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1765 Yankee Doodle Rd - Fire Protection Reports SUBMITTAL SERIAL N0:2349H-04 12-17-1990 PAGE 1 SEST BRANDS 1990 ADDITION REMOTE NW2 BEST BRANDS 1990 ADDITION 1765 YANREE DOODLE ROAD EAGAN MN IFP JOB #91.025 INDEPENDENT FIRE PROTECTION INC 390 93RD AVE NW MINNEAPOLIS MN 55433 CALCULATED BY HARRY WIEBE RELIABLE "G" 286F K=8.2 100 GPM INSIDE HOSE 400 GPM OliTSIDE HOSE 452.14 GPM 56.89 PSI REQUIRED AT BASE OE RISER FLOW TEST RESULTS STATIC 70.00 PSI Ri'SiDllAI. A'P 2990.0 GPM 55.00 PSI YRE5SORE AVAILABLE A7' 852.1 _ GPM 68.53 PSI SOMMARY OE SPRINKLER OUTFL(JWS ACTUAL MINIMUM SPR FLOW I'LOW K-FACTOR PRESSURE 307 27.55 25.64 8.20 11.29 306 25.94 25.64 8.20 10.01 309 25.64 25.64 8.20 9.78 310 25.75 25.64 8.20 9.86 314 27.56 25.64 8.20 11.30 315 26.04 25.64 8.20 10.08 316 25.79 25.64 8.20 9.89 317 25.93 25.64 8.20 10.00 321 28.14 25.64 8.20 11.78 322 26.80 25.64 8.20 10.68 323 26.64 25.64 8.20 10.56 324 26.87 25.64 8.20 10.74 331 33.48 22.21. 8.20 16.67 TOTAL WATER REQUIRED FOR SYSTEM 352.14 GPM OUTFLOWS AT 4 100.00 GPM OUTSIDE HOSE STREAMS AT 0 400.00 GPM TOTAL WATER REQUIREMENT 852.14 GPM YRESSURE REQUIREU AT 0 58.37 7'SI MAXIMUM PRESSURF, UNt3A7.:~^~c'I? I N i,00Y5 0.092 PST MAXIMUM VELOCITY IN PIPES 16.27 FPS SUBMITTAL SERIAL N0:2349H-04 12-17-1990 PAGE 2 BEST BRANDS 1990 ADDT'i'ION REMOTG NW2 EROM TO CLOW DIAM EQli i V P-LOSS PRESSURF. GPM IN PIPE PSI/ET SL~ihAFtY LEN/ET PSI 310 309 1.452 71 12.21 0.0065 PT 9.78 (309) Q 9.28 E=0 F 0.00 PE 0.00 BL C120 T 12.21 PF 0.08 311 3].0DQ 25.75 1.452 L 12.21 0.0754 PT 9.86 (310) Q 35.04 F=0 E 0.00 PE 0.00 BL C120 T 12.21 PF 0.92 367 31]. ].452 L 1.21 0.0754 PT 10.78 (311) Q 35.04 I'=0/T F 6.00 PE 0.00 BL C120 T 7.21 PE 0.54 357 367 1.452 L 1.12 0.0754 PT 11.32 (367) Q 35.04 F=T F 6.00 PE 0.48 RN C120 'P 7.12 PC 0.54 356 357 1.687 L 10.00 0.0363 PT 12.34 (357) Q 35.04 E=0 E 0.00 PE 0.00 CM C120 T 10.00 PF 0.36 355 356DQ 36.79 1.687 L 10.00 0.1370 PT 12.70 (356) Q 71.83 F'=0 P 0.00 PE 0.00 CM C120 T 10.00 PF 1.37 354 355DQ 41.54 1.687 L ].0.00 0.3187 PT 14.07 (355) Q 113.37 F=0 F 0.00 PE 0.00 CM C120 T 10.00 PF 3.19 353 354DQ -7.29 1.687 L 8.75 0.2819 PT 17.26 (354) Q 106.08 F=0 F 0.00 PE 0.00 CM C120 T 8.75 PP 2.47 352 353DQ -29.04 1.687 L 7.83 0.1560 FT 19.73 (353) Q 77.04 E=0 E 0.00 PE 0.00 CM C120 T 7.83 PE 1.22 351 352DQ -27.09 1.687 L 9.25 0.0700 PT 20.95 (352) Q 49.95 F=0 E 0.00 PE 0.00 CM C120 'r 9.25 PF 0.65 350 351DQ -25.45 1.687 L 9.67 0.0187 PT 21.60 f3511 Q 24.50 F=0 F 0.00 PE 0.00 CM C120 T 9.67 PF 0.18 360 350 1.452 I, 1.37 0.0389 PT 21.78 (350) Q 24.50 F=T P 6.00 PE -0.59 RN C1.20 T 7.37 PF 0.29 223 360 1.4,52 71 60.29 0.0389 PT 21.48 (360) Q 24.50 L' 0i7' r 6.OU PE 0.00 BL C120 7' 66.29 PF 2.58 SURMi'C`CAli SERIAli N0:234911-04 12-17-1990 i'AGI1; 3 }tI;S'I' RRIiND5 1990 ADDITION REMOTE NW2 FROM TO FLOW DIAi1 EQGIV P-LUSS PRESSURE GPM 1:N PIYE P5I/FT SUMMARY LEN/FT PSI 224 223 1.452 L 12.83 0.0389 PT 24.06 (223) Q 24.50 F=0 F 0.00 PE 0.00 BI, t`7 20 'C 12.83 PF 0.50 225 224 1.687 71 12.17 0.0187 PT 24.56 (224) Q 24.50 F=0/T li 8.00 PE 0.00 BL C120 T 20.17 PE 0.38 200 225 2.154 L 2.00 0.0057 PT 24.44 (225) Q 24.50 F=T F 10.00 PE 0.87 RN c120 T 12.00 Pr 0.07 201 2no 2.635 L, 9.67 0.0021 YT 25.88 (200) Q 24.50 F=0 F 0.00 PE 0.00 CK C120 T 9.67 PF 0.02 PT 25.90 (201) 361 351 1.452 L 1.62 0.0417 PT 21.52 (351) Q 25.45 F=T F 6.00 PE -0.70 kN C120 T 7.62 Fr' 0.32 218 361 1.452 L 60.29 0.041.7 P'C 21.14 (361) Q 25.95 F=0/T F 6.00 YE 0.00 BL C120 T 66.29 PF 2.76 219 218 1.452 L 12.83 0.0417 PT 23.90 (218) Q 25.45 F=0 F 0.00 PE 0.00 BL C120 T 12.83 PF 0.54 220 219 1.687 L 12.17 0.0201 PT 24.44 (219) Q 25.45 F=0/T F 8.00 PE 0.00 BL C120 T 20.17 PE 0.41 201 220 2.154 L 2.00 0.0061 PT 24.85 (220) Q 25.45 F=T P 10.00 PE 0.87 RN C120 T 12.00 PF 0.07 202 201DQ 24.50 2.635 L 7.96 0.0080 PT 25.79 (201) Q 49.95 F=0 E 0.00 PE 0.00 CM C120 T 7.96 PF 0.06 PT 25.85 (202) 362 352 1.452 L 1.54 0.0468 PT 20.89 (352) Q 27.09 E=T E' 6.00 PE -0.67 RN C1.20 T 7.54 PF 0.35 213 362 1.452 L 60.29 0.0468 PT 20.57 (362) Q 27.09 E=01T E 6.00 PE 0.00 BL C120 T 66.29 PF 3.10 SUBMITTAL SERIAL N0:2349H-04 12-17-1990 PAGE 4 BEST BRANDS 1990 ADDITION REMOTE NW2 EROM TO FLOW DIAM EQliIV P-LOSS PRESSURE i;l'M I[V PIPE P57/LT SUMMARY LEN/FT PSI 214 213 1.452 L 12.83 0.0468 PT 23.67 (213) Q 27.09 F=0 E 0.00 PE 0.00 BL C120 T 12.83 PF 0.60 215 214 1.687 L 12.7.7 0.0226 PT 24.27 (214) Q 27.09 F=O/T E 8.00 PE 0.00 BL C120 T 20.17 PF 0.46 203 215 1.687 L 2.00 0.0226 PT 24.73 (215) Q 27•09 E='P E 8.00 PE 0.87 RN C120 T 10.00 FF 0.23 PT 25.83 (203) 363 353 1.452 1. 1.12 0.0533 PT 19.67 (353) Q 29.04 F=T F 6.00 PE -0.48 RN C120 T 7.12 PF 0.38 210 363 1.452 L 60.29 0.0533 PT 19.57 (363) Q 29.04 F=O/T F 6.00 PE 0.00 BL C120 T 66.29 PL' 3.53 2]1 Ziu 1.452 i"l.rt"t r ,33 PT 23.10 (210) Q 29.04 e'-0 P 0.00 Pt: 11.00 BL C120 T 12.83 PF 0.68 212 211 1.687 L 12.17 0.0257 PT 23.78 (211) Q 29.04 F=O/T E 8.00 PE 0.00 BL C120 T 20.17 PF 0.52 204 212 1.687 L 2.00 0.0257 PT 24.30 (212) Q 29.04 F=T F 8.00 PE 0.87 RN C120 T 10.00 PF 0.26 PT 25.43 (204) 364 354 1.452 L 1.37 0.0041 PT 17.23 l3541 Q 7.29 F=T F 6.00 PE -0.59 RN C120 T 7.37 PF 0.03 332 364 1.452 L 1.08 0.0041 PT 16.67 (364) Q 7.29 F=O/T F 6.00 PE 0.00 BL C120 T 7.08 PF 0.03 331 332 1.452 L 11.75 0.0041 PT 16.70 (332) Q 7.29 F=0 L' 0.00 PE 0.00 BL C1.20 '1' 11.75 PE 0.05 330 331DQ 33.48 1.452 L 11.75 0.0998 PT 16.75 (331) Q 40.77 F'=0 E' 0.00 PE 0.00 13L C7.20 T 11.75 PL 1.17 Si1FtMi9"I'AL S}?RIAL N0:2349H-04 12-17-1990 PAGE 5 13EST URANDS 1990 ADDITION REMUTE NW2 E'ROM TO ELOW DIAM EQOIV P-LOSS PRESSUttb; GPM 1N PIPE PSI/FT SUMMARY LEN/FT PSl 329 330 1.452 L 11.75 0.0998 PT 17.92 (330) Q 40.77 F=0 P 0.00 FE 0.00 BL C120 T 11.75 PF 1.17 328 329 1.452 L 11.75 0.0998 PT 19.09 (329) Q 40.77 F=0 F 0.00 PE 0.00 BL C120 T 11.75 PF 1.17 327 328 1.452 L 12.21 0.0998 PT 20.26 (328) Q 40.77 F=0 F 0.00 PE 0.00 BL C120 T 12.21 PF 1.22 326 327 1.452 L 12.75 0.0998 PT 21.48 (327) Q 40.77 E=0 E' 0.00 PE 0.00 BL C120 T 12.75 PF 1.27 301 326 1.687 L 12.04 0.0481 PT 22.75 (326) Q 40.77 F=T E 8.00 PE 0.00 BL C120 T 20.04 PF 0.96 205 301 1.687 1, 1.37 0.0481 PT 23.71 (301) Q 40.77 F-Ir r 8.00 PE 0.59 RN C120 T 9.37 PF 0.45 PT 24.75 (205) 324 323 1.452 I, 1"l.2:I 0.01.51 PT 10.56 (323) Q 14.67 F=0 N 0.00 PE 0.00 BL C120 T 12.21 PF 0.18 325 324D4 26.87 1.452 L 12.21 0.1033 PT 10.74 (324) Q =ii .54 c=o F 0.00 Ps 0.00 BL C120 T 1.2.21 PF 1.26 365 325 1.452 L 1.21 0.1033 PT 12.00 (325) Q 41.54 F=0/T r 6.00 PE 0.00 YT. C120 T 7.21 PF 0.74 355 365 1.452 L 1.29 0.1033 PT 12.74 (365) Q 41.54 L'=T F 6.00 PE 0.56 RN C120 T 7.29 PF 0.75 PT 14.05 (355) 322 323 1.452 L 12.21 0.0103 PT 10.56 (323) Q 11.97 E=0 F 0.00 PE 0.00 BL C120 T 12.21 PF 0.13 321 322DQ 26.80 1.452 L 12.21 0.0909 PT 10.69 (322) Q 38.77 E=0 F 0.00 PE 0.00 BL C120 T 12.21 PF 1.11 SUBMITTAL SERIAL N0:2349H-04 12-17-1990 PAGE 6 BEST BRANDS 1990 ADllITION REMOTE NW2 L'HOM TO FLOW DIAM EQUIV P-LOSS PRESSORE GPM iN PIPE PSI/FT SOMMAKY LEN/ET PSI 320 ,11DQ 28.14 1.452 L 12.21 0.2495 PT 11.80 (321) Q 66.92 H'=0 F 0.00 PE 0.00 BL C1.20 T 12.21 PF 3.05 319 320 1.452 L 12.21 0.2495 PT 14.85 (320) Q 66.92 F=0 I? 0.00 PE 0.00 BL C120 T 12.21 PF 3.05 302 319 1.452 L 10.62 0.2495 PT 17.90 (319) Q 66.92 E=T E 6.00 PE 0.00 BL C120 T 16.62 PF 4.15 206 302 1.452 L 1.29 0.2495 P'r 22.05 (302) Q 66.92 F=T F 6.00 PE 0.56 RN C120 T 7.29 PF 1.82 PT 24.43 (206) 317 316 1.452 L 12.21 0.0086 PT 9.89 (316) Q 10.87 F=0 F 0.00 PE 0.00 BL C120 T 12.21 PF 0.11 318 317DQ 25.93 1.452 L 12.21 0.0825 PT 10.00 (317) Q 36.79 E=0 P 0.00 PE 0.00 BL C120 T 12.21 PF 1.01 366 318 1.452 L 1.21 0.0825 PT 11.01 (318) Q 36.79 F=0/T F 6.00 PE 0.00 Flll Cl 20 7' 7.21 PF 0.59 356 366 1.452 T, 1.21. 0.0825 PT 11.60 (366) Q 36.79 L'=T F 6.00 PE 0.52 RN C120 'I` 7.21 PE 0.59 FT 12.71 (356) 315 316 1.452 L 12.21 0.0155 PT 9.89 (316) Q 14.92 F=0 F 0.00 PE 0.00 BL C120 T 12.21 PE 0.19 314 315DQ 26.04 1.452 L 12.21 0.1006 PT 10.08 (315) Q 40.96 E=0 F 0.00 PE 0.00 BL C120 T 12.21 PF 1.23 313 314DQ 27.56 1.452 L 12.21 0.2607 PT 11.31 (314) Q 68.52 F=0 E 0.00 PE 0.00 BL C120 T 12.21 PF 3.18 312 313 1.452 L 12.21 0.2607 PT 14.49 (313) Q 68.52 E=0 F 0.00 PE 0.00 BL C120 T 12.21 PE 3.18 SUBMITTAL SERIAL N0:2349H-04 12-17-1990 PAGE 7 gEST BftANDS 1990 .ADDITION REMOTE NW2 EROM TO FLOW DIAM EQUIV P-LOSS PRESSURE GPM IN PIPE PSC/ET SUMMARY LEN/FT PSI 303 312 1.452 L 10.62 0.2607 PT 17.67 (312) Q 68.52 F=T F 6.00 PE 0.00 BL C120 T 16.62 PF 4.33 207 303 1.452 L 1.21 0.2607 PT 22.00 (303) Q 68.52 F=T F 6.00 PE 0.52 RN C120 T 7.21 PF 1.88 PT 24.40 (207) 308 309 1.452 L 12.21 0.0184 PT 9.78 (309) Q 16.36 F=0 F 0.00 PE 0.00 BL C120 T 12.21 PE 0.22 307 308DQ 25.94 1.452 L 12.21 0.1068 PT 10.00 (308) Q 42.29 F=0 E 0.00 PE 0.00 BL C120 T 12.21 PF 1.30 306 307DQ 27.55 1.452 L 12.21 0.2701 PT 11.30 (307) Q 69.85 F=0 P 0.00 PE 0.00 BL C120 T 12.21 PF 3.30 305 306 1.452 L 12.21 0.2701 PT 14.60 (306) Q 69.85 E=0 E 0.00 PE 0.00 BL C120 T 12.21 PF 3.30 304 305 1.452 L 10.62 0.2701 PT 17.90 (305) Q 69.85 F=T E 6.00 PE 0.00 BL C120 T 16.62 PF 4.49 209 304 1.452 L 1.12 0.2701 PT 22.39 (304) Q 69.85 F=T F 6.00 PE 0.48 RN C120 T 7.12 PF 1.92 208 209 2.154 L 1.00 0.0396 PT 24.79 (209) Q 69.85 E=T E 10.00 PE 0.00 CM C120 T 11.00 PF 0.44 wr ~9.23 (208) 207 206 2.154 11 10.00 0.0002 PT 24.39 (206) Q 3.56 P=0 F 0.00 PE 0.00 CM C120 T 10.00 PE 0.00 208 207DQ 68.52 2.154 L 9.00 0.0419 PT 24.39 (207) Q 72•08 F=0/T F 10.00 PE 0.00 CM C120 T 19.00 PE 0.80 300 208DQ 69.85 2.154 L 31.00 0.1969 PT 25.19 (208) Q 141.92 E=T/2E F 20.00 PE -2.60 CM C120 T 51.00 PF 7.49 PT 30.08 (300) SUBMITTAL SERLAL N0:2349H-04 12-17-1990 PAGE 8 BEST BRANDS 1990 ADDITION REMOTE NGv'2 FROM TO FLOW DTAM EQUIV P-LOSS PRESSURE GPM IN PIPC PSI/ET SUMMARY LEN/FT PSI 205 206 2.154 L 10.00 0.0330 PT 24.39 (206) Q 63.36 F=D F 0.00 PE 0.00 CM C120 T 10.00 PF 0.33 204 205DQ 40.77 2.154 L 8.75 0.0828 PT 24.72 (205) Q 104.13 F=0 E 0.00 PE 0.00 CM C120 T 8.75 PF 0.72 203 204DQ 29.04 2.635 L 7.67 0.0489 PT 25.44 (204) Q 133.17 F=0 F 0.00 PE 0.00 CM C120 T 7.67 PE 0.38 202 203DQ 27.09 2.635 L 1.41 0.0689 PT 25.82 (203) Q 160.27 F=0 E 0.00 PE 0.00 CM C120 T 1.41 PF 0.10 89 202DQ 49.95 2.635 L 27.58 0.1139 PT 25.92 (202) Q 210.21 E=2E/T E 20.00 PE -3.46 CM C120 T 47.58 PF 5.42 52 89 2.635 L 0.67 0.1139 PT 27.88 ( 89) Q 210.21 E=T E 12.00 PE 0.00 aL r_120 T 12.67 pF 1.44 PT 29.32 ( 52) 38 300 3.260 L 1.00 0.0008 PT 30.05 (300) Q 25.06 F=0 E 0.00 PE 0.00 CM C120 T 1.00 PF 0.00 58 38 1.452 L 1.00 0.0405 PT 30.05 ( 38) Q 25.06 F=T F 6.00 YE -0.43 RN C120 'P 7.00 PF 0.28 48 58 7.452 L 97.67 0.0405 PT 29.90 ( 58) Q 25.06 E=T/T E 12.00 PE 0.00 BL C120 T 109.67 PF 4.44 16 48 1.452 L 8.00 0.0405 PT 34.34 ( 48) Q 25.06 F=T F 6.00 PE 3.46 RN C120 T 14.00 PE' 0.57 17 7.8 4.260 L 10.00 0.0002 PT 38.37 ( 18) Q 25.06 F=0 0.00 PE 0.00 CM C120 T 10.00 PF 0.00 PT 38.37 ( 17) 37 300 3.260 L, 9.00 0.0136 PT 30.05 (300) Q 116.87 E'=0 F 0.00 PE 0.00 CM C120 T 9.00 PF 0.12 PT 30.17 ( 37) Si7BMITTAL SERIAL N0:2399H-04 12-17-1990 PAGR 9 SES'I' BRANDS 1990 ADDITION REMOTE NW2 rROM TO FLOW UTAM EQUIV P-LOS5 PRESSURE GPM IN PIFE PSI/FT SOMMARY LEN/FT PSI 32 52 3.068 11 1.00 0.0356 PT 29.28 ( 52) Q 167.37 F=T F 15.00 PE 0.43 RN C120 T 16.00 PE 0.57 33 32DQ -81.53 3.260 L 9.00 0.0077 PT 30.28 ( 32) Q 85.84 E=0 E 0.00 PE 0.00 r_M C120 T 9.00 PF 0.07 34 33DQ -39.14 3.260 L 3.00 0.0025 PT 30.35 ( 33) Q 46.70 F=0 F 0.00 PE 0.00 Cm C120 T 3.00 PF 0.01 160 34DQ 43.43 2.154 L 18.00 0.0634 PT 30.36 ( 34) Q 90.13 E=T/E E 15.00 PE 7.79 CM C120 T 33.00 PF 2.09 161. 160 2.154 L 6.00 0.0634 PT 40.24 (160) Q 90.13 E=0 F 0.00 PE 0.00 CM C120 T 6.00 PF 0.38 162 161DQ -24.01 2.154 L 10.00 0.0358 PT 40.62 (161) Q 66.12 E=0 C 0.00 PE 0.00 CM C120 T 10.00 PE 0.36 163 162DQ -22.63 2.154 L 10.00 0.0165 PT 40.98 (162) Q 43.49 F=0 F 0.00 PE 0.00 CM C120 T 10.00 PE 0.16 164 163llQ -21.86 2.154 L 10.00 0.0045 FT 41.14 (163) Q 21.63 F=0 E 0.00 YI~; 0.00 CM C120 T 10.00 PF 0.04 154 164 1.452 L 99.67 0.0309 PT 41.18 (164) Q 21.63 F=2T/2T L 24.00 PE 0.00 BL C120 T 123.67 PF 3.82 153 154 2.635 L 10.00 0.0017 PT 45.00 (154) Q 21.63 F=0 F 0.00 PE 0.00 CM C120 T 10.00 PF 0.02 PT 45.02 (153) 153 163 1.452 L 99.67 0.0315 PT 41.12 (163) Q 21.86 E=2T/2T F 24.00 PE 0.00 BL C120 T 123.67 PF 3.90 152 153DQ 21.63 2.635 L 10.00 0.0062 PT 45.02 (153) Q 43.49 F=0 E 0.00 PE 0.00 CM C120 T 10.00 PF 0.06 PT 45.08 (152) SUBMITTAL SERIAI, N0:2349H-04 12-17-1990 PAGE 10 BEST BRANDS 1990 ADDITION REMOTE NW2 ' FROM TO FLOW DIAM EQUIV P-LOSS PRESSURE GPM IN PIPE PSI/ET SUMMARY LEN/FT PSI 152 162 1.452 L 99.67 0.0336 PT 40.95 (162) Q 22.63 Y=2T/2T F 24.00 PE 0.00 BL C120 T 123.67 PE 4.16 151 152DQ 43.49 2.635 L 10.00 0.0134 PT 45.11 (152) Q 66.12 F=0 E 0.00 PE 0.00 CM C120 T 10.00 PF 0.13 PT 45.24 (151) 151 161 1.452 L 99.67 0.0375 PT 40.59 (161) Q 24.111 E=2Ti2T F 24.00 PE 0.00 BL C120 T 123.67 PE 4.64 150 151DQ 66.12 2.635 L 6.00 0.0238 PT 45.23 (151) Q 90.13 e=0 e 0.00 PE 0.00 CM C120 T 6.00 PC 0.14 14 150 2.635 L 18.00 0.0238 PT 45.37 (150) Q 90.13 1 16.00 PE -7.79 CM C120 T 34.00 PE 0.$1 PT 38.39 ( 14) 57 37 1.452 L 1.00 0.0395 PT 30.18 ( 37) Q 24.72 E=T E 6.00 PE -0.43 RN C120 T 7.00 PE 0.28 47 57 1.452 L 97.67 0.0395 PT 30.03 ( 57) Q 24..72 F=T/T F 12.00 PE 0.00 BL C120 T 109.67 ijl? 4.33 17 47 1.452 L 8.00 0.0395 PT 34.36 ( 47) Q 24.72 P=T E 6.00 PE 3.46 RN C120 T 14.00 PF 0.55 16 17DQ 25.06 4.260 L 10.00 0.0008 PT 38.37 ( 17) Q 49.78 F=0 F 0.00 FE 0.00 CM C120 T 10.00 PE 0.01 PT 38.38 ( 16) 36 37 3.260 L 10.00 0.0088 PT 30.18 ( 37) Q 92.15 F=0 F 0.00 PE 0.00 CM C120 T 10.00 PF 0.09 56 36DQ -67.75 1.452 L 1.00 0.0386 PT 30.27 ( 36) Q 24.39 E=T F 6.00 PE -0.43 RN C120 T 7.00 PF 0.27 46 56 1.452 L 97.67 0.0386 PT 30.11 ( 56) Q 24.39 F=T/T F 12.00 PE 0.00 BL C120 T 109.67 PF 4.23 SUBMITTAL SERIAL N0:2349H-04 12-17-1990 PAGE 11 BEST BRANDS 1990 ADDITION REMOTE NW2 FROM TO FLOW DIAM EQUIV P-LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY liEN/ET PSI 16 46 1.452 L 8.00 0.0386 PT 34.34 ( 46) Q 24.39 F=T F 6.00 PE 3.46 RN C120 T 14.00 PF 0.54 7.5 16DQ 49.78 4.260 L 10.00 0.0016 PT 38.34 ( 16) Q 74.1.7 F=0 F 0.00 PE 0.00 CM C120 T 10.00 PF 0.0? PT 38.36 ( 15) 35 36 3.260 L 10.00 0.0050 PT 30.26 ( 36) Q 67.75 F=0 F 0.00 PE 0.00 CM C120 T 10.00 PF 0.05 55 35DQ -43.43 1.452 L 1.00 0.0384 PT 30.31 ( 35) Q 24.33 E=T E 6.00 PE -0.43 RN C120 T 7.00 PF 0.27 45 55 1.452 L 97.67 0.0384 PT 30.15 ( 55) Q 24.33 F=T/T E 12.00 PE 0.00 BL C120 T 109.67 PF 4.21 7.5 45 1.452 L 8.00 0.0384 PT 34.36 ( 45) Q 24.33 E=T F 6.00 PE 3.46 RN C120 T 14.00 PF 0.54 14 150Q 74.17 4.260 L 6.00 0.0027 PT 38.36 ( 15) Q 98.50 E=0 F 0.00 PE 0.00 CM C120 T 6.00 PF 0.02 l3 14uQ 90.13 4.260 L 3.00 0.0090 PT 38.38 ( 14) Q 188.63 F=0 F 0.00 pr: 0.00 CM C120 'P 3.00 PF 0.03 PT 38.41 ( 13) 53 33 2.154 L 1.00 0.0136 PT 30.32 ( 33) Q 39.14 F=T F 10.00 Pr -0.43 1tN C120 T 11.00 PV 0.15 43 53 1.687 L 97.67 0.0446 PT 30.04 ( 53) Q 39.74 F=T F 8.00 YP; 0.00 BL C:l20 'e 105.67 PF 4.71 13 43 2.154 L 8.00 0.0136 P'1' 34.75 ( 43) Q ?9.1,4 F=T F 10.00 PE 3.46 RN C120 'r 38.00 PF 0.24 1.2 13DQ 188.63 4.260 L 9.00 0.0127 PT 38.45 ( 1.3) Q 227.76 F=0 E 0.00 PE 0.00 CM C120 T 9.00 PE 0.11 PT 38.56 ( 12) SUBMITTAL SERIAL N0:2349f[-04 12-17-1990 PAGE 12 BR57'IiRANllS 1990 ADUITION REMOTE NW2 I'ROM TO FLOW DIAM EQUIV P-LOSS PRESSURE GPM .LN PIPE PSI/F'1' SUMMARY LEN/FT PSI 42 52 1.687 L 97.67 0.0527 PT 29.28 ( 52) Q 42.84 E=T E 8.00 PE 0.00 BL C120 T 105.67 PE 5.57 12 42 2.154 L 8.00 0.0160 PT 34.85 ( 42) Q 42.84 F=T F 10.00 PE 3.46 RN C120 T 18.00 PF 0.29 11 12DQ 227.76 4.260 L 9.00 0.0175 PT 38.60 ( 12) Q 270.60 E=0 E 0.00 PE 0.00 CM C120 T 9.00 PF 0.16 PT 38.76 ( 11) 31 32 3.260 L 9.00 0.0070 PT 30.29 ( 32) Q 81.53 F=0 F 0.00 PE 0.00 CM C120 T 9.00 PF 0.06 51 31DQ -41.10 2.154 L 1.00 0.0144 PT 30.35 ( 31) Q 90.43 F=T r 10.00 PE -0.43 RN C120 T 11.00 PF 0.16 41 51 1.687 L 97.67 0.0473 PT 30.08 ( 51) Q 40.43 F=T P 8.00 PE 0.00 BL C120 T 105.67 PF 5.00 ll 41 2.154 L 8.00 0.0144 PT 35.08 ( 41) Q 40.43 E=T F 10.00 PE 3.46 RN C120 'i' 18.00 PE 0.26 10 11llQ 270.60 4.260 L 9.00 0.0227 PT 38.80 ( 11) Q 311.03 F=0 P 0.00 PE 0.00 CM C120 T 9.00 PF 0.20 PT 39.00 f 10) 30 31 3.260 L 9.00 0.0020 PT 30.31 ( 31) Q 41.10 F=0 F 0.00 PE 0.00 CM C120 T 9.00 PE 0.02 50 30 2.154 L 1.00 0.0148 PT 30.33 ( 30) Q 41.10 F=T F 10.00 PE -0.43 RN C120 T 11.00 PF 0.16 40 50 1.687 L 97.67 0.0488 PT 30.06 ( 50) Q 41.10 F=T F 8.00 PE 0.00 BL C120 T 7.05.67 PF 5.16 10 40 2.154 L 8.00 0.0148 PT 35.22 ( 40) Q 41.10 E=T F 10.00 PE 3.46 RN C120 T 18.00 PE 0.27 YT 38.95 ( 10) 1 UAMtiTTAL SERIAL N0:2349H-04 12-17-1.990 PAGE ].3 EST BRANDS 1990 ADDITION EMOTE NW2 FROM 'PO FLOW DIAM EQUIV P-LOSS PRESSURE GPM fN PIPE PSI/FT :iUf-1MANY ],h;N/FT PSS 34 35 3.260 L 6.00 0.0022 PT 30.31 ( 35) Q 43.43 F=0 F 0.00 PB 0.00 CM C120 T 6.00 PE 0.01 PT 30.32 ( 34) 5 10 5.295 L 377.12 0.0099 PT 38.95 ( 10) Q 352.14 F=2E/2E F 32.00 PG 2.60 EM C120 T 409.12 PE 4.05 4 5 5.295 L 18.00 0.0099 PT 45.60 ( 5) Q 352.14 F=E/E E 16.00 PE 7.36 FR C120 T 34.00 PE 0.34 3 4DQ 100.00 4.026 L 2.00 0.0596 PT 53.30 ( 4) Q 452.14 F=2GV/T E 24.00 PE 0.00 FR C120 T 26.00 PF 1.55 2 3 4.026 L 1.00 0.0596 PT 54.85 ( 3) Q 452.14 F=CV F 22.00 PE 0.00 Ea C120 T 23.00 Pr 1.37 1 2 4.026 L 2.00 0.0596 PT 56.22 ( 2) Q 452.14 F=0/GV F 2.00 PE 0.43 FR C120 T 4.00 PF 0.24 0 1 6.140 L 150.00 0.0057 PT 56.89 ( 1) Q 452.14 E=T,GV%2E,T F 108.00 PE 0.00 UN C140 T 258.00 PE 1.47 PT 58.36 ( O) PRESSORE AVAILABLE AT NODE 0 AT 852.1 GPM 68.5 PSI MAXIMUM PRESSURE UNBALANCE IN LOOPS 0.092 PSI MAXIMUM VE;LOCITY IN PIPES 16.27 FFS . WATE`r2 FLCNJ TEST =U~ .°+'ARY ~t-tE=T :tydrart Ouctet LD Pitot Press. Flaw Resi6ti e: Ttr-e:- Ccrt. 'j o. ~'}O - i nc,'~e s Ds i g;rn q ~2 ress: 3 To[a! Flow tic Press: Fiow B- yP TTf F i i i iTi i~~?7f(TTTI7Tf ~lTf i,j rCTT771 120 - ~ ~ 115 , n0- i05 - ioo - ~s - - 90 ss - ~ . - 75 o -7"0 70 ~ E5 _ ? o • - 6] C5 5- 55 _ 50 452.\4 ~ 45 sg.4- PSZ - . 40D(:~4kv iko5t E ;5 ! ~ 1 3- - i 25 20 - _ j IS ~ Sca!e: ~ ~ ic i}~DE~E2iDfKT . C M11 ~ n~ ei ~ I~ I tt ii Sr+ ~ '~6 BB 43@ 669 Sci4 C 400 too ;i^'J ~6:C 2X19 24C0 2400 ~ Wates Ffo+v arn 77. Sp}S~II', 1 IsI:SAL N0:2349H-04 11-20-1990 PAGV 1 BEST BRANDS 1990 ADDITION MEZZ REMOTE 3 .21/1500 BEST BRANll5 1990 ADDITION 1765 YANKEE DOODLE ROAD EAGAN MN IFP JOB #91025 INDEPENDENT FIRE PROTECTION INC 390 93RD AVE NW MINNEAPOLIS MN 55433 CALCULATED BY HARRY WIEBE RELIABLE "G" 286F K=8.2 100 GPM :INSIIIE }IpSri: 400 GPM OUTSIDE HOSE 433.61 GPM 41.69 PSI REQUIRED AT BASE OF RISER F'.L014' 'I'1tiS9' ItIiF:1.iI,TS S'I'n l j c' 70.00 PSI i;i,:;;CDUAL AT 2990.0 GPM 55.00 PST P12F;SSURE AVAILABLE AT 833.6 GPM 68.59 PSI SUMMARY OF SPRINKLER OUTELOWS ACTUAL MINIMUM SPR FLOW FLOW K-EACTOR PRESSURF 301 28.46 27.30 8.20 7.2.05 302 27.51 27.30 8.20 11.26 303 27.48 27.30 8.20 11.23 304 27.93 27.30 8.20 11.60 309 28.44 27.30 8.20 12.03 310 21,4v 27.30 8.20 11.24 311 27.31 27.30 8.20 11.09 312 27.90 27.30 8.20 11.57 317 28.42 27.30 8.20 12.02 318 27.48 27.30 8.20 11.23 319 27.30 27.30 8.20 11.08 320 27.89 27.30 8.20 71.57 'POTAL WATER REQUIRED FOR SYSTEM 333.61 GPM OUTFLOWS AT 4 100.00 GPM OUTSIDE HOSE STREAMS AT 0 400.00 GPM TOTAL WATER REQOIREMENT 833.61 GPM PRESSURE REQGIRED AT 0 43.10 PSI MAXIMUM I'RI?SSURE ONBALANCE IN LOOPS 0.073 PS1 MAXIMUM VELOCITY IN PIPES 11.90 EPS SU11M].7^i'AL SERIAL No:2349x-04 11-20-1990 }v\C;r 2 BEST BRANDS 1990 AUDITION MEZZ REMOTE 3 .21/1500 E'ROM TO FLOW DIAM EQUIV P-LOSS PRESSURE GPM IN PIPE P5I/FT SUMMARY LEN/ET PSI 320 319 1.452 L 13.00 0.0315 PT 11.08 (319) Q 21.86 F=0 E 0.00 PE 0.00 BL C120 T 13.00 Yi:' 0.41 321 320DQ 27.89 1.452 L 13.00 0.1442 PT 11.49 (320) Q 49.75 F=0 F 0.00 PE 0.00 BL C120 T 13.00 PF 1.87 322 321 1.452 L 13.00 0.1442 PT 13.36 (321) Q 49.75 F=0 F 0.00 PE 0.00 Fsl. C.1 "l0 13.00 PF 1.87 323 322 1.452 L 13.00 0.1442 PT 15.23 (322) Q 49.75 F=0 F 0.00 YE 0.00 EL C120 T 13.00 PE 1.87 57 323 1.452 L 0.41 0.1442 PT 17.10 (323) Q 49.75 F=0/T F 6.00 PE 0.00 SL C120 T 6.41 PF 0.92 37 57 1.452 L 1.00 0.1442 PT 18.02 ( 57) Q 49.73 F=T E 6.00 PE 0.43 RN C120 T 7.00 PF 1.01 38 37DQ -38.76 3.260 L 10.00 0.0002 PT 19.46 ( 37) Q 10.99 F=0 F 0.00 PH 0.00 CM C120 T 10.00 PF 0.00 58 38 1.452 L 1.00 0.0088 PT 19.46 ( 38) Q 10.99 F=T F 6.00 PE -0.43 RN C120 T 7.00 PF 0.06 48 58 1.452 L 97.67 0.0088 PT 19.09 ( 58) Q 10.99 F=T/T F 12.00 PE 0.00 BL C120 T 109.67 PF 0.97 18 48 1.452 L 8.00 0.0088 PT 20.06 ( 48) Q 10.99 F=T F 6.00 PE 3.46 RN C120 T 14.00 PE 0.12 17 18 4.260 L 10.00 0.0000 PT 23.64 ( 18) Q 10.99 F=0 E 0.00 PE 0.00 CM C120 T 10.00 PF 0.00 PT 23.64 ( 17) 31P :ti9 1.452 11 13.00 0.0024 PT 11.08 (319) Q 5.44 E'-0 E 0.00 PE 0.00 BL C120 T 13.00 PF 0.03 SUBMITTAL SERIAL N0:2349H-04 11-20-1990 PAGE 3 BEST BRANDS 1990 ADDITION MEZ'L REMOTE 3 .21/1500 FROM TO FLOW DIAM EQUIV P-LOSS PRESSURE c,PM IN PIPE PSI/FT SUMMARY L EN / F'f` P 5 I 317 318DQ 27.43 1.452 L 13.00 0.0672 P'C 11.11 (31.8) Q 32.91 F=0 V 0.00 PE 0.00 BL C120 T 13.00 pI? 0.87 316 3171)Q 28.42 1.452 L 13.00 0.2124 PT 11.98 (317) Q 61.34 E=0 F 0.00 PE 0.00 BL C120 T 13.00 PF 2.76 47 316 1.452 L 5.50 0.2124 PT 14.74 (316) Q 61.34 F=T F 6.00 PE 0.00 BL C120 T 11.50 PE 2.44 17 47 1.452 L 8.00 0.2124 PT 17.18 ( 47) Q 61.34 F=T F 6.00 PE 3.46 RN C120 T 14.00 PF 2.97 16 17DQ 10.99 4.260 L 10.00 0.0015 PT 23.61 ( 17) Q 72.33 F=0 F 0.00 PE 0.00 CM C120 T 10 . 00 PE 0. ti 1 PT 23.62 ( 16) 312 311 1.452 L 13.00 0.031.6 PT 11.09 (311) Q 21.89 F=D F 0.00 PE 0.00 BL C120 T 13.00 PE' 0.41 313 312DQ 2?.90 1..452 L 13.00 0.1444 PT 11.50 (312) Q 49.78 E=0 E 0.00 PE 0.00 BL C120 T 13.00 PE 1.88 314 313 1.452 L 13,00 0.1444 PT 13.38 (313) Q 49.78 F=0 F 0.00 PE 0.00 BL C720 7 73.00 PF 1.88 ;i'i '14 1.452 L 13.00 0.1444 PT 15.26 (314) Q 49.78 r'= 0 r' 0.00 PE 0.00 nL c120 T 13.00 r?rl 1.9 ~ 56 315 1.452 11 0.41 0.1444 PT 17.14 (315) Q 49.78 F=0/T F 6.00 PE 0.00 BL C120 T 6.41 PF 0.93 36 56 1.452 L 1.00 0.1444 PT 18.07 ( 56) Q 49.78 F=T E 6.00 YE 0.43 RN C120 T 7.00 PE 1.01. PT 19.51 ( 36) 310 311 1.452 L 13.00 0.0024 PT 11.09 (311) Q 5.43 F=0 F 0.00 PE 0.00 BL C120 t' 13.00 PF 0.03 Xt.1*11'I^CAL SERIAL N0:2349H-04 11-20-1990 PAGE 4 FsRST BRANDS 1990 ADDITION MEZZ REMOTE 3 .21/1500 CROM TO FLOW DIAM RQUIV P-LOSS PRESSUR}: GPM IN PIPE PSI/F9' t, i.MP'1.4HY I,h-N i FT PSI 309 310DQ 27.49 1.452 1_1 13.00 0.0672 PT 11.12 (310) Q 32.92 E'=0 F 0.00 PE 0.00 BL C120 '1' 13.00 PF 0.37 308 309DQ 28.44 1.452 L 13.00 0.2125 PT 11.99 (309) q_ 61.35 E=0 F 0.00 PE 0.00 BL C120 T 13.00 PF 2.76 46 308 1.452 L 5.50 0.2125 PT 14.75 (308) Q 61.35 F=T F 6.00 PE 0.00 B1; C120 T 11.50 PF 2.44 16 46 1.452 L 8.00 0.2125 PT 17.19 ( 46) Q 61.35 F=T F 6.00 PE 3.46 RN C120 T 14.00 PF 2.97 15 16DQ 72.33 4.260 L 1.0.00 0.0047 PT 23.62 ( 16) Q 133.68 F=0 F 0.00 PE 0.00 CM C120 T 10.00 PE 0.05 PT 23.67 ( 15) 304 303 1.452 L 1.3.00 0.0319 PT 11.23 (303) Q 22.02 F=0 F 0.00 PE 0.00 BL C120 T 13.00 PF 0.41 305 304DQ 27.93 1.452 L 13.00 0.1453 PT 11.64 (304) Q 49.95 F=0 E' 0.00 PE 0.00 BL C120 T 13.00 PF 1.89 306 305 1.452 L 13.00 0.1453 PT 13.53 (305) Q 49.95 F=0 F 0.00 PE 0.00 BL C120 T 13.00 PF 1.89 307 306 1.452 L 13.00 0.1453 PT 15.42 (306) Q 49.95 F=0 F 0.00 PE 0.00 BL C120 T 13.00 PF 1.89 55 307 1.452 L 0.41 0.1453 PT 17.31 (307) Q 49.95 F=0/T F 6.00 PE 0.00 BL C120 T 6.41 PE 0.93 35 55 1.452 L 1.00 0.1453 PT 1I8.24 ( 55) Q 49.95 }?='1' F 6.00 PE 0.43 RN (1120 '1 7.00 PF 1.02 PT 19.69 ( 35) 302 303 1.452 I, 13.110 0.0C!24 PT 11.23 (303) Q 5.45 G=0 F 0.00 PF 0.00 BL C120 T 13.00 PF 0.03 SUBMITTAL SERIAL N0:2349H-04 L1-20-1990 PAGE 5 BES`P BRANDS 1990 ADDITION MEZZ RF,MOTE 3 .21/1500 EROM TO NLO[v DIAM EQUIV P-LOSS PRESSURE GYM IN PIPE PSI/FT SUMMARY LEN/FT PSI 301 302DQ 27.51 1.452 L 13.00 0.0673 PT 11.26 (302) Q 32.97 F=0 F 0.00 PE 0.00 BL C120 T 13.00 PF 0.87 300 301UQ 28.46 1.452 L 13.00 0.2130 PT 12.13 (301) Q 61.43 E=0 F 0.00 PE 0.00 BL C120 T 13.00 PF 2.77 45 300 1.452 L 5.50 0.2130 PT 14.90 (300) Q 61.43 P=T F 6.00 PE 0.00 BL C120 T 11.50 PF 2.45 15 45 1.452 L 8.00 0.2130 PT 17.35 ( 45) Q 61.43 F='1' F 6.00 PE 3.46 RN C120 T 14.00 PF 2.98 14 15DQ 133.68 4.260 L 6.00 0.0096 PT 23.79 ( 15) Q 195.11 F'=0 F 0.00 PE 0.00 CM C120 T 6.00 PE 0.06 Y'P 23. 85 ( 14) 36 37 3.26+; L 10.00 0.0018 PT 19.52 ( 37) Q 38.76 E=0 F 0.00 PE 0.00 Ctvi C120 T 10.00 PF 0.02 35 36DQ 49.78 3.260 L 10.00 0.0082 PT 19.54 ( 36) Q 88.54 E'=0 E 0.00 Pr; 0.00 CM C1.20 'c 10.00 PF 0.08 34 35DQ 49.95 3.260 I, 6.00 0.0187 PT 19.62 ( 35) Q 138.49 E=0 E 0.00 PE 0.00 CM C120 T 6.00 PE 0.11 160 34DQ -75.21 2.154 L 10.00 0.0330 PT 19.73 ( 34) Q 63.29 F=T/E F 15.00 PE 7.79 CM c120 T 33.00 PF 1.09 161 160 2.154 L 6.00 0.0330 PT 28.61 (160) Q 63.29 F=0 F 0.00 PE 0.00 CM C120 T 6.00 PF 0.20 162 161DQ -15.80 2.1.54 L 10.00 0.. P'i' 28 .81_ (161) Q 46.48 F=U E 0.00 PE 0.00 CM C120 T 10.00 PF 0.19 163 162DQ -15.70 2.154 L 10.00 0.0087 PT 29.00 (162) Q 30.78 F=0 F 0.00 PE 0.00 CM C120 T 10.00 PF 0.09 1.64 163UQ -15.53 2.154 L 10.00 0.0024 PT 29.09 (163) Q 15.25 F=0 E 0.00 PF: 0.00 ' CM C120 'r 10.00 PF 0.02 SUBMITTAL SERIAL N0:2349H-04 11-20-1990 PAGE 6 BEST BRANDS 1990 ADDITION MEZZ REMOTE 3 .21/1500 FROM TO FLOW DIAM EQUIV P-L055 PRESSURH' GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 154 164 1.452 L 96.00 0.0162 PT 29.11 (164) Q 15.25 F=2T/2T F 24.00 PE 0.00 BL C120 T 120.00 PE 1.94 153 154 2.635 L 10.00 0.0009 P7' 31.05 (154) Q 15.25 F=0 E 0.00 PE 0.00 CM C120 T 10.00 PF 0.01 PT 31.06 (153) 153 163 1.452 L 96.00 0.0167 PT 29.12 (163) Q 15.53 F=2T/2T F 24.00 PE 0.00 BL C7 20 Ii20.00 PF 2.00 152 153DQ L5.25 2.635 C, 10.00 0.0033 P`C .11.12 (153) Q 30.78 F=0 F 0.00 PE 0.00 CM C120 T 10.00 PF 0.03 PT 31.15 (152) 152 162 1.452 L 96.00 0.0171 PT 29.03 (162) Q 15.70 F=2T/2T F 24.00 PE 0.00 BL C120 T 120.00 PE 2. (1`, 157. 30.73 2.635 L 10.00 0.0070 PT 31.08 (152) Q 46.48 F=0 F 0.00 1:)t,: 0.00 CM C120 T 10.00 PF 0.07 PT 31.15 (151) - 151 161 1.452 L 96.00 0.0194 PT 28.85 (161) Q 16.80 F=2T/2T P 24.00 PE 0.00 BL C120 T 120.00 PF 2.33 150 151DQ 46.48 2.635 L 6.00 0.0124 PT 31.18 (131) Q 63.29 F=0 F 0.00 PE 0.00 CM C120 T 6.00 PE 0.07 14 150 2.635 L 18.00 0.0124 PT 31.25 (150) Q 63.29 F=T/E F 16.00 PE -7.79 CM C120 T 34.00 PF 0.42 13 14DQ 195.11 4.260 I, 3.00 0.0161 PT 23.88 ( 14) Q 258.40 E=0 F 0.00 PE 0.00 CM C120 T 3.00 PF 0.05 PT 23.93 ( 13) 33 34 3.260 L 3.00 0.0060 PT 19.77 ( 34) Q 75.21 F=0 E 0.00 PE 0.00 CM C1.20 T 3.00 PF 4.02 53 ?:?i;~~~ ;5 2.154 L 1.00 0.0029 PT 19.79 ( 33) Q 16.55 F=T E' 10.00 PL: -0.43 RN C1_20 T 11100 PF 0.03 SUBMITTAL SERIAL NO: 2i;.9~i;•-Od 11-20-1990 PAGE 7 BEST BRANDS 1990 ADDITION MEZZ RETIOTE 3 .21/1500 FROM TO FLOW DIAM F'QOIV P-LOSS PRE55URE GPM IN PIFE PSI/FT SUMMARY LEN/ FT P;; J 43 53 1.687 L 97.67 0.0094 PT 19.39 ( 53) Q 16.85 F=T F 8.00 PE 0.00 BL C120 T 105.67 PF 0.99 13 43 2.1.54 L 8.00 0.0029 PT 20.38 ( 43) Q 16.85 E=T F 10 . 00 PE 3.46 RN C120 T 18.00 PF 0.05 12 13DQ 258.40 4.260 L 9.00 0.0181 PT 23.89 ( 13) Q 275.25 F=0 F 0.00 PE 0.00 CM C120 T 9.00 PE 0.16 PT 24.05 ( 12) 32 33 3.260 L 9.00 0,0038 PT 19.78 ( 33) Q 58.35 F=0 F 0.00 PF 0.00 CM C120 T 9.00 PF 0.03 52 32DQ -39.99 3.068 L 1.00 0.0006 PT 19.81 ( 32) Q 18.37 F=T E 15.00 PE -0.43 RN C120 T 16.00 PF 0.01 42 52 1.687 L 97.67 0.0110 PT 19.39 ( 52) Q 18.37 F=T E' 8.00 PE 0.00 BL C120 T 105.67 PF 1.16 12 42 2.154 L 8.00 0.0033 PT 20.55 ( 42) Q 18.37 F=T F 10.00 PE 3.46 RN C120 T 18.00 I?h' 0.06 11 12DQ 27,,.7.5 4.260 L 9.00 0 ,1) %n4 P'r 24.07 ( 12) Q 293.62 E=0 E 0.00 PL 0.00 CP1 C120 T 9.00 PF' 0.18 PT 24.25 ! 11) 31 32 3. 2Gis L 9.00 0.007.9 11'I' 19.80 ( 32) Q 39.99 F=0 F 0.00 PE 0.00 CM C120 T 9.00 YF 0.02 51 31DQ -20.70 2.154 L 1.00 0.0037 PT 19.82 ( 31) Q 19.29 F=T F 10.00 PE -0.43 RN C120 T 11.00 PF 0.04 41 51 1.687 L 97.67 0.0120 PT 19.43 ( 51) Q 19.29 F=T F 8.00 PE 0.00 BL C120 T 105.67 PF 1.27 11 41 2.154 L 8.00 0.0037 PT 20.70 ( 41) Q 19.29 F='P F 10.00 PE 3.46 RN C120 T 18.00 PF 0.07 SUBMITTAL SERIAL N0:2349H-04 11-20-1990 PAGE 8 BEST BRANDS 1990 ADDITION ,;MEZZ REMOTE 3 .21/1500 FROM TO FLOW DIAM EQUIV P-LOSS PRESSURE i GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 10 11DQ 293.62 4.260 L 9.00 0.0229 PT 24.23 ( 11) Q 312.91 F=0 P 0.00 PE 0.00 CM C120 T 9.00 PF 0,21 PT 24.44 ( 10) 30 31 3.260 L 9.00 0.0006 PT 19.79 ( 31) Q 20.70 F=0 F 0.00 PE 0.00 CM C120 T 9.00 PE 0.01 50 30 2.154 L 1.00 0.0042 PT 19.80 ( 30) Q 20.70 F'=T E 10.00 PE -0.4-3 RN C120 T 11.00 p I." U.uS 40 50 1.687 L 97.67 0.0137 PT 19.42 ( 50) Q 20.70 E=T E 8.00 PE 0.00 BL C120 T 105.67 PF 1.45 10 40 2.154 L 8.00 0.0042 PT 20.87 ( 40) Q 20.70 F=T F 10.00 PE 3.46 kN C120 T 18.00 PF 0.08 5 10DQ 312.91 5.295 L 377.12 0.0089 L',t, 24.41 ( 10) Q 333.61 E=2E/2E F 32.00 PE 2.60 FM C120 T 409.12 PF 3.64 4 5 5.295 L 18.00 0.0089 PT 30.65 ( 5) Q 333.61 I?='i',GV/E E 35.00 PE 7.36 ER C120 T 53.00 PF 0.47 3 4DQ 100.00 4.026 L 2.00 0.0551 PT 38.48 ( 4) Q 433.61 F=GV,T F 22.00 PE 0.00 FR C120 T 24.00 PF 1.32 2 3 4.026 L 1.00 0.0551 PT 39.80 ( 3) Q 433.61 F=CV F 22.00 PE 0.00 FR C120 T 23.00 PF 1.27 1 2 4.026 L 1.50 0.0551 PT 41.07 ( 2) Q 433.61 F=0/GV F 2.00 PE 0.43 FR C120 T 3.50 PF 0.19 0 1 6.140 L 150.00 0.0053 PT 41.69 ( 1) Q 433.61 F=T,GVt:,T E' 108.00 PE 0.00 UN C140 T 258.00 PF 1.37 PT 43.06 ( 0) PRESSURE AVAILABliE AT NODE 0 A'P 833.6 GPM 68.6 PSI MAXIMUM PRESSURE UNBALANCE IN LOOPS 0.073 PSI MAXIMUM VELOCITY IN PIPES 11.90 FPS WATER FLOitV TEST SUAAtvIAFZY SHE,-T ~~raK Ouz{et !_D Pitot P~ess. Fto.v Rtsid~.Jal Date: . No. ir~~es P5i [jxn i Cort. yo. . 1 COrX. F1drrC:: t5 ~ 2 aaa~s5: IZ ~ 3 Total Ftow Static Pr^ess: -7 0 Dsi Flow ',S 5= asi Z~) + yPtr+ 1 1 120 TT7T -rTTTTrTTT -T-rTT TMTM 115 nl~.z z r~cnu,o-z-~- 3 ~ iio ~ 105 loo 7s 90 as ~ . ~ 75 0 3D 70 ~ ~ 65 _ a _ b) ' L5 C5 55 ~ 50 s~ ~ ,5 f 35 400 uwk- ao-rsI~, kbSa I ' ! 433,~,~ GPt~ - ~ 2` - 43 . \ PSZ ~a ~ ~c tHGEFEtiDff{i C - I3( Y~•ECTK~ ~K. _ C. I~ ~ 1 1~ ~ i In I t II II il ~ }j~lf s~,< c aa Watet Fiow tCxn /-c)+ raA .:~c~cr.nnn~~~vn,n~»~~nGr~,ni>n.nr.~.r~.r~i> >.n~~i~i~.nni~t~.nc~.n~.nz~t~avt~nnr~.n.n~~.nr~r.7n.nc,n.nanr,nnn.n.nr~nn~7t~nnr~t>~~c~.° 3 Fiyr.irauI ic:s `;unlm;ary Shic;et , i i 3 Thll)EPL'.hIIICMT F1Rk. f'I<OTt?.CTCOhI T.PIC De.,igner: li tJCt:t3L 3 .i' 5510 93R17 hillF.: Plld C'a ic: F.ty; hS W]'.f:EtE 3 j' M:[I`IPI"L',HF'pl.[S; hIM 55d3:3 Date: 10..13-9:1 5' Y 3 ;'1>(,7/,7/.~%~C.~lJl~1.7.P4.I~.l~I.70(~1.~/.~I,~1~1.7L7/.1L7/.7I.71~L>L~L7/.>(,7CII,lUl.7l~/.7L7/.7/.71~L71j:' .:'U/.~L>I~CRL7(.~.R1.7D4/,~/,~D.(Il~l/L11.7(JL~UI.71.~Cr%~/,>Ul7/.7.' 3` Prnjeat l:ni'nrmatrori Hytlraulics Irifnrmatictin 3 _s• 3 s' 3 Nt ST EtRFlMII`.; nemarid. 3 _S' 1765 Y F l PI iC 1 : . 1 ; . D O O O L E f2 p(l [i Spr i n k 1 e r__. 3 PST i j' L"f16Flhl hIM 3 REquii ecl 1'res: 51.50 i 3_i Reiqllir•cicS F I0w: 342..41 [iPI'i 3 rtaric I?,leaV: 0 .G(7 I"r ~ , f:onti-:ar..i: Mo: 92042 sy_,Y:P:III .r± Nu i I~I rnr{: ].393 f117U7.1 CC1P1 i" 3 Tota I Presr• 5?.l.l a`.il. 3 3 5ystwin ID: 15193..1. 3.? Hdd' 1 Floais: 250.00 GIsM ~7. 3 kef Uraiafny: 1 qf' G A 3 Fiose aT, 5rre: 0.00 rf'M ; _i Tnt'al Flaw: 592.42 (i4'11 3 Const: S'fkEL BERhI & BFlR ,IiIIST 3 3 e 17CCupanCy:: C..OMMli.ff(::[,NL 3_i' Sup{:ily.„ 3 J! _s' Water F low Test 3 _s' Ri.ithority: 7.50 fpMhiERC.[RI,. R.T.SI( St:CdU.iCES 33 SL'aL'iC: 10.00 PSI Residua 1: 55.00 1'S7 S a L 7 ( . 7 / , 7 G 7 p 1 7 / . 1 / . ~ p p [ r C / D L l 4 / . 1 L ~ / . J / , 7 ~ ~ % i / ~ / , J / , 7 l . 7 C l L 1 % 1 D 1 . ~ n l ~ C i L ~ l i / , r 4 / . 1 1 , 7 L r D ~ l , > L ~ Y a' Q t y F 1 n wi n S! : 2990.00 GPt1 3 ,:'C~I~I~.C~.Crli[~~~~L~L7l7l~UL~I~C~.F~I~~I~C~G~l7pZ7[1L~l~.fiC~t~L~l.'~L7l~L~DL'rL"iC~C~I~? S F T C 1 e v e r, i o n: 0.00 F r, 3 A SysP:em Informar, inn S 3 [Jar.e: T iioe:.._......_.._. .:7 5' 1 3 E.iy: C1".T'r Of` 1=HrAPl 3 hiydrau I ic, Ues ign C.r iCeri.a 3 3 3 s Standard: IVF'F'fl 13 p'uinp Uata ; _i' NaZnrd: [If2l`l:l'.hlf'if2'i 1.1 . _i Ratc;d (I`IF) I''Sl.@ (hlh'1) fiF'hl _r' 3 Pigure: 5--2.:3 Cirve: 3 3 Etuust Pr•es (MM) PSI i A System Iypc: WET 3 S' pischarge Nres (NR) PSI 3 _i Ili,cl'iarge f"lnid (PI11) GI'hi 3 Derisiry: .20 (54%hi /Sq1 t S' 3 A liemote Hrea: 1500 SqC t 3 inad 3 Sp' CU~d: 1.3f1 SqFT, .i _St:att IC: (MA) "S:[ S S' Residudl: (NR) P S I: _i S' ;prinklers & hln;zies 3 j, Floui: fiVA) rPi1 i Manufac: 1"tELSRBLE 3 i9adr, i; flv;-:+r Ia ti le.. J, 3 S ize: 112" 3_i 1') 69.25 nS:C@ 592.42 GPi1 i " It~-ra~;c~or; , r.sz ' F`) 52.12 f"_"I@ ?787.1.i' 6f'hl _7 ~ ° e: T A . ..i j r 6.tOl41 }~e1T.'I 1"1 ~;;I.' 6 ,a .3' J (l 21 I" [J i fl . . . 6'rewS.i~P'e: 11.13 PST. 3.; F Inw: 16:34, f'S (.I'M ; t~L~I7L'N."it~L~i~L~i7LiDL~00.1~t7t7L71'~Dl"~P~UL~ht"il.~d~D,/i%r~l[7UliC~i~L7~17GCN.'~9' G~'!~L"~l~l~l'~L7L'iUI,~L~i.~/.'~l~l~I.iC~L~L~LrC~L7l7171717nl.7C~~17f V 3 Sigma Dynamres Cnrporation 7700 Mydr>+ulics J t?C~L~%N.~nCtOUC~L"rpPG~l~~C~/r['1Ci/.>Grnitl."~l'~l'~l~L7L~l~l'~l~L'~C~[~G~D~~I.."~l~l."~L~~~Irl>lll"~Pl~l.'~C~GL'rG~~il'~C~I~f~L"~G~l~l~l~l~l~l~l7l.'~C~Ct~1(r~i~> y ill ~ • . SII13i4:11'IHl. WEI"'t:IFlI Ni]:2349HY1 10-13_1993 NFiGE A. Rt"i'i0"fk; ilR(1Ji'llli;'i Rl'.l:il"f rI01J TfSf Nli;lll_"(i y:iY,c:r SI,i17t:i ll! .ST"rI1I.C ;(i,(lfj NST. N I;. i Da. IJ (i I,. 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System Demand._ Water Supply._ ` Sprinkler Demand 51.50 PSI @ 342.41 GPM Static 70.00 PSI Additional Flows 250.00 GPM Residual 55.00 PSI @ 2990.00 GPM Hose.at Source 0.00 GPM Elevation 0.00 PSI ~ Total Demand ~ 52.12 P5I 0 592.42 GPM ~ ' R t~,o~ ~ ~tr,Gk I ~'~''lrlr~i~rl1L; l~ ~L1/iIrt1~'11, pCJI~Ui~Lll~~~l71~ IrL7l~l'CiI~UI,~L~Gfl~l~/~UI.'~I"~t~lJ!/l, l+t1l~l?lf e` J, F3 U[I i' a I . ! l ' 1 r , : : c ; i l! Ol Ifl ::t I" y ShFeC J' t' ; CPID£iPk_NDlENi t:(.FtI:: P120CfS.r.TXt)IV S_hlC CJe1,ignei•; H ld:[i:.l;E. 5' 390 9 3}i D H U E Nld a 1 c: k; y: Pi W'.I'. BF J 5' MS.IVI`IC;'.f'l1't)!..:[.5; MPI 5540'. litdre: 10-26-93 3 Fro,jccr ]:nfnrmatron 3 S` iiS,ciraulics Irifi'ormation i 3 J , ~ , C3LS T B WRPIDS Oemand Spri~7klEr....... . ' j' 1765 'rWNI;FF C)ilODl,E RltHO 3 A _ ~ `i°..s. FeU.Si f~il'. J ? k1Rf7f~l` i91`I 3 3 IGUq~liP'GU' ~ , _4' ~r' ..r` I F . q u 1 ieCI. F 1 olJ : 1249.60 G P M .a° ?1 `i Y ,il t: 'I r E1 e'.'J : 0.00 FT: j, e, 0 I"I t; i.~ l f.i 94042 _i _i Sl~S 1:. E3 IIl . I $uiitlirlg: 1:393 FlUI)STTOhI 3 IGt:al I'i"<.s: Fifi.Eii3 s` I Sysi;ent :T.D: 1993-1, 3 3 HCicl' 1 F Inw=:; 500..00 GI°'M _r' 3Refi Di',iwing: 2 0 F _i' 3 liusn zst S;rce: 0 .JCI GPI'I 3 3 3 3 Tol'a?i f"loid; 1749.69 f1'M 3 _ CnnsY,: SRFRM & BFlfi JG1.S"f .4 11 Q.r,.cuparrcy: 6lHF;FNOUSE Supp14.., 5 . a t e r F i c~~~ (~E~~°r, + lJ . . _ w ~ i ` N~~tPtcrr'iP:Si: 1'...;I"1 f;UM~~k'.ftf;~C11L I'7',;k c ~,f:.I{L7.~,t..ti ; 0 Wt:=it i c70 . q f fa i.1 ~ R e•. s 9 cl i c~., i i7 !~l/DL~L~l~C~l~U011J.~1717L"1j7Z111/1/](]/Jl!/,"I(!jl(!j7/7L1l3%1%1/Jjlj!(lJIL!!!j!C!%!!,a/7j' A QCv FIGId liig: 2990..00 r;;:>M j' f T f. i c• vas, i o n: 0.00 1` t ; 5ysc.am Cnfiarmzition S' 3 li::sr,e:........ T~im~-~: _ a _t 3 r;si: CT.TY t11 EiRGflPI HVdi"dtll iCf, DSStgi`I (;i' IY,ei" IZS _1 .i o, i' St:arinard, I;FF'R 231(; J' Data___... 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