . 6 0 . 0 3 . 9 120 FTG ---- PE 0 . 0 520A 12 . 5 10 . 6 10 . 5 0 . 0 0 . 028 TL 9 . 25 PV 0 . 1 Pipe: 525 18 . 1 1 . 049 PL 6. 33 PF 0 . 7 525A 12 . 5 10 . 9 10 . 6 0 . 0 6. 7 120 FTG ---- PE 1 . 5 525 9 . 0 11 . 7 11 . 7 18 . 1 0 . 108 TL 6. 33 PV 0 . 3 Pipe: 525a 36. 1 1 . 610 PL 3 . 42 PF 0 . 2 530A 12 . 5 11 . 0 10. 8 0 . 0 5 . 7 120 FTG ---- PE 0 . 0 525A 12 . 5 10 . 9 10 . 6 0 . 0 0. 048 TL 3 . 42 PV 0 . 2 Pipe: 530 18 . 4 1 . 049 PL 2 . 33 PF 0 . 8 530A 12 . 5 11 . 0 10. 8 0 . 0 6. 8 120 FTG T PE 1 . 5 530 9 . 0 11 . 7 11 . 7 18 . 4 0. 112 TL 7 . 33 PV 0 . 3 Pipe: 530a 54 . 6 2 . 067 PL 5 . 12 PF 0 . 5 535A 12 . 5 11 . 5 11 .2 0 . 0 5 . 2 120 FTG 2E PE 0 . 0 530A 12 . 5 11 . 0 10. 8 0 . 0 0 . 031 TL 15 . 12 PV 0 . 2 Pipe: 535 18 . 6 1 . 049 PL 1 . 33 PF 0 . 7 535A 12 . 5 11 . 5 11 . 2 0 . 0 6. 9 120 FTG T PE 1 . 5 535 9. 0 12 . 3 12. 3 18 . 6 0. 114 TL 6. 33 PV 0 . 3 Pipe: 535a 73 . 1 2 . 067 PL 8 . 08 PF 0 . 4 540A 12 . 5 11 . 9 11. 4 0 . 0 7 . 0 120 FTG ---- PE 0 . 0 535A 12 . 5 11 . 5 11.2 0 . 0 0. 053 TL 8 . 08 PV 0 . 3 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 12/8/2004 C: \HASS DATA\ROMANOS\ORD HAZARD. SDF JOB TITLE : Ramonos Kitchen PIPE TAG Q (GPM) DIA(IN) LENGTH PRESS . END ELEV. PT PN DISC. VEL (FPS) HW (C) (FT) SUM. NODES (FT) (PSI) (PSI) (GPM) FL/FT (PSI) Pipe : 540 18 . 9 1 . 049 PL 1 . 33 PF 0 . 7 540A 12 . 5 11 . 9 11 . 4 0 . 0 7 . 0 120 FTG T PE 1 . 5 540 9. 0 12 . 7 12 . 7 18 . 9 0 .117 TL 6. 33 PV 0 . 3 Pipe : 540a 92 . 0 2 . 067 PL 23 . 08 PF 3 . 9 155 12 . 5 15 . 8 15. 5 0 . 0 8 . 8 120 FTG 2TE PE 0 . 0 540A 12 . 5 11 . 9 11 . 4 0 . 0 0. 081 TL 48 . 08 PV 0 . 5 Pipe: 150 81 . 9 3. 260 PL 1 . 33 PF 0 . 0 155 12 . 5 15 . 8 15 . 5 0 . 0 3 . 1 120 FTG ---- PE 0 . 0 150 12 . 5 15 . 8 15 . 7 0 . 0 0 . 007 TL 1 . 33 PV 0 . 1 Pipe: 155 173 . 9 3 . 260 PL 2 . 00 PF 0 . 3 TOR 12 . 5 16 . 0 15 . 7 0 . 0 6. 7 120 FTG L PE 0 . 0 155 12 . 5 15 . 8 15 . 5 0 . 0 0. 028 TL 9 . 00 PV 0 . 3 Pipe: tor 173 . 9 3 . 260 PL 10 . 00 PF 0 . 7 BOR 1 . 0 21 . 7 21 . 7 100 . 0 6. 7 120 FTG B PE -5 . 0 TOR 12 . 5 16. 0 15 . 7 0 . 0 0. 028 TL 24 . 00 PV 0 . 3 Pipe : BOR 273 . 9 6. 280 PL 45 . 00 PF 0 . 2 DCOUT -3 . 0 23 . 6 23 . 6 0 . 0 2 . 8 140 FTG 3L PE -1 . 7 BOR 1 . 0 21 . 7 21 . 7 100 . 0 0. 002 TL 87 . 00 PV 0 . 1 Pipe: DCOUT FIXED PRESSURE LOSS DEVICE DCIN -3 . 0 0 . 0 29. 6 0 . 0 6. 0 psi, 273. 9 gpm DCOUT -3 . 0 0 . 0 23 . 6 0. 0 Pipe: DCIN 273 . 9 6. 280 PL 1 . 00 PF 0 . 0 SOURCE 3 . 0 27 . 0 27 . 0 (N/A) 2 . 8 140 FTG ---- PE 2 . 6 DCIN -3 . 0 29 . 6 29 . 6 0 . 0 0. 002 TL 1 . 00 PV 0 . 1 NOTES: (1) Calculations were performed by the HASS 7 . 6 computer program under license no. 3806024810 granted by HRS Systems, Inc. 4792 LaVista Road Tucker, GA 30084 (2 ) The system has been calculated to provide an average imbalance at each node of 0 . 004 gpm and a maximum imbalance at any node of 0 . 081 gpm. (3) Velocity pressures have been included in the calculation of the system pressures and flows . Maximum water velocity is 8 . 8 ft/sec at pipe 540a. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 12/8/2004 C: \HASS DATA\ROMANOS\ORD HAZARD. SDF JOB TITLE: Ramonos Kitchen (4) PIPE FITTINGS TABLE Pipe Table Name: STANDARD. PIP PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Ell Tee LngEll ChkV1v BfyVly GatV1v AlmChk DPV1v NPTee 1. 049 2 . 00 5 . 00 2 . 00 5 . 00 6. 00 1 . 00 10 . 00 10 . 00 5 . 00 1 . 380 3 . 00 6. 00 2 . 00 7 . 00 6. 00 1 . 00 10 . 00 10 . 00 6. 00 1 . 610 4 . 00 8 . 00 2 . 00 9 . 00 6 . 00 1 . 00 10 . 00 10 . 00 8 . 00 2 . 067 5 . 00 10 . 00 3 . 00 11 . 00 6. 00 1 . 00 10 . 00 10 . 00 10 . 00 PAGE: B MATERIAL: THNWL HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Ell Tee LngEll ChkV1v BfyVly GatV1v AlmChk DPV1v NPTee 3 .260 10. 00 20 . 00 7 . 00 22 . 00 14 . 00 1 . 00 18 . 00 18 . 00 20 . 00 PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Ell Tee LngEll ChkV1v BfyVly GatV1v NPTee 6. 280 22 . 00 47 . 00 14 . 00 51 . 00 16. 00 5 . 00 47 . 00 r ��J `i V . O � W H tri WATER SUPPLY ANALYSIS y .. 60. 0 Static: 54 .00 psi Resid: 50. 00 psi Flow: 838. 0 gpm 1--1 ,J LEGEND r `� A Available pressure 1 77 N 52.87 psi @ 423.9 gpm • o Required pressure p ,A 50. 0 _ 2-_27.03 psi @ 423.9 gpm G A. Source Supply Curve o B. System Demand Curve A N- cn 0- ro G 40.0 _ • H E m z P R N E 30.0 v, H 2 U x R n d E 20.0 xa ( N H N n p d s • z i 10. 0 • r H z 0 0. 0 B 0 0 r=1 7d rU 0 • Q -14.7 I I I I I I I I 0 cn 200 300 400 500 600 700 800 900 1000 FLOW (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 . DATE : 12/8/2004 C: \HASS DATA\ROMANOS\ORD HAZARD. SDF JOB TITLE: Ramonos Kitchen WATER SUPPLY CURVE 60+ 55+ *\\\\\\\\\\\\\\\ 0 \\\\\\\\\\\\\\\\ \\\\\\\\\\\\\\\ 50+ 50 . 0 psi @ 838 gpm-> * Flow Test Point 45+ 1 P 40+ R I E 1 S 1 S 35+ U I R 1 E I 30+ ( 1 P I X S I I 25+ I 1 20+ 1 I 15+ 1 10+ LEGEND " I " I X = Required Water Supply I 27 . 03 psi @ 423 . 9 gpm 5+ I 0 = Available Water Supply " 1 52 . 87 psi @ 423 . 9 gpm " " 0++-+---+----+ + + + + + + 200 300 400 500 600 700 800 900 1000 FLOW (GPM)