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HomeMy WebLinkAboutPP - 6955 SOUTHCENTER BLVD - HOMEWOOD SUITES - PERMITS AND PLANS6955 SOUTHCENTER BLVD ASSOCIATED PERMITS 91-S-300 910251 W B LEHNER & ASSOCIATES FIRE PROTECTION ENGINEERS 307 N. Olympic Ave., #208 Arlington, WA 98223 (206) 435-2549/FAX 435-6424 August 17, 1991 To: Mr. Fred Bowman 9924 NE 200th Bothell, WA 98011 Re: FIRE PROTECTION ENGINEERING REVIEW #1 HOMEWOOD SUITES DEVELOPMENT Tukwila, WA Dear Mr. Bowman: We have reviewed the fire sprinkler system underground piping, downstream from and including the detector check vaults shown on Drawing No. SP -1, "FIRE PROTECTION SITE PLAN", submitted by you 8- 16-91. That portion of Drawing SP -1 is ACCEPTED AS NOTED, (notes on second sheet and attached to plans): Should you have any questions please call at your convenience. Sincerely ou lie W.B. ehner, P.E. 91902-R2.WPS W B LEHNER & ASSOC. cc Marshal Nick Olivas DRAWING SP -1; REVIEWED by W. B. Lehner, P.E. Date: 8-17-91 ACCEPTED AS NOTED: Plan note numbers refer to comments below. NOTE # COMMENTS 1. Designate size of vault and manufacturer, and obtain Approval from Tukwila Water Dept. before installation. 2. Recommend omission of OS&Y valve from downstream end of double detector check. 3. Equip F.D.C. check with automatic drain, spill to vault floor drain. 4. Protect indicating valve posts as necessary from traffic. 5. General Note indicating installation to be per NFPA-24 is too general. Inspection` items should include the following (reference NFPA-24 paragraph numbers): a. 8-3.2; NO unnecessary joints are allowed under the building. b. 8-5.2; CLEAN ALL bolted joint accessories and COAT with asphaltum. c. 8-6.2; Rodding & clamping, thrust blocking, and retainer glands to be installed strictly per this section. d. FLUSH clear for 6" pipe and certify before connecting underground to sprinkler pipe. e. 8-9; TEST piping scrupulously per this section 8-9. CONTACT the City to WITNESS testing and INSPECT the installation BEFORE cover. 6. Pipe locating dimensions are only shown for lead-ins, but should be shown for all runs of piping. Provide as -built locations as a minimum. atm i, 1 NMI MIN OMNI HOMEWOOD SUITES HYDRAULIC CALCULATIONS pTUKWILA FIRE DEPARTMENT 9/ 5, j 2 W. B. LEHNER & ASSOCIATES Fire Protection Engineers o ACCEPTED ACCEPTED AS NOTED o RESUBMIT ❑ REJECTED for Date. CiCt 121991 P. ' JOB. NO. HYDRAULIC SUMMARY SHEET CUSTOMER'S P.O. NO. CUSTOMER'S NAME HaMELvoab SuirES • • ADDRESS 6.42S ,5• CENT ,31-v0 1 DESCRIPTION OF HAZARD DRO. CTAtOV, 7 AUTHORITY HAVING JURISDICTION 7 JKL✓'1t.A- CALCULATIONS BY /3D L✓ Mot A',,J . SHEET NO 1 OF DRAWING NO s F- 3 Tt/K 1.411- 1. i4 , k.'.+. DATE /o—¢-9/ AREA TO BE CALCULATED SYSTEM REQUIREMENTS ST?? 94I MVI Z N'o F j.1r . OLP 4- 2. REQUIRED DENSITY PER. SQ. FT. • 1 iv • ALLOWANCE FOR INSIDE HOSE STATIONS ALLOWANCE FOR OUTSIDE FIRE HYDRANTS TOTAL WATER REQUIRED: 572— G.P.M. AT / Z 3 ' G P.M. GPM P.S.I. REMARKS' • STATIC PRESSURE IN P S I RESIDUAL PRESSURE: G.P.M. FLOWING 3 / 6-7 ELEVATION LOCATION PUMP DATA: TANK DATA: WATER SUPPLY INFORMATION 4- l AT /08 PSI RATED CAPACITY: G.P.M. AT P S I. ELEVATION LOCATION CAPACITY G.P.M. ELEVATION LOCATION REMARKS* ABBREVIATIONS o - FLOW INCREMENT AT SPECIFIC LOCATION Q - FLOW AT A SPECIFIC LOCATION G.P.M. - GALLONS PER MINUTE P.S.I. - POUND PER SQUARE INCH PT - TOTAL PRESSURE IN P.S.I. PF - PRESSURE LOSS DUE TO FRICTION PE - PRESSURE CHANGE DUE TO ELEVATION EE - 450 ELBOW , E - 900 ELBOW L.T.E. - LONG TURN ELBOW • STAR FORM PISS 3/67 T - TEE C - CROSS DEL. V. - DELUGE VALVE DRY. V. - DRY VALVE AL. V. - ALARM VALVE GV - GATE VALVE CV - SWING CHECK VALVE AV - ANGLE VALVE GLV - GLOBE VALVE ST - STRAINER PRINTED IN U.S.A. - JOB. NO. HYDRAULIC SUMMARY SHEET CUSTOMER'S P.O. NO. CUSTOMER'S NAME HOA45-t.crorC, -(0/7-E--1 ADDRESS 6,92-C S. CE---A/Tr-72_ el -VP DESCRIPTION OF HAZARD O )2.1:) .I SHEET NO / OF DRAWING NO .S P- 4- 77/14L.v>tA, 14,4- DESCRIPTION 4_? L • AUTHORITY HAVING JURISDICTION C/ TY OF 1 V -k W 1 -i -A CALCULATIONS BY / BQWMA-n/ DATE SYSTEM REQUIREMENTS AREA TO BE CALCULATED Arne_ £ AY S YS TC -714 i3 1-17 f- 2 - REQUIRED REQUIRED DENSITY PER. SQ. FT . /!o ALLOWANCE FOR INSIDE HOSE STATIONS D ALLOWANCE FOR OUTSIDE FIRE HYDRANTS • TOTAL WATER REQUIRED: 25'0 7 !o G.P.M. AT G.P.M. GPM P.S.I. REMARKS' WATER SUPPLY INFORMATION STATIC PRESSURE IN P S I /4/ RESIDUAL PRESSURE: 1 G.P.M. FLOWING .3 / .5'7 ELEVATION LOCATION , PUMP DATA: J TANK DATA: AT /OS P S.I. RATED CAPACITY: G.P.M. AT P S I ELEVATION LOCATION CAPACITY G.P.M. ELEVATION LOCATION REMARKS' ABBREVIATIONS o - FLOW INCREMENT AT SPECIFIC LOCATION Q - FLOW AT A SPECIFIC LOCATION - ' G.P.M. - GALLONS PER MINUTE P.S.I. - POUND PER SQUARE INCH PT - TOTAL PRESSURE IN P.S.I. PF - PRESSURE LOSS DUE TO FRICTION PE - PRESSURE CHANGE DUE TO ELEVATION EE - 450 ELBOW E - 900 ELBOW L.T.E. - LONG TURN ELBOW , STAR FORM HSS 3/67 T - TEE C - CROSS DEL. V. - DELUGE VALVE DRY. V. - DRY VALVE AL. V. - ALARM VALVE GV - GATE VALVE CV - SWING CHECK VALVE AV - ANGLE VALVE GLV - GLOBE VALVE ST - STRAINER PRINTED IN V.S.A. N CONTRACT NO. NAME: H b A4 El clow j2 S ADDRESS: 4,1 L S S . C E-riTaR $ LV J 711'14i vI LA MULTIPLY SCALE BY PSI CO ,o t p N1.85 GRAPH 2.344 SHEET SYSTEM NO. 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I MININViIH1iHre ■ ■■ps=mmucIII:�I■�N■IHIHI■HN■iiumpNHNI■ e NN '''777■■N■■/N■■:■u■■N■ N�N�Y■Yq,■h■:■h�■ll�■N�mouti■n■NNli■■■/N■■■■■N■■■■N■■■Y■N■■ i ■■N■■N■NM■N■NY ■N/ �iMw Jnirs■p�ppNr�a..■i�i�i�swisous:aths—N/: unr.rN==WN:NifaN�■p�■::.■�■N=: NaMI:N:IN a lrenli ■■N■:AN:::::N:N.■:NN•NSMM/r MMIXAN::: N:M:"YY NfaN:N~:p:p:N N=NMEINIMIB gMtn aginiN�M. =WA.1NNpp�11N::::=: �N� qNi�p��Y�� N„1NN� M�== �■■�■�■� ���� app �N�/pp�fap��N�N ��p�N�NNp�p�MN�NAN�■YNNN� ui i■'■iiiiiHRf :ii iiiiL' entii■■Nl1='11:IIIIllunamo uIII uullnJ AI 1111■►'■Ni■■■■■■■■i..:'-M■■Y■N■■I .wN ■■■■■B■Nw■■■■■w■■■w■N■N■■r■ ■NI!\■11■N■■■N■N■�'7■N■NpI■NN■O■ N■N■■N■N■■■NN■■■N■■■N■ • ■NN■■M■■■■■YNN■ 1 I'i ii1 1_,1igm - ,.i, 1""."it"il"ii�11 i �."ii Ii�1 11i.i. � a 0I SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD TUKWILA, WA. f BLDG NO. 2 3RD FLR ' 5 SPKR IN CORRIDOR J FLOW TEST RESULTS STATIC RESIDUAL AT 3157.0 GPM PRESSURE AVAILABLE AT 425.9 GPM SUMMARY OF SPRINKLER OUTFLOWS ACTUAL MINIMUM SPR FLOW FLOW K -FACTOR PRESSURE 208 15.18 14.82 209 15.01 14.82 210 14.82 14.82 211 15.05 14.82 212 15.83 14.82 5.60 5.60 5.60 5.60 5.60 TOTAL WATER REQUIRED FOR SYSTEM OUTFLOWS AT 100 OUTFLOWS AT 200 OUTSIDE HOSE STREAMS AT 0 TOTAL WATER REQUIREMENT PRESSURE REQUIRED AT 0 MAXIMUM PRESSURE UNBALANCE IN LOOPS MAXIMUM VELOCITY IN PIPES 7.35 7.19 7.00 7.22 7.99 10-03-1991 PAGE 1 141.00 PSI 108.00 PSI 140.19 PSI 75.89 GPM 50.00 GPM 50.00 GPM 250.00 GPM 425.89 GPM 47.23 PSI 0.086 PSI 10.35 FPS SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD TUKWILA, WA. FROM TO FLOW GPM 110 210 Q 14.82 112 212 Q 15.83 DIAM IN 1.049 AO 1.049 AO 111 211 1.049 Q 15.05 109 209 1.049 Q 15.01 108 208 Q 15.18 30 40 Q 125.89 7 11 Q 175.89 23 30 Q 44.96 1.049 2.635 2.635 2.067 AO AO AO NC NC CM2 L F=T , E F C120 T L F=T F C120 T L F=T F C120 T L F=T F C120 T L F=T F C120 T L F=T,2EE F C120 T L F=2E F C120 T L F=0 F C120 T 200 23DQ -39.03 1.610 L Q 5.93 F=0/T F BL C120 T COMMENT: 50 GPM FOR INSIDE HOSE 13 200D0 50.00 1.610 Q 55.93 11.24 1.610 BL BL2 L F=T F C120 T L F=0 F C120 T EQUIV PIPE LEN/FT 5.50 7.00 12.50 1.00 5.00 6.00 5.50 5.00 10.50 5.50 5.00 10.50 5.50 5.00 10.50 52.00 24.00 76.00 2.50 16.00 18.50 3.50 0.00 3.50 65.50 8.00 73.50 63.50 8.00 71.50 8.50 0.00 8.50 10-03-1991 PAGE 2 P -LOSS PSI/FT O .0747 PT PE PF PT O .0844 PT PE PF PT O .0769 PT PE PF PT O .0765 PT PE PF PT O .0782 PT PE PF PT 0.0441 PT PE PF PT O .0819 PT PE PF PT O .0214 PT PE PF O .0017 PT PE PF O .1083 PT PE PF PT O .0056 PT PE PF PRESSURE SUMMARY PSI 7.00 (210) O .00 O .93 7.93 (110) 7.99 (212) O .00 O .51 8.50 (112) 7.22 (211) O .00 O .81 8.03 (111) 7.19 (209) O .00 O .80 7.99 (109) 7.35 (208) O .00 O .82 8.17 (108) 11.20 ( 40) O .00 3.35 14.55 ( 30) 23.81 ( 11) O .00 1.52 25.33 ( 7) 14.55 ( 30) O .00 O .07 14.62 ( 23) O .00 O .12 14.74 (200) O .00 7.74 22.48 ( 13) 7.90 (110) O .00 O .05 • SUBMITTAL SERIAL NO:2480HY1 • HOMEWOOD SUITES 6925 SOUTHCENTER BLVD TUKWILA, WA. FROM TO 10-03-1991 PAGE 3 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 62 111D0 15.05 1.610 Q 26.29 • 109 110 L 12.50 0.0268 PT 7.95 (111) F=0/T F 8.00 PE 0.00 BL2 C120 T 20.50 PF 0.55 PT 8.50 ( 62) 1.610 L 9.50 0.0007 PT 7.90 (110) Q 3.58 F=0 F 0.00 PE 0.00 BL2 C120 T 9.50 PF 0.01 108 109DQ 15.01 1.610 Q 18.59 52 108DQ 15.18 1.610 Q 33.77 • 112 62 Q 2.84 L 14.00 0.0141 PT 7.91 (109) F=0 F 0.00 PE 0.00 BL2 C120 T 14.00 PF 0.20 L 62.50 0.0426 PT 8.11 (108) F=T F 8.00 PE 0.00 BL2 C120 T 70.50 PF 3.00 PT 11.11 ( 52) 2.067 L 5.50 0.0001 PT 8.49 ( 62) F=0 F 0.00 PE 0.00 CM4 C120 T 5.50 PF 0.00 63 112DQ 15.83 2.067 L 5.50 0.0042 PT 8.49 (112) Q 18.67 F=0 F 0.00 PE 0.00 CM4 C120 T 5.50 PF 0.02 PT 8.51 ( 63) 101 100 1.610 L 71.50 0.0006 PT 8.48 (100) Q 3.28 F=0 F 0.00 PE 0.00 BL2 C120 T 71.50 PF 0.04 COMMENT: 50 GPM FOR INSIDE HOSE 102 101 63 102 Q 3.28 Q 3.28 1.610 L 10.50 0.0006 PT 8.52 (101) F=0 F 0.00 PE 0.00 BL2 C120 T 10.50 PF 0.01 1.610 L 2.50 0.0006 PT 8.53 (102) F=0/T F 8.00 PE 0.00 BL2 C120 T 10.50 PF 0.01 64 63DQ 18.67 2.067 L 8.00 0.0057 PT 8.54 ( 63) Q 21.95 F=0 F 0.00 PE 0.00 CM4 C120 T 8.00 PF 0.05 106 64 Q 21.95 1.610 L 3.25 0.0192 PT 8.59 ( 64) F=0/E F 4.00 PE 0.00 BL2 C120 T 7.25 PF 0.14 • 105 106 1.610 L 1.75 0.0192 PT 8.73 (106) Q 21.95 F=0 F 0.00 PE 0.00 BL2 C120 T 1.75 PF 0.03 • 1 SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD TUKWILA, WA. FROM TO 104 105 103 104 54 103 53 54 10-03-1991 PAGE 4 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI Q 21.95 Q 21.95 Q 21.95 Q 21.95 53 100 O 46.72 1.610 L 1.00 0.0192 PT 8.76 (105) F=0 F 0.00 PE 0.00 BL2 0120 T 1.00 PF 0.02 1.610 L 7.50 0.0192 PT 8.78 (104) F=0 F 0.00 PE 0.00 BL2 C120 T 7.50 PF 0.14 1.610 L 93.50 0.0192 PT 8.92 (103) F=E F 4.00 PE 0.00 BL2 C120 T 97.50 PF 1.87 2.067 L 8.00 0.0057 PT 10.79 F=0 F 0.00 PE 0.00 CM3 C120 T 8.00 PF 0.05 PT 10.84 54) 53) 1.610 L 22.50 0.0776 PT 8.48 (100) F=T F 8.00 PE 0.00 BL2 C120 T 30.50 PF 2.37 40 53DQ 21.95 2.067 L 8.00 0.0469 PT 10.85 ( 53) Q 68.67 F=0 F 0.00 PE 0.00 CM3 C120 T 8.00 PF 0.38 PT 11.23 ( 40) 61 62 51 61 52 51 Q 23.45 Q 23.45 Q 23.45 2.067 L 8.00 0.0064 PT 8.49 ( 62) F=0 F 0.00 PE 0.00 CM4 C120 T 8.00 PF 0.05 1.610 L 107.00 0.0217 PT 8.54 ( 61) F=E/E F 8.00 PE 0.00 BL2 C120 T 115.00 PF 2.50 2.067 L 8.00 0.0064 PT 11.04 ( 51) F=0 F 0.00 PE 0.00 CM3 C120 T 8.00 PF 0.05 40 52D0 33.77 2.067 L 3.00 0.0335 PT 11.09 ( 52) Q 57.22 F=0 F 0.00 PE 0.00 CM3 C120 T 3.00 PF 0.10 PT 11.19 ( 40) 24 23 14 24 O 39.03 Q 39.03 2.067 L 8.00 0.0165 PT 14.63 ( 23) F=0 F 0.00 PE 0.00 CM2 C120 T 8.00 PF 0.13 1.610 L 129.00 0.0557 PT 14.76 ( 24) F=E/E F 8.00 PE 0.00 BL C120 T 137.00 PF 7.63 SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD TUKWILA, WA. 10-03-1991 PAGE 5 FROM TO FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 13 14 2.067 L 8.00 0.0165 PT 22.39 ( 14) Q 39.03 F=0 F 0.00 PE 0.00 CM1 C120 T 8.00 PF 0.13 12 13DQ 55.93 2.067 L 11.00 0.0854 PT 22.52 ( 13) Q 94.96 F=0 F 0.00 PE 0.00 CM1 0120 T 11.00 PF 0.94 PT 23.46 ( 12) 22 30 Q 80.93 2.067 L 7.50 0.0635 PT 14.55 ( 30) F=0 F 0.00 PE 0.00 CM2 C120 T 7.50 PF 0.48 12 22DQ -41.09 1.610 Q 39.84 L 129.00 0.0578 PT 15.03 ( 22) F=T/T F 16.00 PE 0.00 BL C120 T 145.00 PF 8.38 11 12DQ 94.96 2.635 L 8.00 0.0500 PT 23.41 ( 12) Q 134.80 F=0 F 0.00 PE 0.00 CM1 C120 T 8.00 PF 0.40 PT 23.81 ( 11) 21 22 11 21 Q 41.09 Q 41.09 6 7 5 4 5 3 4 2 3 Q 175.89 Q 175.89 Q 175.89 Q 175.89 Q 175.89 2.067 L 8.00 0.0181 PT 15.03 ( 22) F=0 F 0.00 PE 0.00 CM2 C120 T 8.00 PF 0.14 1.610 L 129.00 0.0612 PT 15.17 ( 21) F=T/E F 12.00 PE 0.00 BL C120 T 141.00 PF 8.63 PT 23.80 ( 11) 2.635 L 18.00 0.0819 PT 25.32 ( 7) F=T F 16.00 PE 7.79 FR C120 T 34.00 PF 2.78 2.635 L 6.50 0.0819 PT 35.89 ( 6) F=E F 8.00 PE 0.00 FR C120 T 14.50 PF 1.19 3.260 L 8.00 0.0290 PT 37.08 ( 5) F=T,E,GV/CV F 52.00 PE 2.71 FR C120 T 60.00 PF 1.74 4.124 L 1.50 0.0092 PT 41.53 ( 4) F=0 F 0.00 PE 0.65 FR C120 T 1.50 PF 0.01 4.155 L 35.00 0.0067 PT 42.19 F=T,EE,E F 53.00 PE 1.73 UN C140 T 88.00 PF 0.59 ( 3) SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD TUKWILA, WA. FROM TO 10-03-1991 PAGE 6 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 1 2 6.215 Q 175.89 0 1 Q 175.89 L 35.00 0.0009 PT 44.51 ( 2) F=GV,EE F 16.00 PE 0.00 UN C140 T 51.00 PF 0.05 8.325 L 14.00 0.0002 PT 44.56 ( 1) F=T , GV ,DDC F %11728.00 PE 0.00 UN C140 T %11742.00 PF 2.35 PRESSURE AVAILABLE AT NODE 0 AT 425.9 GPM - MAXIMUM PRESSURE UNBALANCE IN LOOPS 0.086 PSI MAXIMUM VELOCITY IN PIPES 10.35 FPS PT 46.91 ( 0) 140.2 PSI - J SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD TUKWILA, WA. BLDG NO. 2 3RD FLR UNIT A 7 SPKR. FLOWING FLOW TEST RESULTS STATIC RESIDUAL AT 3157.0 GPM PRESSURE AVAILABLE AT 551.8 GPM SUMMARY OF SPRINKLER OUTFLOWS ACTUAL MINIMUM SPR FLOW FLOW K -FACTOR PRESSURE 115 31.35 14.82 _, 216 30.50 18.72 117 30.10 14.82 220 29.12 29.12 121 25.87 14.82 122 24.92 22.08 118 29.94 14.82 l 5.60 5.60 5.60 5.60 5.60 5.60 5.60 TOTAL WATER REQUIRED FOR SYSTEM OUTFLOWS AT 100 OUTFLOWS AT 200 OUTSIDE HOSE STREAMS AT 0 TOTAL WATER REQUIREMENT PRESSURE REQUIRED AT 0 31.34 29.66 28.89 27.04 21.35 19.80 28.59 10-03-1991 PAGE 1 141.00 PSI 108.00 PSI 139.69 PSI 201.80 GPM 50.00 GPM 50.00 GPM 250.00 GPM 551.80 GPM 125.79 PSI MAXIMUM PRESSURE UNBALANCE IN LOOPS 0.100 PSI MAXIMUM VELOCITY IN PIPES 18.86 FPS SUBMITTAL SERIAL NO 2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD TUKWILA, WA. FROM TO 10-03-1991 PAGE 2 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 120 220 Q 29.12 116 216 Q 30.50 1.049 L 1.50 0.2608 PT 27.04 (220) F=T F 5.00 PE 0.00 AO C120 T 6.50 PF 1.70 PT 28.74 (120) 1.049 L 1.00 0.2841 PT 29.66 (216) F=T F 5.00 PE 0.00 AO C120 T 6.00 PF 1.70 PT 31.36 (116) 121 122 1.049 L 8.00 0.1955 PT 19.80 (122) Q 24.92 F=0 F 0.00 PE 0.00 BN C120 T 8.00 PF 1.56 118 121DQ 25.87 1.049 L 5.00 0.7298 PT 21.36 (121) Q 50.79 F=T F 5.00 PE 0.00 BN C120 T 10.00 PF 7.30 PT 28.66 (118) 30 40 2.635 Q 251.80 L 52.00 0.1590 PT 40.55 ( 40) F=T,6EE/T F 56.00 PE 0.00 NC C120 T 108.00 PF 17.17 PT 57.72 ( 30) 7 11 2.635 L 2.50 0.2223 PT 84.28 ( 11) Q 301.80 F=2E F 16.00 PE 0.00 NC C120 T 18.50 PF 4.11 PT 88.39 ( 7) 119 118 Q 14.21 1.610 L 1.00 0.0086 PT 28.59 (118) F=0 F 0.00 PE 0.00 BL4 C120 T 1.00 PF 0.01 120 119 1.610 L 8.00 0.0086 PT 28.60 (119) Q 14.21 F=0 F 0.00 PE 0.00 BL4 C120 T 8.00 PF 0.07 64 120DQ 29.12 1.610 L 71.00 0.0675 PT 28.67 (120) Q 43.33 F=0/E F 4.00 PE 0.00 BL4 C120 T 75.00 PF 5.06 63 64 Q 43.33 117 118 Q 66.53 2.067 L 8.00 0.0200 PT 33.73 ( 64) F=0 F 0.00 PE 0.00 CM4 C120 T 8.00 PF 0.16 PT 33.89 ( 63) 1.610 L 2.00 0.1493 PT 28.59 (118) F=0 F 0.00 PE 0.00 BL4 C120 T 2.00 PF 0.30 SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD TUKWILA, WA. FROM TO 10-03-1991 PAGE 3 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 54 117DQ 30.10 1.610 L 25.00 0.2977 PT 28.89 (117) Q 96.63 F=E F 4.00 PE 0.00 BL4 C120 T 29.00 PF 8.63 53 54 Q 96.63 2.067 L 8.00 0.0882 PT 37.52 ( 54) F=0 F 0.00 PE 0.00 CM3 C120 T 8.00 PF 0.71 PT 38.23 ( 53) 23 30 2.067 L 3.50 0.1094 PT 57.70 ( 30) Q 108.56 F=0 F 0.00 PE 0.00 CM2 C120 T 3.50 PF 0.38 200 23DQ -69.05 1.610 L 65.50 0.0569 PT 58.08 ( 23) Q 39.51 F=0/T F 8.00 PE 0.00 BL C120 T 73.50 PF 4.18 COMMENT: 50 GPM FOR INSIDE HOSE 13 200DQ 50.00 1.610 Q 89.51 115 116 Q 1.68 L 63.50 0.2585 PT 62.26 (200) F=T F 8.00 PE 0.00 BL C120 T 71.50 PF 18.48 PT 80.74 ( 13) 1.610 L 11.00 0.0002 PT 31.45 (116) F=0 F 0.00 PE 0.00 BL3 C120 T 11.00 PF 0.00 100 115DQ 31.35 1.610 L 3.00 0.0409 PT 31.45 (115) Q 33.03 F=0 F 0.00 PE 0.00 BL3 C120 T 3.00 PF 0.12 53 100DQ 50.00 1.610 Q 83.03 L 22.00 0.2249 PT 31.57 (100) F=T F 8.00 PE 0.00 BL3 C120 T 30.00 PF 6.75 40 53DQ 96.63 2.067 L 8.00 0.2777 PT 38.32 ( 53) Q 179.65 F=0 F 0.00 PE 0.00 CM3 C120 T 8.00 PF 2.22 PT 40.54 ( 40) 63 116 Q 28.82 1.610 L 71.50 0.0318 PT 31.45 (116) F=0/T F 8.00 PE 0.00 BL3 C120 T 79.50 PF 2.53 62 63DQ 43.33 2.067 Q 72.15 52 62DQ -36.41 1.610 Q 35.74 L 11.00 0.0514 PT 33.98 ( 63) F=0 F 0.00 PE 0.00 CM4 C120 T 11.00 PF 0.57 L 107.00 0.0473 PT 34.55 ( 62) F=T/T F 16.00 PE 0.00 BL2 C120 T 123.00 PF 5.82 PT 40.37 ( 52) SUBMITTAL SERIAL NO:2480HY1 • HOMEWOOD SUITES 6925 SOUTHCENTER BLVD ' TUKWILA, WA. 1 FROM TO 10-03-1991 PAGE 4 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 61 62 2.067 L 8.00 0.0145 PT 34.58 ( 62) Q 36.41 F=0 F 0.00 PE 0.00 CM4 C120 T 8.00 PF 0.12 51 61 1.610 L 107.00 0.0489 PT 34.70 ( 61) Q 36.41 F=E/E F 8.00 PE 0.00 BL2 C120 T 115.00 PF 5.62 52 51 2.067 L 8.00 0.0145 PT 40.32 ( 51) Q 36.41 F=0 F 0.00 PE 0.00 CM3 C120 T 8.00 PF 0.12 40 52DQ 35.74 2.067 L 3.00 0.0514 PT 40.44 ( 52) Q 72.15 F=0 F 0.00 PE 0.00 CM3 C120 T 3.00 PF 0.15 PT 40.59 ( 40) 24 23 2.067 L 8.00 0.0474 PT 58.09 ( 23) Q 69.05 F=0 F 0.00 PE 0.00 CM2 C120 T 8.00 PF 0.38 14 24 1.610 L 129.00 0.1599 PT 58.47 ( 24) Q 69.05 F=E/E F 8.00 PE 0.00 BL C120 T 137.00 PF 21.91 13 14 2.067 L 8.00 0.0474 PT 80.38 ( 14) Q 69.05 F=0 F 0.00 PE 0.00 CM1 C120 T 8.00 PF 0.38 12 13D0 89.51 2.067 L 11.00 0.2204 PT 80.76 ( 13) Q 158.56 F=0 F 0.00 PE 0.00 CM1 C120 T 11.00 PF 2.42 PT 83.18 ( 12) 22 30 2.067 L 7.50 0.1827 PT 57.70 ( 30) Q 143.24 F=0 F 0.00 PE 0.00 CM2 C120 T 7.50 PF 1.37 12 22D0 -72.67 1.610 L 129.00 0.1665 PT 59.07 ( 22) Q 70.57 F=T/T F 16.00 PE 0.00 BL C120 T 145.00 PF 24.14 11 12DQ 158.56 2.635 L 8.00 0.1335 PT 83.21 ( 12) Q 229.13 F=0 F 0.00 PE 0.00 CM1 C120 T 8.00 PF 1.07 PT 84.28 ( 11) 21 22 Q 72.67 2.067 L 8.00 0.0521 PT 59.07 ( 22) F=0 F 0.00 PE 0.00 CM2 C120 T 8.00 PF 0.42 SUBMITTAL SERIAL NO:2480HY1 HOMEW00D SUITES 6925 SOUTHCENTER BLVD TUKWILA, WA. FROM TO 11 21 10-03-1991 PAGE 5 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI Q 72.67 6 7 Q 301.80 5 6 2.635 L 6.50 0.2223 PT103 .74 ( 6) Q 301.80 F=E F 8.00 PE 0.00 FR C120 T 14.50 PF 3.22 1.610 L 129.00 0.1758 PT 59.49 ( 21) F=T/E F 12.00 PE 0.00 BL C120 T 141.00 PF 24.79 PT 84.28 ( 11) 2.635 L 18.00 0.2223 PT 88.39 ( 7) F=T F 16.00 PE 7.79 FR C120 T 34.00 PF 7.56 4 5 3.260 L 8.00 0.0788 PT106.96 ( 5) Q 301.80 F=T,E,GV/CV F 52.00 PE 2.71 FR C120 T 60.00 PF 4.73 3 4 4.124 L 1.50 0.0251 PT114.40 ( 4) Q 301.80 F=0 F 0.00 PE 0.65 FR C120 T 1.50 PF 0.04 2 3 Q 301.80 1 2 Q 301.80 0 1 Q 301.80 4.155 L 35.00 0.0182 PT115.09 F=T,EE,E F 53.00 PE 1.73 UN C140 T 88.00 PF 1.60 ( 3) 6.215 L 35.00 0.0026 PT118.42 ( 2) F=GV,EE F 16.00 PE 0.00 UN C140 T 51.00 PF 0.13 8 325 L 14.00 0.0006 PT118.55 ( 1) F=T,GV,DDC F %11728.00 PE 0.00 UN C140 T %11742.00 PF 7.05 PRESSURE AVAILABLE AT NODE 0 AT 551.8 GPM MAXIMUM PRESSURE UNBALANCE IN LOOPS 0.100 PSI MAXIMUM VELOCITY IN PIPES 18.86 FPS PT125.60 ( 0) 139.7 PSI SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD TUKWILA, WA. BLDG NO. 2 3RD FLR REMOTE ROOM WITH GREATEST DEMAND 6 SPRINKLERS FLOWING FLOW TEST RESULTS STATIC RESIDUAL AT 3157.0 GPM PRESSURE AVAILABLE AT 535.7 GPM SUMMARY OF SPRINKLER OUTFLOWS ACTUAL MINIMUM SPR FLOW FLOW K -FACTOR PRESSURE 201 31.06 18.72 102 31.93 14.82 203 30.52 29.12 104 31.34 14.82 205 29.44 29.44 106 31.38 14.82 5.60 5.60 5.60 5.60 5.60 5.60 TOTAL WATER REQUIRED FOR SYSTEM OUTFLOWS AT 100 OUTFLOWS AT 200 OUTSIDE HOSE STREAMS AT 0 TOTAL WATER REQUIREMENT PRESSURE REQUIRED AT 0 MAXIMUM PRESSURE UNBALANCE IN LOOPS MAXIMUM VELOCITY IN PIPES 30.77 32.51 29.70 31.33 27.64 31.41 10-03-1991 PAGE 1 141.00 PSI 108.00 PSI 139.76 PSI 185.68 GPM 50.00 GPM 50.00 GPM 250.00 GPM 535.68 GPM 121.71 PSI 0.046 PSI 16.81 FPS . .1 • SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD TUKWILA, WA. FROM TO 10-03-1991 PAGE 2 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 105 205 Q 29.44 103 203 Q 30.52 101 201 Q 31.06 1.049 L 9.00 0.2661 PT 27.64 (205) F=T F 5.00 PE 0.00 AO C120 T 14.00 PF 3.73 PT 31.37 (105) 1.049 L 1.50 0.2844 PT 29.70 (203) F=T F 5.00 PE 0.00 AO C120 T 6.50 PF 1.85 PT 31.55 (103) 1.049 L 1.00 0.2938 PT 30.77 (201) F=T F 5.00 PE 0.00 AO C120 T 6.00 PF 1.76 PT 32.53 (101) 30 40 2.635 Q 235.68 L 52.00 0.1407 PT 43.87 ( 40) F=T,6EE/T F 56.00 PE 0.00 NC C120 T 108.00 PF 15.20 PT 59.07 ( 30) 7 11 2.635 L 2.50 0.2008 PT 83.00 ( 11) Q 285.68 F=2E F 16.00 PE 0.00 NC C120 T 18.50 PF 3.71 PT 86.71 ( 7) 23 30 2.067 L 3.50 0.0949 PT 59.11 ( 30) Q 100.52 F=0 F 0.00 PE 0.00 CM2 C120 T 3.50 PF 0.33 200 23DQ -65.17 1.610 L 65.50 0.0463 PT 59.44 ( 23) Q 35.34 F=0/T F 8.00 PE 0.00 BL C120 T 73.50 PF 3.40 COMMENT: 50 GPM FOR INSIDE HOSE 13 200DQ 50.00 1.610 Q 85.34 L 63.50 0.2366 PT 62.84 (200) F=T F 8.00 PE 0.00 BL C120 T 71.50 PF 16.92 PT 79.76 ( 13) 105 104 1.610 L 1.00 0.0015 PT 31.33 (104) Q 5.44 F=0 F 0.00 PE 0.00 BL2 C120 T 1.00 PF 0.00 106 105DQ 29.44 1.610 L 1.75 0.0452 PT 31.33 (105) Q 34.88 F=0 F 0.00 PE 0.00 BL2 C120 T 1.75 PF 0.08 64 106DQ 31.38 1.610 L 3.25 0.1482 PT 31.41 (106) Q 66.26 F=0/E F 4.00 PE 0.00 BL2 0120 T 7.25 PF 1.07 SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD TUKWILA, WA. FROM TO 10-03-1991 PAGE 3 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 63 64 2.067 L 8.00 0.0439 PT 32.48 ( 64) Q 66.26 F=0 F 0.00 PE 0.00 CM4 C120 T 8.00 PF 0.35 112 63DQ 29.33 2.067 L 5.50 0.0864 PT 32.83 ( 63) Q 95.59 F=0 F 0.00 PE 0.00 CM4 C120 T 5.50 PF 0.48 62 112 Q 95.59 2.067 L 5.50 0.0864 PT 33.31 (112) F=0 F 0.00 PE 0.00 CM4 C120 T 5.50 PF 0.48 111 62D0 -48.15 1.610 O 47.44 110 111 Q 47.44 Q 47.44 109 110 1.610 1 .610 L 12.50 0.0799 PT 33.79 ( 62) F=0/T F 8.00 PE 0.00 BL2 C120 T 20.50 PF 1.64 L 8.50 0.0799 PT 35.43 (111) F=0 F 0.00 PE 0.00 BL2 C120 T 8.50 PF 0.68 L 9.50 0.0799 PT 36.11 (110) F=0 F 0.00 PE 0.00 BL2 C120 T 9.50 PF 0.76 108 109 1.610 L 14.00 0.0799 PT 36.87 (109) Q 47.44 F=0 F 0.00 PE 0.00 BL2 C120 T 14.00 PF 1.12 52 108 Q 47.44 1.610 L 62.50 0.0799 PT 37.99 (108) F=T F 8.00 PE 0.00 BL2 C120 T 70.50 PF 5.63 PT 43.62 ( 52) 103 104 1.610 O 25.91 54 10300 30.52 1.610 Q 56.43 53 54 Q 56.43 63 102 Q 29.33 2.067 L 7.50 0.0261 PT 31.33 (104) F=0 F 0.00 PE 0.00 BL2 C120 T 7.50 PF 0.20 L 93.50 0.1101 PT 31.53 (103) F=E F 4.00 PE 0.00 BL2 C120 T 97.50 PF 10.73 L 8.00 0.0326 PT 42.26 ( 54) F=0 F 0.00 PE 0.00 CM3 C120 T 8.00 PF 0.26 PT 42.52 ( 53) 1.610 L 2.50 0.0328 PT 32.51 (102) F=0/T F 8.00 PE 0.00 BL2 C120 T 10.50 PF 0.34 PT 32.85 ( 63) SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES ' 6925 SOUTHCENTER BLVD TUKWILA, WA. .a FROM TO 10-03-1991 PAGE 4 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 101 102 1.610 L 10.50 0.0004 PT 32.51 (102) Q 2.60 F=0 F 0.00 PE 0.00 BL2 C120 T 10.50 PF 0.00 100 101DQ 31.06 1.610 L 71.50 0.0423 PT 32.51 (101) Q 33.66 F=0 F 0.00 PE 0.00 BL2 C120 T 71.50 PF 3.02 COMMENT: 50 GPM FOR INSIDE HOSE 53 100DQ Q 50.00 83.66 1.610 L 22.50 0.2281 PT 35.53 (100) F=T F 8.00 PE 0.00 BL2 C120 T 30.50 PF 6.96 40 53DQ 56.43 2.067 L 8.00 0.1753 PT 42.49 ( 53) Q 140.08 F=0 F 0.00 PE 0.00 CM3 C120 T 8.00 PF 1.40 PT 43.89 ( 40) 61 62 51 61 Q 48.15 Q 48.15 2.067 L 8.00 0.0243 PT 33.79 ( 62) F=0 F 0.00 PE 0.00 CM4 C120 T 8.00 PF 0.19 1.610 L 107.00 0.0821 PT 33.98 ( 61) F=E/E F 8.00 PE 0.00 BL2 C120 T 115.00 PF 9.44 52 51 2.067 L 8.00 0.0243 PT 43.42 ( 51) Q 48.15 F=0 F 0.00 PE 0.00 CM3 C120 T 8.00 PF 0.19 40 52DQ 47.44 Q 95.59 24 23 2.067 L 3.00 0.0864 PT 43.61 ( 52) F=0 F 0.00 PE 0.00 CM3 C120 T 3.00 PF 0.26 PT 43.87 ( 40) 2.067 Q 65.17 14 24 Q 65.17 Q 65.17 12 13DQ 85.34 2.067 Q 150.52 1.610 13 14 2.067 L 8.00 0.0426 PT 59.44 ( 23) F=0 F 0.00 PE 0.00 CM2 C120 T 8.00 PF 0.34 L 129.00 0.1437 PT 59.78 ( 24) F=E/E F 8.00 PE 0.00 BL C120 T 137.00 PF 19.69 L 8.00 0.0426 PT 79.47 ( 14) F=0 F 0.00 PE 0.00 CM1 C120 T 8.00 PF 0.34 L 11.00 0.2002 PT 79.81 ( 13) F=0 F 0.00 PE 0.00 CM1 C120 T 11.00 PF 2.20 PT 82.01 ( 12) SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD TUKWILA, WA. • FROM TO 10-03-1991 PAGE 5 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 22 30 2.067 L 7.50 0.1641 PT 59.11 ( 30) Q 135.16 F=0 F 0.00 PE 0.00 CM2 C120 T 7.50 PF 1.23 12 22DQ -68.62 1.610 Q 66.55 L 129.00 0.1493 PT 60.34 ( 22) F=T/T F 16.00 PE 0.00 BL C120 T 145.00 PF 21.65 11 12DQ 150.52 2.635 L 8.00 0.1208 PT 81.99 ( 12) Q 217.06 F=0 F 0.00 PE 0.00 CM1 C120 T 8.00 PF 0.97 PT 82.96 ( 11) 21 22 Q 68.62 2.067 11 21 1.610 Q 68.62 6 7 2.635 Q 285.68 5 6 2.635 Q 285.68 4 5 Q 285.68 3 4 Q 285.68 2 3 Q 285.68 1 2 Q 285.68 0 1 Q 285.68 L 8.00 0.0468 PT 60.34.( 22) F=0 F 0.00 PE 0.00 CM2 C120 T 8.00 PF 0.37 L 129.00 0.1581 PT 60.71 ( 21) F=T/E F 12.00 PE 0.00 BL C120 T 141.00 PF 22.29 PT 83.00 ( 11) L 18.00 0.2008 PT 86.68 ( 7) F=T F 16.00 PE 7.79 FR C120 T 34.00 PF 6.83 L 6.50 0.2008 PT101.30 ( 6) F=E F 8.00 PE 0.00 FR C120 T 14.50 PF 2.91 3.260 L 8.00 0.0712 PT104.21 ( 5) F=T,E,GV/CV F 52.00 PE 2.71 FR C120 T 60.00 PF 4.27 4.124 L 1.50 0.0227 PT 111 .19 ( 4) F=0 F 0.00 PE 0.65 FR C120 T 1.50 PF 0.03 4.155 L F=T,EE,E F UN C140 T 35.00 0.0164 PT111.87 53.00 PE 1.73 88.00 PF 1.44 ( 3) 6.215 L 35.00 0.0023 PT 115 .04 ( 2) F=GV,EE F 16.00 PE 0.00 UN C140 T 51.00 PF 0.12 8.325 L 14.00 0.0006 PT115.16 ( 1) F=T,GV,DDC F %11728.00 PE 0.00 UN C140 T %11742.00 PF 7.05 PT122.21 ( 0) • SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD • TUKWILA, WA. BLDG NO. 2 2ND FLR STAFF BREAK RM. ALL SPRINKLERS FLOWING FLOW TEST RESULTS STATIC RESIDUAL AT 3157.0 GPM PRESSURE AVAILABLE AT 571.9 GPM SUMMARY OF SPRINKLER OUTFLOWS ACTUAL MINIMUM SPR FLOW FLOW K -FACTOR PRESSURE 71 31.09 14.82 73 27.12 21.12 74 25.11 21.12 75 22.36 21.12 76 21.12 21.12 179 32.94 14.82 180 31.80 21.12 181 30.34 21.12 5.60 5.60 5.60 5.60 5.60 5.60 5.60 5.60 TOTAL WATER REQUIRED FOR SYSTEM OUTFLOWS AT 32 OUTFLOWS AT 200 OUTSIDE HOSE STREAMS AT 0 TOTAL WATER REQUIREMENT PRESSURE REQUIRED AT 0 30.83 23.45 20.11 15.94 14.22 34.60 32.25 29.35 10-02-1991 PAGE 1 141.00 PSI 108.00 PSI 139.60 PSI 221.88 GPM 50.00 GPM 50.00 GPM 250.00 GPM 571.88 GPM 122.97 PSI MAXIMUM PRESSURE UNBALANCE IN LOOPS 0.079 PSI MAXIMUM VELOCITY IN PIPES 20.40 FPS SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD TUKWILA, WA. FROM TO 10-02-1991 PAGE 2 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 75 76 1.049 L 12.00 0.1439 PT 14.22 ( 76) Q 21.12 F=0 F 0.00 PE 0.00 BN C120 T 12.00 PF 1.73 72 75D0 22.36 1.049 L 15.00 0.5473 PT 15.95 ( 75) Q 43.48 F=5E F 10.00 PE 0.00 BN C120 T 25.00 PF 13.68 PT 29.63 ( 72) 81 181 1.049 L 1.00 0.2813 PT 29.35 (181) Q 30.34 F=T F 5.00 PE 0.00 AO C120 T 6.00 PF 1.69 80 81 1.049 L 11.00 0.2813 PT 31.04 ( 81) Q 30.34 F=0 F 0.00 PE 0.00 BN2 C120 T 11.00 PF 3.09 PT 34.13 ( 80) 80 180 1.049 L 1.00 0.3069 PT 32.25 (180) Q 31.80 F=T F 5.00 PE 0.00 AO C120 T 6.00 PF 1.84 79 80D0 30.34 1.380 L 9.00 0.2788 PT 34.09 ( 80) Q 62.14 F=0 F 0.00 PE 0.00 BN2 C120 T 9.00 PF 2.51 PT 36.60 ( 79) 79 179 1.049 L 1.00 0.3275 PT 34.60 (179) Q 32.94 F=T F 5.00 PE 0.00 AO C120 T 6.00 PF 1.96 78 79D0 62.14 1.380 L 10.50 0.6123 PT 36.56 ( 79) Q 95.08 F=0 F 0.00 PE 0.00 BN2 C120 T 10.50 PF 6.43 32 78 1.610 L 2.00 0.2890 PT 42.99 ( 78) Q 95.08 F=T F 8.00 PE 0.00 BN2 C120 T 10.00 PF 2.89 31 32DQ 50.00 2.635 L 24.00 0.0573 PT 45.88 ( 32) Q 145.08 F=0 F 0.00 PE 0.00 NC C120 T 24.00 PF 1.38 COMMENT: 50 GPM FOR INSIDE HOSE 73 74 Q 25.11 PT 47.26 ( 31) 1.049 L 12.00 0.1983 PT 20.11 ( 74) F=T F 5.00 PE 0.00 BN C120 T 17.00 PF 3.37 SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD TUKWILA, WA. FROM TO 10-02-1991 PAGE 3 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 72 7300 27.12 1.049 L 3.00 0.7685 PT 23.48 ( 73) Q 52.23 F=T F 5.00 PE 0.00 BN C120 T 8.00 PF 6.15 70 72DQ 43.48 1.610 Q 95.71 70 71 Q 31.09 L 11.00 0.2925 PT 29.63 ( 72) F=0 F 0.00 PE 0.00 BN C120 T 11.00 PF 3.22 PT 32.85 ( 70) 1.049 L 1.50 0.2944 PT 30.83 ( 71) F=T F 5.00 PE 0.00 BN C120 T 6.50 PF 1.91 31 70DQ 95.71 1.610 O 126.80 30 31D0 145.08 2.635 Q 271.88 7 11 2.635 Q 321.88 L 13.50 0.4922 PT 32.74 ( 70) F=T,2E F 16.00 PE 0.00 BN C120 T 29.50 PF 14.52 L 14.00 0.1833 PT 47.26 ( 31) F=T,3EE F 28.00 PE 0.00 NC C120 T 42.00 PF 7.70 PT 54.96 ( 30) L 2.50 0.2504 PT 85.15 ( 11) F=2E F 16.00 PE 0.00 NC 0120 T 18.50 PF 4.63 PT 89.78 ( 7) 23 30 2.067 L 3.50 0.1289 PT 55.04 ( 30) O 118.63 F=0 F 0.00 PE 0.00 CM2 C120 T 3.50 PF 0.45 200 23DQ -74.01 1.610 L 65.50 0.0713 PT 55.49 ( 23) Q 44.62 F=0/T F 8.00 PE 0.00 BL C120 T 73.50 PF 5.24 COMMENT: 50 GPM FOR INSIDE HOSE 13 200D0 50.00 1.610 O 94.62 24 23 14 24 13 14 Q 74.01 Q 74.01 O 74.01 2.067 L 63.50 0.2864 PT 60.73 (200) F=T F 8.00 PE 0.00 BL C120 T 71.50 PF 20.48 PT 81.21 ( 13) L 8.00 0.0538 PT 55.49 ( 23) F=0 F 0.00 PE 0.00 CM2 C120 T 8.00 PF 0.43 1.610 L 129.00 0.1818 PT 55.92 ( 24) F=E/E F 8.00 PE 0.00 BL C120 T 137.00 PF 24.91 2.067 L 8.00 0.0538 PT 80.83 ( 14) F=0 F 0.00 PE 0.00 CM1 C120 T 8.00 PF 0.43 SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD ' TUKWILA, WA. FROM TO 10-02-1991 PAGE 4 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 12 13DQ 94.62 2.067 Q 168.63 L 11.00 0.2470 PT 81.26 ( 13) F=0 F 0.00 PE 0.00 CM1 C120 T 11.00 PF 2.72 PT 83.98 ( 12) 22 30 2.067 L 7.50 0.2070 PT 55.04 ( 30) Q 153.25 F=0 F 0.00 PE 0.00 CM2 C120 T 7.50 PF 1.55 12 22DQ -77.74 1.610 Q 75.51 L 129.00 0.1887 PT 56.59 ( 22) F=T/T F 16.00 PE 0.00 BL C120 T 145.00 PF 27.36 11 12DQ 168.63 2.635 L 8.00 0.1502 PT 83.95 ( 12) Q 244.14 F=0 F 0.00 PE. 0.00 CM1 C120 T 8.00 PF 1.20 PT 85.15 ( 11) 21 22 11 21 Q 77.74 Q 77.74 2.067 L 8.00 0.0590 PT 56.59 ( 22) F=0 F 0.00 PE 0.00 CM2 0120 T 8.00 PF 0.47 1.610 L 129.00 0.1991 PT 57.06 ( 21) F=T/E F 12.00 PE 0.00 BL C120 T 141.00 PF 28.07 PT 85.13 ( 11) 6 7 2.635 L 9.00 0.2504 PT 89.77 ( 7) Q 321.88 F=T F 16.00 PE 3.90 FR C120 T 25.00 PF 6.26 5 6 2.635 L 6.50 0.2504 PT 99.93 ( 6) Q 321.88 F=E F 8.00 PE 0.00 FR C120 T 14.50 PF 3.63 4 5 3.260 L 8.00 0.0888 PT103.56 ( 5) Q 321.88 F=T , E , GV/CV F 52.00 PE 2.71 FR C120 T 60.00 PF 5.33 3 4 4.124 L 1.50 0.0283 PT111.60 ( 4) Q 321.88 F=0 F 0.00 PE 0.65 FR C120 T 1.50 PF 0.04 2 3 4.155 L 35.00 0.0205 PT112.29 ( 3) Q 321.88 F=T,EE,E F 53.00 PE 1.73 UN C140 T 88.00 PF 1.80 1 2 6.215 L 35.00 0.0029 PT115.82 ( 2) Q 321.88 F=GV,EE F 16.00 PE 0.00 UN C140 T 51.00 PF 0.15 SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD TUKWILA, WA. FROM TO 0 1 10-02-1991 PAGE 5 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI Q 321.88 8.325 L 14.00 0.0007 PT115.97 ( 1) F=T,GV,DDC F %10061.00 PE 0.00 UN C140 T %10075.00 PF 7.05 PRESSURE AVAILABLE AT NODE 0 AT 571.9 GPM MAXIMUM PRESSURE UNBALANCE IN LOOPS 0.079 PSI MAXIMUM VELOCITY IN PIPES 20.40 FPS PT123.02 ( 0 139.6 PSI ) SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD TUKWILA, WA. BLDG NO. 2 1ST FLR REMOTE ROOM WITH GREATEST DEMAND ALL SPRINKLERS FLOWING FLOW TEST RESULTS STATIC RESIDUAL AT 3157.0 GPM PRESSURE AVAILABLE AT 538.1 GPM SUMMARY OF SPRINKLER OUTFLOWS ACTUAL MINIMUM SPR FLOW FLOW K -FACTOR PRESSURE 201 32.18 18.72 102 33.05 14.82 203 30.69 29.12 104 31.33 14.82 205 29.44 29.44 106 31.39 14.82 5.60 5.60 5.60 5.60 5.60 5.60 TOTAL WATER REQUIRED FOR SYSTEM OUTFLOWS AT 100 OUTFLOWS AT 200 OUTSIDE HOSE STREAMS AT 0 TOTAL WATER REQUIREMENT PRESSURE REQUIRED AT 0 MAXIMUM PRESSURE UNBALANCE IN LOOPS MAXIMUM VELOCITY IN PIPES 33.02 34.83 30.03 31 .29 27.64 31.42 10-03-1991 PAGE 1 141.00 PSI 108.00 PSI 139.75 PSI 188.07 GPM 50.00 GPM 50.00 GPM 250.00 GPM 538.07 GPM 122.22 PSI 0.071 PSI 19.09 FPS • SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD TUKWILA, WA. FROM TO 10-03-1991 PAGE 2 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI ' 105 205 1.049 L 9.00 0.2661 PT 27.64 (205) Q 29.44 F=T F 5.00 PE 0.00 AO C120 T 14.00 PF 3.73 PT 31.37 (105) a -i 103 203 1.049 L 1.50 0.2873 PT 30.03 (203) Q 30.69 F=T F 5.00 PE 0.00 AO C120 T 6.50 PF 1.87 PT 31.90 (103) 101 201 1.049 L 1.00 0.3137 PT 33.02 (201) Q 32.18 F=T F 5.00 PE 0.00 AO C120 T 6.00 PF 1.88 PT 34.90 (101) 30 40 2.635 L 52.00 0.1433 PT 59.69 ( 40) Q 238.07 F=T,6EE/T F 56.00 PE 0.00 NC C120 T 108.00 PF 15.48 PT 75.17 ( 30) 6 11 2.635 L 2.50 0.2040 PT 99.39 ( 11) Q 288.07 F=E F 8.00 PE 0.00 NC C120 T 10.50 PF 2.14 PT101.53 ( 6) 23 30 2.067 L 3.50 0.0971 PT 75.16 ( 30) Q 101.76 F=0 F 0.00 PE 0.00 CM2 C120 T 3.50 PF 0.34 200 2300 -65.75 1.610 L 65.50 0.0480 PT 75.50 ( 23) Q 36.01 F=0/T F 8.00 PE 0.00 BL C120 T 73.50 PF 3.53 COMMENT: 50 GPM FOR INSIDE HOSE 13 200D0 50.00 1.610 L 63.50 0.2401 PT 79.03 (200) Q 86.01 F=T F 8.00 PE 0.00 BL C120 T 71.50 PF 17.17 PT 96.20 ( 13) 105 104 1.380 L 1.00 0.0001 PT 31.29 (104) Q 1.05 F=0 F 0.00 PE 0.00 BL2 C120 T 1.00 PF 0.00 106 10500 29.44 1.380 L 1.75 0.0747 PT 31.29 (105) Q 30.49 F=0 F 0.00 PE 0.00 BL2 0120 T 1.75 PF 0.13 64 10600 31.39 1.380 L 3.25 0.2766 PT 31.42 (106) Q 61.88 F=0/E F 3.00 PE 0.00 BL2 C120 T 6.25 PF 1.73 • l . SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD TUKWILA, WA. FROM TO 10-03-1991 PAGE 3 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 63 64 1.380 L 8.00 0.2766 PT 33.15 ( 64) Q 61.88 F=0 F 0.00 PE 0.00 CM4 C120 T 8.00 PF 2.21 112 630Q 27.11 1.380 L. 5.50 0.5417 PT 35.36 ( 63) Q 88.99 F=0 F 0.00 PE 0.00 CM4 C120 T 5.50 PF 2.98 62 112 1.380 L 5.50 0.5417 PT 38.34 (112) Q 88.99 F=0 F 0.00 PE 0.00 CM4 C120 T 5.50 PF 2.98 111 620Q -44.22 1.380 Q 44.77 110 111 109 110 108 109 52 108 Q 44.77 Q 44.77 Q 44.77 Q 44.77 L 12.50 0.1520 PT 41.32 ( 62) F=0/T F 6.00 PE 0.00 BL2 C120 T 18.50 PF 2.81 1.380 L 8.50 0.1520 PT 44.13 (111) F=0 F 0.00 PE 0.00 BL2 C120 T 8.50 PF 1.29 1.380 L 9.50 0.1520 PT 45.42 (110) F=0 F 0.00 PE 0.00 BL2 C120 T 9.50 PF 1.44 1.380 L 14.00 0.1520 PT 46.86 (109) F=0 F 0.00 PE 0.00 BL2 C120 T 14.00 PF 2.13 1.380 L 62.50 0.1520 PT 48.99 (108) F=T F 6.00 PE 0.00 BL2 C120 T 68.50 PF 10.41 PT 59.40 ( 52) 103 104 1.380 L 7.50 0.0737 PT 31.29 (104) Q 30.27 F=0 F 0.00 PE 0.00 BL2 C120 T 7.50 PF 0.55 54 1030Q 30.69 Q 60.96 53 54 Q 60.96 63 102 Q 27.11 1.380 L 93.50 0.2690 PT 31.84 (103) F=E F 3.00 PE 0.00 BL2 C120 T 96.50 PF 25.96 2.067 L 8.00 0.0376 PT 57.80 ( 54) F=0 F 0.00 PE 0.00 CM3 C120 T 8.00 PF 0.30 PT 58.10 ( 53) 1.380 L 2.50 0.0601 PT 34.83 (102) F=0/T F 6.00 PE 0.00 BL2 C120 T 8.50 PF 0.51 PT 35.34 ( 63) SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD TUKWILA , WA. FROM TO 10-03-1991 PAGE 4 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI Q 101 102 5.94 1.380 L 10.50 0.0036 PT 34.83 (102) F=0 F 0.00 PE 0.00 BL2 C120 T 10.50 PF 0.04 100 101DQ 32.18 1.380 L 71.50 0.1129 PT 34.87 (101) Q 38.12 F=0 F 0.00 PE 0.00 BL2 C120 T 71.50 PF 8.07 COMMENT: 50 GPM FOR INSIDE HOSE 53 100D0 50.00 1.380 L 22.50 0.5319 PT 42.94 (100) Q 88.12 F=T F 6.00 PE 0.00 BL2 C120 T 28.50 PF 15.16 40 53DQ 60.96 2.067 L 8.00 0.1967 PT 58.10 ( 53) Q 149.08 F=0 F 0.00 PE 0.00 CM3 C120 T 8.00 PF 1.57 PT 59.67 ( 40) 61 62 1.380 L 8.00 0.1485 PT 41.37 ( 62) Q 44.22 F=0 F 0.00 PE 0.00 CM4 C120 T 8.00 PF 1.19 51 61 1.380 L 107.00 0.1485 PT 42.56 ( 61) Q 44.22 F=E/E F 6.00 PE 0.00 BL2 C120 T 113.00 PF 16.78 52 51 2.067 L 8.00 0.0208 PT 59.34 ( 51) Q 44.22 F=0 F 0.00 PE 0.00 CM3 C120 T 8.00 PF 0.17 40 52DQ 44.77 2.067 L 3.00 0.0757 PT 59.51 ( 52) Q 88.99 F=0 F 0.00 PE 0.00 CM3 C120 T 3.00 PF 0.23 PT 59.74 ( 40) 24 23 2.067 L 8.00 0.0433 PT 75.50 ( 23) Q 65.75 F=0 F 0.00 PE 0.00 CM2 C120 T 8.00 PF 0.35 14 24 1.610 L 129.00 0.1461 PT 75.85 ( 24) Q 65.75 F=E/E F 8.00 PE 0.00 BL C120 T 137.00 PF 20.02 13 14 2.067 L 8.00 0.0433 PT 95.87 ( 14) Q 65.75 F=0 F 0.00 PE 0.00 CM1 C120 T 8.00 PF 0.35 12 13DQ 86.01 2.067 L 11.00 0.2033 PT 96.22 ( 13) Q 151.76 F=0 F 0.00 PE 0.00 CM1 C120 T 11.00 PF 2.24 PT 98.46 ( 12) SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD TUKWILA, WA. ' FROM TO 10-03-1991 PAGE 5 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 22 30 2.067 L 7.50 0.1667 PT 75.16 ( 30) Q 136.31 F=0 F 0.00 PE 0.00 CM2 C120 T 7.50 PF 1.25 12 22DQ -69.13 1.610 L 129.00 0.1520 PT 76.41 ( 22) Q 67.18 F=T/T F 16.00 PE 0.00 BL C120 T 145.00 PF 22.04 11 12DQ 151.76 2.635 L 8.00 0.1228 PT 98.45 ( 12) Q 218.94 F=0 F 0.00 PE 0.00 CM1 C120 T 8.00 PF 0.98 PT 99.43 ( 11) • 21 22 11 21 Q 69.13 Q 69.13 2.067 L 8.00 0.0475 PT 76.41 ( 22) F=0 F 0.00 PE 0.00 CM2 C120 T 8.00 PF 0.38 1.610 L 129.00 0.1603 PT 76.79 ( 21) F=T/E F 12.00 PE 0.00 BL C120 T 141.00 PF 22.60 PT 99.39 ( 11) 5 6 2.635 L 6.50 0.2040 PT101.57 ( 6) Q 288.07 F=E F 8.00 PE 0.00 FR C120 T 14.50 PF 2.96 4 5 3.260 L. 8.00 0.0723 PT104 .53 ( 5) Q 288.07 F=T,E,GV/CV F 52.00 PE 2.71 FR C120 T 60.00 PF 4.34 3 4 4.124 L 1.50 0.0230 PT111.58 ( 4) Q 288.07 F=0 F 0.00 PE 0.65 FR C120 T 1.50 PF 0.03 2 3 4.155 L 35.00 0.0167 PT112.26 ( 3) Q 288.07 F=T,EE,E F 53.00 PE 1.73 UN C140 T 88.00 PF 1.47 1 2 6.215 L 35.00 0.0023 PT115.46 ( Q 288.07 F=GV,EE F 16.00 PE 0.00 UN C140 T 51.00 PF 0.12 0 1 8 325 L 14.00 0.0006 PT115.58 ( 1) Q 288.07 F=T,GV,DDC F %11728.00 PE 0.00 UN C140 T %11742.00 PF 7.05 • J PT122.63 ( 0) PRESSURE AVAILABLE AT NODE 0 AT 538.1 GPM MAXIMUM PRESSURE UNBALANCE IN LOOPS 0.071 PSI MAXIMUM VELOCITY IN PIPES 19.09 FPS 139.7 PSI TUKWILA, WA. - BLDG NO. 2 ATTIC DRY SYSTEM DESIGN DENSITY .16/1950 FLOW TEST RESULTS STATIC RESIDUAL AT 3157.0 GPM PRESSURE AVAILABLE AT 766.2 GPM SUMMARY OF SPRINKLER OUTFLOWS ACTUAL MINIMUM SPR FLOW FLOW K -FACTOR PRESSURE ___ ____ ---- 101 32.17 16.00 5.60 33.00 103 31.18 16.00 5.60 31.00 104 25.73 16.00 5.60 21.10 106 21.84 16.00 5.60 15.21 208 19.23 16.00 5.60 11.79 109 32.21 16.00 5.60 33.08 ',111 28.30 16.00 5.60 25.54 112 26.54 16.00 5.60 22.47 113 32.40 16.00 5.60 33.47 115 31.30 16.00 5.60 31.25 116 32.07 16.00 5.60 32.80 118 31.08 16.00 5.60 30.81 119 25.65 16.00 5.60 20.98 121 21.78 16.00 5.60 15.13 223 19.17 16.00 5.60 11.72 226 16.19 16.00 5.60 8.35 . 227 16.16 16.00 5.60 8.32 124 20.56 16.00 5.60 13.47 125 20.50 16.00 5.60 13.40 .'128 16.00 16.00 5.60 8.16 129 16.13 16.00 5.60 8.30 _TOTAL WATER REQUIRED FOR SYSTEM OUTSIDE HOSE STREAMS AT 0 ..TOTAL WATER REQUIREMENT PRESSURE REQUIRED AT 0 141.00 PSI 108.00 PSI 138.60 PSI 516.18 GPM 250.00 GPM 766.18 GPM 115.13 PSI , MAXIMUM PRESSURE UNBALANCE IN LOOPS 0.041 PSI MAXIMUM VELOCITY IN PIPES 20.36 FPS .TUKWILA, WA. ''FROM TO `' FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 127 128 O 16.00 '^ 117 116 1.049 L 9.00 F=E F 1.00 BN4 C100 T 10.00 0.1207 PT 8.16 (128) PE 0.00 PF 1.21 PT 9.37 (127) 2.067 L 8.50 0.0161 PT 32.80 (116) O 32.07 F=0/T F 7.00 PE 0.00 BN4 C100 T 15.50 PF 0.25 24 117DQ 150.34 2.067 L 2.00 0.4003 PT 33.05 (117) O 182.41 F=T F 7.00 PE 0.87 NR C100 T 9.00 PF 3.60 3 24 O 182.41 114 113 3.260 L 11.00 0.0435 PT 37.52 ( 24) F=0 F 0.00 PE 0.00 NC C100 T 11.00 PF 0.48 PT 38.00 ( 23) 1.610 L 6.50 0.0552 PT 33.47 (113) O 32.40 F=0/T F 6.00 PE 0.00 BN3 C100 T 12.50 PF 0.69 23 114D0 31.30 2.067 L 7.00 0.0572 PT 34.16 (114) O 63.70 F=T F 7.00 PE 3.03 NR C100 T 14.00 PF 0.80 20 23D0 182.41 3.260 L 8.00 0.0757 PT 37.99 ( 23) O 246.11 F=T F 14.00 PE 0.00 NC C100 T 22.00 PF 1.67 PT 39.66 ( 20) 102 101 2.067 L 8.50 0.0161 PT 33.00 (101) '' O 32.17 F=0/T F 7.00 PE 0.00 BN C100 T 15.50 PF 0.25 22 21 102D0 150.85 O 183.02 22 O 183.02 2.067 3.260 L 2.00 0.4028 PT 33.25 (102) F=T F 7.00 PE 0.87 NR 0100 T 9.00 PF 3.63 L 11.00 0.0438 PT 37.75 ( 22) F=0 F 0.00 PE 0.00 NC C100 T 11.00 PF 0.48 PT 38.23 ( 21) 110 109 1.610 L 6.50 0.0547 PT 33.08 (109) O 32.21 F=0/T F 6.00 PE 0.00 BN2 C100 T 12.50 PF 0.68 21 110D0 54.84 2.067 L 7.00 0.1019 PT 33.76 (110) O 87.05 F=T F 7.00 PE 3.03 ' TUKWILA, WA. ''FROM TO '` FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 20 21D0 183.02 3.260 L 2.00 0.0899 PT 38.22 ( 21) O 270.07 F=T F 14.00 PE 0.00 NC C100 T 16.00 PF 1.44 PT 39.66 ( 20) 123 223 1.049 L 1.00 0.1687 PT 11.72 (223) ' 0 19.17 F=E F 1.00 PE 0.43 SG C100 T 2.00 PF 0.34 '^122 123 1.049 L 6.50 0.1687 PT 12.49 (123) O 19.17 F=E F 1.00 PE0.00 BN4 C100 T 7.50 PF 1.27 . PT 13.76 (122) 108 208 1.049 L 1.00 0.1695 PT 11.79 (208) O 19.23 F=E F 1.00 PE 0.43 SG C100 T 2.00 PF 0.34 107 108 1.049 L 6.50 0.1695 PT 12.56 (108) O 19.23 F=E F 1.00 PE 0.00 BN C100 T 7.50 PF 1.27 PT 13.83 (107) '127 227 1.049 L 1.00 0.1228 PT 8.32 (227) O 16.16 F=T F 4.00 PE 0.43 SG C100 T 5.00 PF 0.61 122 127D0 16.00 O 32.16 1.049 L 6.00 0.4389 PT 9.36 (127) F=T F 4.00 PE 0.00 BN4 C100 T 10.00 PF 4.39 '121 122D0 19.17 1.380 L 3.00 0.2742 PT 13.75 (122) O 51.33 F=0/E F 2.00 PE 0.00 BN4 C100 T 5.00 PF 1.37 , 120 121D0 21.78 1.610 L 3.00 0.2490 PT 15.12 (121) O 73.11 F=0 F 0.00 PE 0.00 BN4 C100 T 3.00 PF 0.75 PT 15.87 (120) 126 226 1.049 L 1.00 0.1233 PT 8.35 (226) O 16.19 F=T F 4.00 PE 0.43 SG C100 T 5.00 PF 0.62 PT 9.40 (126) 120 125 Q 20.50 ' 119 120DQ 73.11 Q 93.61 1.049 L 9.00 0.1908 PT 13.40 (125) F=T F 4.00 PE 0.00 BN4 C100 T 13.00 PF 2.48 1.610 L 7.00 0.3934 PT 15.88 (120) F=T F 6.00 PE 0.00 BN4 C100 T 13.00 PF 5.11 TUKWILA, WA. ''FROM TO FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 118 119D0 25.65 1.610 Q 119.26 L 10.00 0.6157 PT 20.99 (119) F=0/T F 6.00 PE 0.00 BN4 C100 T 16.00 PF 9.85 117 118D0 31.08 2.067 L 1.00 0.2799 PT 30.84 (118) Q 150.34 F=T F 7.00 PE 0.00 BN4 C100 T 8.00 PF 2.24 PT 33.08 (117) '~126 129 1.049 L 8.00 0.1225 PT 8.30 (129) O 16.13 F=E F 1.00 PE 0.00 BN C100 T 9.00 PF 1.10 ^ 107 126D0 16.19 1.049 L 6.00 0.4431 PT 9.40 (126) ` 0 32.32 F=T F 4.00 PE 0.00 BN C100 T 10.00 PF 4.43 106 107D0 19.23 1.380 L 3.00 0.2764 PT 13.83 (107) O 51.55 F=0/E F 2.00 PE 0.00 BN C100 T 5.00 PF 1.38 105 106D0 21.84 1.610 L 3.00 0.2508 PT 15.21 (106) O 73.39 F=0 F 0.00 PE 0.00 BN C100 T 3.00 PF 0.75 PT 15.96 (105) `- 105 124 1.049 L 9.00 0.1918 PT 13.47 (124) O 20.56 F=T F 4.00 PE 0.00 BN C100 T 13.00 PF 2.49 104 105D0 73.39 1.610 L 7.00 0.3960 PT 15.96 (105) O 93.94 F=T F 6.00 PE 0.00 , BN C100 T 13.00 PF 5.15 103 104D0 25.73 1.610 L 10.00 0.6197 PT 21.11 (104) O 119.67 F=0/T F 6.00 PE 0.00 BN C100 T 16.00 PF 9.92 102 103D0 31.18 2.067 L 1.00 0.2817 PT 31.03 (103) ' Q 150.85 F=T F 7.00 PE 0.00 BN C100 T 8.00 PF 2.25 PT 33.28 (102) ' 114 115 1.049 L 3.00 0.4176 PT 31.25 (115) O 31.30 F=T F 4.00 PE 0.00 BN3 C100 T 7.00 PF 2.92 PT 34.17 (114) 111 112 1.049 L 9.00 0.3078 PT 22.47 (112) -' 0 26.54 F=0/E F 1.00 PE 0.00 BN2 C100 T 10.00 PF 3.08 TUKWILA, WA. -'FROM TO FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 110 111D0 28.30 1.049 O 54.84 19 20 • 17 19 • 16 17 14 16 ' 12 14 9 12 O 516.18 Q 516.18 Q 516.18 O 516.18 Q 516.18 O 516.18 L 3.00 1.1785 PT 25.55 (111) F=T F 4.00 PE 0.00 BN2 C100 T 7.00 PF 8.25 PT 33.80 (110) 3.260 L 65.00 0.2982 PT 39.70 ( 20) F=0 F 0.00 PE 0.00 FM C100 T 65.00 PF 19.38 3.260 L 30.50 0.2982 PT 59.08 ( 19) F=EE F 3.00 PE 0.00 FM C100 T 33.50 PF 9.99 4.260 L 28.50 0.0810 PT 69.07 ( 17) F=EE F 3.00 PE 0.00 FM C100 T 31.50 PF 2.55 4.260 L 32.50 0.0810 PT 71.62 ( 16) F=0 F 0.00 PE 0.00 FM C100 T 32.50 PF 2.63 4.260 L 63.00 0.0810 PT 74.25 ( 14) F=0 F 0.00 PE 0.00 FM C100 T 63.00 PF 5.10 4.260 L 53.00 0.0810 PT 79.35 ( 12) F=E F 8.00 PE 0.00 FM C100 T 60.00 PF 4.86 8 9 4.260 L 18.00 0.0810 PT 84.21 ( 9) O 516.18 F=E F 8.00 PE 0.43 FM C100 T 26.00 PF 2.11 4 8 4.260 L 26.00 0.0810 PT 86.75 ( 8) Q 516.18 F=GV,CV F 19.00 PE 10.61 ^ FR C100 T 45.00 PF 3.64 3 4 4.260 L 1.50 0.0578 PT101.00 ( 4) Q 516.18 F=0 F 0.00 PE 0.65 ' FR C120 T 1.50 PF 0.09 ' 2 3 4.155 L 35.00 0.0491 PT101.74 ( 3) O 516.18 F=T,EE,E F 53.00 PE 1.73 UN C140 T 88.00 PF 4.32 1 2 6.215 L 35.00 0.0069 PT107.79 ( 2) O 516.18 F=GV,EE F 16.00 PE 0.00 UN C140 T 51.00 PF 0.35 0 1 O 516.18 8.325 L 14.00 0.0017 PT108.14 ( 1) F=T,GV,DDC F 4179.00 PE 0.00 UN C140 T 4193.00 PF 7.13 PT115.27 ( 0) . TUKWILA, WA. PRESSURE AVAILABLE AT NODE 0 AT 766.2 GPM MAXIMUM PRESSURE UNBALANCE IN LOOPS 0.041 PSI -.MAXIMUM VELOCITY IN PIPES 20.36 FPS ' `' _, .^ 138.6 PSI JOB. NO. HYDRAULIC SUMMARY SHEET CUSTOMER'S P.O. NO. CUSTOMER'S NAME / P-4Etub6V S cr/reS ADDRESS 4.9 2S ,S_ Ce/47-EQ gLv-n, DESCRIPTION OF HAZARD °AA, &/Z p trP / ' • AUTHORITY HAVING JURISDICTION -77//Lwi C_,4 CALCULATIONS BY P as tAz--A-yt/ SHEET NO / OF DRAWING NO 5 P- S r1,k tv-/ LA 444 DATE tO — ¢'9� 'AREA TO BE CALCULATED SYSTEM REQUIREMENTS 012 REQUIRED DENSITY PER. SQ. FT. ,ALLOWANCE FOR INSIDE HOSE STATIONS ALLOWANCE FOR OUTSIDE FIRE HYDRANTS • 'TOTAL WATER REQUIRED: /� 2 zso • G P M. 7¢z G.P.M. AT / 4 3 GPM P.S.I. REMARKS' WATER SUPPLY INFORMATION STATIC PRESSURE INPSI 1 4 - RESIDUAL PRESSURE: G.P.M. FLOWING }UMP DATA: TANK DATA: 3/ S7 AT PSI ELEVATION LOCATION RATED CAPACITY: G.P.M. AT P S I ELEVATION LOCATION CAPACITY G P M ELEVATION LOCATION REMARKS: ABBREVIATIONS o — FLOW INCREMENT AT SPECIFIC LOCATION Q — FLOW AT A SPECIFIC LOCATION 4u.P.M. — GALLONS PER MINUTE P.S.I. — POUND PER SQUARE INCH PT — TOTAL PRESSURE IN P.S.I. PF — PRESSURE LOSS DUE TO FRICTION PE — PRESSURE CHANGE DUE TO ELEVATION EE — 450 ELBOW E — 900 ELBOW L.T.E. — LONG TURN ELBOW ;A R FO RM 1435 3/67 T — TEE C — CROSS DEL. V. — DELUGE VALVE DRY. V. — DRY VALVE AL. V. — ALARM VALVE GV — GATE VALVE CV — SWING CHECK VALVE AV — ANGLE VALVE GLV — GLOBE VALVE ST — STRAINER PRIM TBD IN V.S.A. CONTRACT NO. NAME: HantEwOdSVI J' ADDRESS: 492- S S. G EST-* BLV19. 7Pgta L,, (�r4 MULTIPLY SCALE BY PSI m N1.85 GRAPH SHEET N0. � OF SYSTEM NO. 137-114- 8 DATE: /DJ¢'IT/ 0 TLIKWILAq WA. BLDG NO. 8 ATTIC DRY SYSTEM DESIGN DENSITY .16/1950 FLOW TEST RESULTS STATIC RESIDUAL AT 3157.0 GPM PRESSURE AVAILABLE AT 741.6 GPM SUMMARY OF SPRINKLER OUTFLOWS ACTUAL MINIMUM SPR FLOW FLOW K -FACTOR PRESSURE 10.3 22.92 16.00 104 20.74 16.00 105 17.64 16.00 206 16.00 16.00 107 27.44 16.00 108 24.94 16.00 109 20.47 16.00 110 19.39 16.00 111 27.62 16.00 112 22.77 16.00 117 21.72 16.00 116 24.06 16.00 117 19.72 16.00 118 18.68 16.00 219 24.52 16.00 220 21.25 16.00 221 25.40 16.00 ��� 22.83 16.00 123 24.47 16.00 124 21.27 16.00 125 25.33 16.00 126 22.82 16.00 5.60 5.60 5.60 5.60 5.60 5.60 5.60 5.60 5.60 5.60 5.60 5.60 5.60 5.60 5.60 5.60 5.60 5.60 5.60 5.60 5.60 5.60 TOTAL WATER REQUIRED FOR SYSTEM OUTSIDE HOSE STREAMS AT 0 TOTAL WATER REQUIREMENT PRESSURE REQUIRED AT 0 16.75 17.72 9.92 8.16 24.01 19.84 13.76 11.99 24.3: 7••' 16.54 14.50 18.45 12.40 11.12 19.18 14.40 20.58 16.63 19.09 14.43 20.46 16.60 141.00 PSI 108.010 PSI 138.74 PSI 491.60 GPM 250.00 GPM 741.60 GPM 102.11 PS I MAXIMUM PRESSURE UNBALANCE IN LOOPS 0.082 PSI MAXIMUM VELOCITY IN PIPES 18.90 FPS TUkWILA, WA. -'FROM TO FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIFE PSI/FT SUMMARY LEN/FT PSI 106 206 105 i06 O 16.00 O 16.00 1.049 L 1.00 0.1207 PT 8.16 (206 ) F=0 F 0.00 PE 0.47 SG C100 T 1.00 PF 0.12 1.049 L 9.00 0.1207 PT 8.71 (106) F=E F 1.00 PE 0.00 BN C100 T 10.00 PF 1.21 104 105D0 17.64 1.049 L 7.00 0.4771 PT 9.92 (105) O .7.64 F=0/E F 1.00 PE 0.00 BN C100 T 8.00 PF 3.82 . ~ 103 104D0 20.74 1.380 L 10.00 0.7051 PT 17.74 (104 ) O 54.78 F=0 F 0.00 PE 0.00 BN C100 T 10.00 PF 3.05 • J 102 103D0 22.92 1.610 L 10.00 0.2760 PT 16.79 (103) O 77.70 F=0 F 0.00 PE 0.00 ti. BN C100 T 10.00 PF 2.76 PT 19.55 (102) 122 222 1.049 L 1.00 0.23.30 PT 16.63 (222) O 22.8= F=T F 4.00 PE 0.43 SG C100 T 5.00 PF 1.16 PT 18.22 (122) J 121 221 1.049 L 1.00 0.2838 PT 20.58 (221) O 25.40 F=T F 4.00 PE 0.47 SG C100 T 5.00 PF 1.42 PT 22.43 (121) 120 220 1.049 L 1.00 0.2040 PT 14.40 (220) O 21.25 F=T F 4.00 PE 0.43 SG C100 T 5.00 PF 1.02 PT 15.85 (120) 119 219 1.049 L 1.00 0.2659 PT 19.18 (219) O 24.52 F=T F 4.00 PE 0.47 SG C100 T 5.00 PF 1.77 PT 20.94 (119) 122 126 1.049 L 7.00 0.2326 PT 16.60 (126) O 22.82 F=0 F 0.00 PE 0.00 BN C100 T 7.00 PF 1.63 '115 122D0 22.83 1.049 L 1.00 0.8193 PT 18.23 (122) O 45.65 F=T F 4.00 PE 0.00 BN C100 T 5.00 PF 4.20 PT 22.43 (115) TUKWILA, WA. • FROM TO FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 121 125 O 25.33 1.049 L 7.00 0.2823 PT 20.46 (125) F=0 F 0.00 PE 0.00 BN C100 T 7.00 PF 1.98 ` 114 121D0 25.40 1.049 L 1.00 1.0204 PT 22.44 (121) ' 0 50.73 F=T F 4.00 PE 0.00 BN C100 T 5.00 PF 5.10 PT 27.54 (114) 120 124 O 21.27 1.049 L 7.00 0.2043 PT 14.43 (124) F=0 F 0.00 PE 0.00 BN C100 T 7.00 PF 1.43 ^ 102 120D0 21.25 1.049 L 1.00 0.7360 PT 15.86 (120) O 42.52 F=T F 4.00 PE 0.00 BN C100 T 5.00 PF 3.68 101 102D0 77.30 1.610 O 119.82 L 10.00 0.6211 PT 19.54 (102) F=0 F 0.00 PE 0.00 BN C100 T 10.00 PF 6.21 PT 25.75 (101) '' 119 123 1.049 L 7.00 0.2648 PT 19.09 (123) O 24.47 F=0 F 0.00 PE 0.00 BN C100 T 7.00 PF 1.85 101 119D0 0 12 24.52 48.99 101DQ 119.82 O 168.80 O 168.80 1.049 L 1.00 0.9564 PT 20.94 (119) F=T F 4.00 PE 0.00 BN C100 T 5.00 PF 4.78 2.067 2.067 . 11 12 3.260 O 168.80 L 26.00 0.3468 PT 25.72 (101) F=T F 7.00 PE 0.00 BN C100 T 33.00 PF 11.44 L 1.25 0.3468 PT 37.16 ( 22) F=T F 7.00 PE 0.54 NR C100 T 8.25 PF 2.86 L 10.00 0.0377 PT 40.56 ( 12) F=0 F 0.00 PE 0.00 NC C100 T 10.00 PF 0.38 PT 40.94 ( 11) 117 118 1.049 L 7.00 0.1606 PT 11.12 (118) O 18.68 F=0/E F 1.00 PE 0.00 BN4 C100 T 8.00 PF 1.28 116 117D0 19.72 1.049 L 10.00 0.6094 PT 12.40 (117) O 38.40 F=0 F 0.00 PE 0.00 BN4 C100 T 10.00 PF 6.09 TUKWILA, WA. ' FROM TO FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 115 116D0 24.06 1.380 Q 62.45 114 115D0 45.65 1.610 O 108.10 L 10.00 0.3942 PT 18.49 (116) F=0 F 0.00 PE 0.00 BN4 C100 T 10.00 PF 3.94 L 10.00 0.5134 PT 22.43 (115) F=0 F 0.00 PE 0.00 BN4 C100 T 10.00 PF 5.13 24 114D0 50.73 2.067 L 26.00 0.3099 PT 27.56 (114) ~ 0 158.84 F=T F 7.00 PE 0.00 BN4 C100 T 33.00 PF 10.23 14 24 O 158.84 2.067 '~ 13 14 3.260 O 158.84 L 1.25 0.3099 PT 37.79 ( 24) F=T F 7.00 PE 0.54 NR C100 T 8.25 PF 2.56 L 10.00 0.0337 PT 40.89 ( 14) F=0 F 0.00 PE 0.00 NC C100 T 10.00 PF 0.34 PT 41.23 ( 13) 112 113 1.049 L 10.00 0.2053 PT 14.50 (113) O 21.32 F=0 F 0.00 PE 0.00 BN3 C100 T 10.00 PF 2.05 111 112D0 22.77 O 44.10 1.049 L 10.00 0.7873 PT 16.55 (112) F=0 F 0.00 PE 0.00 BN3 C100 T 10.00 PF 7.87 33 111D0 27.62 1.380 O 71.72 23 33 1.610 2.067 Q 71.72 13 23 Q 71.72 13 33 1.610 L 10.00 0.5091 PT 24.42 (111) F=0 F 0.00 PE 0,00 BN3 C100 T 10.00 PF 5.09 L 26.00 0.2403 PT 29.51 ( 33) F=T F 6.00 PE 0.00 BN3 C100 T 32.00 PF 7.69 L 7.00 0.0712 PT 37.20 F=T F 7.00 PE 3.03 NR C100 T 14.00 PF 1.00 ( 23) ' 10 1300 158.84 3.260 L 5.50 0.0671 PT 41.23 ( 13) O 230.55 F=T F 14.00 PE 0.00 NC C100 T 19.50 PF 1.31 PT 42.54 ( 10) • ' 109 110 O 19.39 1.049 L 7.00 0.1722 PT 11.99 (110) F=0/E F 1.00 PE 0.00 BN2 C100 T 8.00 PF 1.38 TUKWILA, WA. ''FROM TO ,� FLOW DIAM GPM IN 108 109D0 20.47 1.049 O 39.86 `107 108DQ 24.94 Q 64.80 1.380 L F=0 F BN2 C100 T L F=0 F BN2 C100 T 21 107D0 27.44 1.610 L O 92.24 F=T F BN2 C100 T 11 21 O 92.24 2.067 L F=T F NR C100 T 10 11D0 168.80 3.260 L O 261.05 F=T F NC C100 T 9 10D0 230.55 3.260 O 491.60 8 9 O 491.60 5 8 O 491.60 4 5 O 491.60 3 4 Q 491.60 O 491.60 1 2 O 491.60 0 1 O 491.60 2 3.260 3.260 FM FM L F=E F C100 T L F=2E F C100 T L F=GV,CV F FR C100 T 4.260 L F=0 F FR C120 T EQUIV PIPE LEN/FT P -LOSS PSI/FT PRESSURE SUMMARY PSI 10.00 0.6530 PT 13.37 (109) 0.00 PE 0.00 10.00 PF 6.53 10.00 0.4221 PT 19.90 (108) 0.00 PE 0.00 10.00 PF 4.22 26.00 0.3829 PT 24.12 (107) 6.00 PE 0.00 32.00 PF 12.25 7.00 7.00 14.00 0.1134 PT PE PF 4.50 0.0845 PT 14.00 PE 18.50 PF 36.37 ( 21) 3.03 1.59 40.99 ( 11) 0.00 1.56 31.00 0.2724 PT 42.55 ( 10) 6.00 PE 0.00 37.00 PF 10.08 32.00 0.2724 PT 52.63 ( 13.00 PE 0.00 45.00 PF 12.26 9) 17.00 0.2724 PT 64.89 ( 8) 16.00 PE 7.36 33.00 PF 8.99 1.50 0.0528 0.00 1.50 4.155 L 140.00 F=3E F 48.00 UN C140 T 188.00 4.155 L F=EE F UN C140 T 6.215 L F=EE,GV F UN C140 T 8.325 L F=T,GV,DDC F UN C140 T 49.00 6.00 55.00 0.0449 0 35.00 0. 16.00 51.00 0449 0063 PT PE PF PT PE PF PT PE PF PT PE PF 81.24 ( 5) 0.65 0.08 81.97 ( 4) 1.73 8.44 92.14 ( 3) 0.00 2.47 94.61 ( 2) 0.00 0.32 14.00 0.0015 PT 94.93 ( 1) 4728.00 PE 0.00 4742.00 PF 7.11 PRESSURE AVAILABLE AT NODE 0 AT 741.6 GPM 'MAXIMUM PRESSURE UNBALANCE IN LOOPS 0.082 PSI MAXIMUM VELOCITY IN PIPES 18.90 FPS PT102.04 ( 0) 138.7 PSI •JOB. NO. HYDRAULIC SUMMARY SHEET CUSTOMER'S P.O. NO. CUSTOMER'S NAME . ADDRESS DESCRIPTION OF HAZARD AUTHORITY HAVING JURIS from E 1al0O/2 S C' /7 -r -S g aS' 5_ d c—AsTr-x. BL.vta. 012 P e9 DICTION %lJ'Ke-e-r/LiQ CALCULATIONS BY r. SHEET NO / OF DRAWING NO SP -4. Tvk t,gFtc •4 , Ler DATE SYSTEM REQUIREMENTS AREA TO BE CALCULATED ATTIC t7 /? L/ S Ld C 5' "REQUIRED DENSITY PER. SQ. FT ALLOWANCE FOR INSIDE HOSE STATIONS ALLOWANCE FOR OUTSIDE FIRE HYDRANTS .1 Asa • ,TOTAL WATER REQUIRED: 2.5^O 7325 G.P.M. AT !e77 • G P M. GPM P.S.I. REMARKS* STATIC PRESSURE IN P S I iESIDUAL PRESSURE: G.P.M. FLOWING 31 s-7 AT to S P.S.I. ELEVATION LOCATION , !UMP DATA: TANK DATA: WATER SUPPLY INFORMATION /41 RATED CAPACITY: G.P.M. AT P S I ELEVATION LOCATION CAPACITY G.P.M. ELEVATION LOCATION REMARKS: ABBREVIATIONS o - FLOW INCREMENT AT SPECIFIC LOCATION Q - FLOW AT A SPECIFIC LOCATION - GALLONS PER MINUTE P.S.I. - POUND PER SQUARE INCH PT - TOTAL PRESSURE IN P.S.I. • PF - PRESSURE LOSS DUE TO FRICTION PE - PRESSURE CHANGE DUE TO ELEVATION EE - 450 ELBOW E - 900 ELBOW L.T.E. - LONG TURN ELBOW AR FORM MSS 3/67 T - TEE C - CROSS DEL. V. - DELUGE VALVE DRY. V. - DRY VALVE AL. V. - ALARM VALVE GV - GATE VALVE CV - SWING CHECK VALVE AV - ANGLE VALVE GLV - GLOBE VALVE ST - STRAINER PRINTED IN U.S.A. •.J ..I CONTRACT NO. NAME: HoM E woo D S tf , rE-.5 ADDRESS: G`/Z S S- GeN7-5--R BWWD. %vktijt L.A , JA o a J 0 ti 4► 0 MULTIPLY SCALE BY i5 PSI 1 Mf N N1.85 GRAPH SHEET N0. OF SYSTEM NO. $4-D6r GSeF; DATE: /D/¢/9/ 1111111111111111011 ♦ -) • I I { • r AIM 11.1.11.M111 111111111111111111111=1 MENEM I I, 14 � ISI 11111 M ' ! I I NMI IIouuwmuinim i i t -t I 1H rr . 11111111111111111111M111 Mill NM 1111111111111111111111111111111111111111111111111011 'Illhall11111111111111m1 4f NN1 mI mad UluI 1UNNl s NuIIINNNuuuflI NNI rs 1 MI 1 atignm_ Milli e—rnlwI lI1 1i reunamlunniniame and Low r (! 4t41 41i`R�lli1 ihk -4* 1 I -4 `!i 444 1 { I N■N.N.N. ,.v WIN _ M. '.N... X 1 li -4 ii ii; II, 0 HYDRAULIC SUMMARY SHEET 'JOB. NO. SHEET NO / OF / CUSTOMER'S P.O. NO. DRAWING NO SP -4. CUSTOMER'S NAME FMLit....rDB0 5U'ii- r ADDRESS 49 2 S .5. c eki-ren BLv b DESCRIPTION OF HAZARD dRt, • 4-/24Pcf/' ' ' 'AUTHORITY HAVING JURISDICTION rll/..(.e./-/LA CALCULATIONS BY P !3 v tsrw / DATE J AREA TO BE CALCULATED SYSTEM REQUIREMENTS /G REQUIRED DENSITY PER. SQ. FT ALLOWANCE FOR INSIDE HOSE STATIONS kLLOWANCE FOR OUTSIDE FIRE HYDRANTS ' -TOTAL WATER REQUIRED: //1S -c• 4 i31 -t;4 - 25V 72 Go G.P.M. AT G P.M. GPM P.S.I. 7EMARKS' WATER SUPPLY INFORMATION cTATIC PRESSURE IN P S 1 / ¢ / IES1DUAL PRESSURE: G.P.M. FLOWING a 15 7 P S I ELEVATION LOCATION .UMP DATA: TANK DATA: AT 105 RATED CAPACITY: G.P.M. AT P S 1 ELEVATION LOCATION CAPACITY G P M ELEVATION LOCATION REMARKS' ABBREVIATIONS o - FLOW INCREMENT AT SPECIFIC LOCATION Q - FLOW AT A SPECIFIC LOCATION ti:P.M. - GALLONS PER MINUTE .P.S.I. - POUND PER SQUARE INCH PT - TOTAL PRESSURE IN P.S.I. • PF - PRESSURE LOSS DUE TO FRICTION PE - PRESSURE CHANGE DUE TO ELEVATION EE - 450 ELBOW E -900 ELBOW L.T.E. - LONG TURN ELBOW S. AR FO RM MSS 8/47 T - TEE C - CROSS DEL. V. - DELUGE VALVE DRY. V. - DRY VALVE AL. V. - ALARM VALVE GV - GATE VALVE CV - SWING CHECK VALVE AV - ANGLE VALVE GLV - GLOBE VALVE ST - STRAINER PRINTED IN U.S.A. SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD TUKWILA, WA BLDG NO. E5 2ND FLR. REMOTE UNIT (8 SPKR. FLOWING) FLOW TEST RESULTS STATIC RESIDUAL AT 3157.0 GPM PRESSURE AVAILABLE AT 503.8 GPM SUMMARY OF SPRINKLER OUTFLOWS ACTUAL MINIMUM SPR FLOW FLOW K -FACTOR 101 38.19 14.82 102 38.14 22.08 103 36.62 14.82 104 36.58 14.82 206 34.56 34.56 207 34.15 14.82 108 35.57 14.82 5.60 5.60 5.60 5.60 5.60 5.60 5.60 TOTAL WATER REQUIRED FOR SYSTEM OUTSIDE HOSE STREAMS AT 0 TOTAL WATER REQUIREMENT PRESSURE REQUIRED AT 0 PRESSURE 46.50 46.39 42.77 42.66 38.09 37.18 40.34 10-03-1991 PAGE 1 141.00 PSI 108.00 PSI 139.89 PSI 253.80 GPM 250.00 GPM 503.80 GPM 92.08 PSI MAXIMUM PRESSURE UNBALANCE IN LOOPS 0.083 PSI MAXIMUM VELOCITY IN PIPES 18.20 FPS SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD TUKWILA, WA FROM TO 10-03-1991 PAGE 2 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 106 206 1.049 L 2.00 0.3580 PT 38.09 (206) Q 34.56 F=T F 5.00 PE 0.00 AO C120 T 7.00 PF 2.51 PT 40.60 (106) 107 207 1.049 L 4.00 0.3501 PT 37.18 (207) Q 34.15 F=T F 5.00 PE 0.00 AO C120 T 9.00 PF 3.15 108 107DQ -21.59 1.380 L 3.00 0.0145 PT 40.33 (107) Q 12.55 F=0 F 0.00 PE 0.00 BL C120 T 3.00 PF 0.04 26 108D0 35.57 1.380 L 6.50 0.1737 PT 40.37 (108) Q 48.12 F=0/E F 3.00 PE 0.00 BL C120 T 9.50 PF 1.65 25 26 1.380 L 8.50 0.1737 PT 42.02 ( 26) Q 48.12 F=0 F 0.00 PE 0.00 CM1 C120 T 8.50 PF 1.48 • PT 43.50 ( 25) 106 107 1.380 L 5.50 0.0394 PT 40.25 (107) O 21.59 F=0 F 0.00 PE 0.00 BL C120 T 5.50 PF 0.22 16 10600 34.56 1.380 L 29.50 0.2311 PT 40.47 (106) Q 56.15 F=E F 3.00 PE 0.00 BL C120 T 32.50 PF 7.51 15 16 1.610 L 8.50 0.1091 PT 47.98 ( 16) Q 56.15 F=0 F 0.00 PE 0.00 CM C120 T 8.50 PF 0.93 PT 48.91 ( 15) 105 104 1.380 L 8.50 0.0399 PT 42.66 (104) Q 21.73 F=0 F 0.00 PE 0.00 BL C120 T 8.50 PF 0.34 25 105 1.380 L 5.00 0.0399 PT 43.00 (105) Q 21.73 F=0/T F 6.00 PE 0.00 BL C120 T 11.00 PF 0.44 24 25D0 48.12 1.380 L 10.50 0.3460 PT 43.44 ( 25) O 69.85 F=0 F 0.00 PE 0.00 CM1 C120 T 10.50 PF 3.63 PT 47.07 ( 24) 103 104 Q 14.85 1.380 L 5.50 0.0197 PT 42.66 (104) F=0 F 0.00 PE 0.00 BL C120 T 5.50 PF 0.11 SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD TUKWILA, WA . FROM TO ._1 10-03-1991 PAGE 3 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 15 103D0 36.62 1.380 Q 51.47 14 15DQ 56.15 1.610 O 107.62 24 102 Q 27.63 L 25.50 0.1967 PT 42.77 (103) F=T F 6.00 PE 0.00 BL C120 T 31.50 PF 6.20 L 10.50 0.3635 PT 48.97 ( 15) F=0 F 0.00 PE 0.00 CM C120 T 10.50 PF 3.82 PT 52.79 ( 14) 1.380 L 4.50 0.0622 PT 46.39 (102) F=0/T F 6.00 PE 0.00 BL C120 T 10.50 PF 0.65 23 24D0 69.85 1.610 L 6.00 0.3026 PT 47.04 ( 24) Q 97.47 F=0 F 0.00 PE 0.00 CM1 C120 T 6.00 PF 1.82 PT 48.86 ( 23) 101 102 Q 10.51 1.380 L 11.00 0.0104 PT 46.39 (102) F=0 F 0.00 PE 0.00 BL C120 T 11.00 PF 0.11 14 101D0 38.19 1.380 Q 48.70 L 29.00 0.1776 PT 46.50 (101) F=T F 6.00 PE 0.00 BL C120 T 35.00 PF 6.22 13 14D0 107.62 2.067 L 6.00 0.2147 PT 52.72 ( 14) Q 156.32 F=0 F 0.00 PE 0.00 CM C120 T 6.00 PF 1.29 PT 54.01 ( 13) 13 23 O 34.03 1.380 L 44.50 0.0915 PT 48.87 ( 23) F=T/T F 12.00 PE 0.00 BL C120 T 56.50 PF 5.17 5 13D0 156.32 2.067 L 9.00 0.3091 PT 54.04 ( 13) Q 190.35 F=0 F 0.00 PE 0.00 CM C120 T 9.00 PF 2.78 PT 56.82 ( 5) 22 23 Q 63.44 1.380 L 10.50 0.2896 PT 48.87 ( 23) F=0 F 0.00 PE 0.00 CM1 C120 T 10.50 PF 3.04 12 22DQ -30.85 1.380 Q 32.59 21 22 Q 30.85 L 44.50 0.0845 PT 51.91 ( 22) F=T/T F 12.00 PE 0.00 BL C120 T 56.50 PF 4.77 PT 56.68 ( 12) 1.380 L 8.50 0.0763 PT 51.93 ( 22) F=0 F 0.00 PE 0.00 CM1 C120 T 8.50 PF 0.65 SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD TUKWILA, WA FROM TO 10-03-1991 PAGE 4 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 11 21 1.380 L 44.50 0.0763 PT 52.58 ( 21) Q 30.85 F=E/E F 6.00 PE 0.00 BL C120 T 50.50 PF 3.85 12 11 1.610 L 8.50 0.0360 PT 56.43 ( 11) Q 30.85 F=0 F 0.00 PE 0.00 CM C120 T 8.50 PF 0.31 5 12DQ 32.59 2.067 L 1.50 0.0405 PT 56.74 ( 12) Q 63.44 F=0 F 0.00 PE 0.00 CM C120 T 1.50 PF 0.06 4 5DQ 190.35 2.635 L 1.00 0.1613 PT 56.80 ( 5) Q 253.80 F=E F 8.00 PE 0.00 FR C12.0 T 9.00 PF 1.45 3 4 2.635 L 9.00 0.1613 PT 58.25 ( 4) Q 253.80 F=T F 16.00 PE 3.90 FR C120 T 25.00 PF 4.03 2 3 2.635 L 14.00 0.1613 PT 66.18 ( 3) Q 253.80 F=T,3E,CV/GV F 60.00 PE 2.81 FR C120 T 74.00 PF 11.94 1 2 4.124 L 1.50 0.0182 PT 80.93 ( 2) Q 253.80 F=0 F 0.00 PE 0.65 FR C120 T 1.50 PF 0.03 0 1 4.155 L 44.00 0.0132 PT 81.61 ( 1) Q 253.80 F=2T,2GV,E/DDC F 618.00 PE 1.73 UN C140 T 662.00 PF 8.74 PRESSURE AVAILABLE AT NODE 0 AT 503.8 GPM MAXIMUM PRESSURE UNBALANCE IN LOOPS 0.083 PSI MAXIMUM VELOCITY IN PIPES 18.20 FPS PT 92.08 ( 0) 139.9 PSI SUBMITTAL SERIAL NO:2022H-08 HOMEWOOD SUITES TUKWILA, WA. .BLDG E5 ATTIC DRY SYSTEM DESIGN DENSITY .16/1950 `^ SPR '206 207 ^'108 - .109 110 ''111 112 '114 . '115 116 •.118 119 -'124 125 127 ''129 131 217 .'221 226 -228 230 ., FLOW TEST RESULTS STATIC RESIDUAL AT 3157.0 GPM PRESSURE AVAILABLE AT 726.3 GPM SUMMARY OF SPRINKLER OUTFLOWS ACTUAL MINIMUM FLOW FLOW K -FACTOR PRESSURE ____ ---- 25.71 16.00 5.60 21.07 24.62 16.00 5.60 19.34 24.04 16.00 5.60 18.43 28.66 16.00 5.60 26.19 26.90 16.00 5.60 23.08 22.04 16.00 5.60 15.49 23.60 16.00 5.60 17.75 22.80 16.00 5.60 16.57 20.90 16.00 5.60 13.93 16.00 16.00 5.60 8.16 20.77 16.00 5.60 13.76 22.86 16.00 5.60 16.66 23.81 16.00 5.60 18.08 21.19 16.00 5.60 14.32 16.33 16.00 5.60 8.51 18.53 16.00 5.60 10.95 19.72 16.00 5.60 12.40 16.16 16.00 5.60 8.32 26.53 16.00 5.60 22.44 16.50 16.00 5.60 8.69 18.69 16.00 5.60 11.14 19.92 16.00 5.60 12.66 ''TOTAL WATER REQUIRED FOR SYSTEM OUTSIDE HOSE STREAMS AT 0 TOTAL WATER REQUIREMENT ..PRESSURE REQUIRED AT 0 MAXIMUM PRESSURE UNBALANCE IN LOOPS MAXIMUM VELOCITY IN PIPES 09-23-1991 PAGE 1 141.00 PSI 108.00 PSI 138.82 PSI 476.27 GPM 250.00 GPM 726.27 GPM 79.66 PSI 0.097 PSI 18.51 FPS SUBMITTAL SERIAL NO:2022H-08 HOMEWOOD SUITES TUKWILA, WA. ,FROM TO `^ 09-23-1991 PAGE 2 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI ..117 116 1.049 L 9.00 0.1207 PT 8.16 (116) O 16.00 F=0/E F 1.00 PE 0.00 BN4 C100 T 10.00 PF 1.21 PT 9.37 (117) 121 221 1.049 L 2.00 0.3074 PT 22.44 (221) O 26.53 F=T F 4.00 PE 0.43 AO C100 T 6.00 PF 1.84 PT 24.71 (121) _^130 230 O 19.92 1.049 L 1.00 F=T F 4.00 SG C100 T 5.00 0.1811 PT 12.66 (230) PE 0.43 PF 0.91 PT 14.00 (130) 128 228 1.049 L 1.00 0.1608 PT 11.14 (228) O 18.69 F=T F 4.00 PE 0.43 SG C100 T 5.00 PF 0.80 PT 12.37 (128) .126 226 1.049 L 1.00 0.1278 PT 8.69 (226) O 16.50 F=T F 4.00 PE 0.43 SG C100 T 5.00 PF 0.64 PT 9.76 (126) 117 217 O 16.16 1.049 L 1.00 0.1228 PT 8.32 (217) F=T F 4.00 PE 0.43 SG C100 T 5.00 PF 0.61 118 117D0 16.00 1.049 L 9.00 0.4389 PT 9.36 (117) O 32.16 F=E F 1.00 PE 0.00 BN4 C100 T 10.00 PF 4.39 119 118D0 20.77 1.380 L 8.00 0.2902 PT 13.75 (118) O 52.93 F=0/E F 2.00 PE 0.00 BN4 C100 T 10.00 PF 2.90 '120 119D0 22.86 1.610 L 2.50 0.2662 PT 16.65 (119) O 75.79 F=E F 3.00 PE 0.00 BN4 C100 T 5.50 PF 1.46 PT 18.11 (120) 107 207 1.049 L 1.00 0.2679 PT 19.34 (207) O 24.62 F=T F 4.00 PE 0.43 SG C100 T 5.00 PF 1.34 PT 21.11 (107) '106 206 O 25.71 1.049 L 1.00 0.2901 PT 21.07 (206) F=T F 4.00 PE 0.43 SG C100 T 5.00 PF 1.45 SUBMITTAL SERIAL NO:2022H-08 HOMEWOOD SUITES TUKWILA, WA. .FROM TO '105 106 09-23-1991 PAGE 3 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI Q 25.71 `'130 131 O 19.72 123 130D0 O 19.92 39.64 1.049 L 10.50 0.2901 PT 22.95 (106) F=0/E F 1.00 PE 0.00 BN C100 T 11.50 PF 3.34 PT 26.29 (105) 1.049 L 8.00 0.1776 PT 12.40 (131) F=E F 1.00 PE 0.00 BN4 C100 T 9.00 PF 1.60 1.049 L 6.00 0.6466 PT 14.00 (130) F=T F 4.00 PE 0.00 BN4 C100 T 10.00 PF 6.47 PT 20.47 (123) 128 129 1.049 L 8.00 0.1583 PT 10.95 (129) ' O 18.53 F=E F 1.00 PE 0.00 BN4 C100 T 9.00 PF 1.42 '1120 128D0 18.69 1.049 L 6.00 0.5752 PT 12.37 (128) O 37.22 F=T F 4.00 PE 0.00 BN4 C100 T 10.00 PF 5.75 ^' 121 12000 75.79 1.610 O 113.00 L 9.00 0.5573 PT 18.12 (120) F=0/E F 3.00 PE 0.00 BN4 C100 T 12.00 PF 6.69 122 121D0 26.53 2.067 L 1.50 0.2438 PT 24.81 (121) O 139.53 F=E F 4.00 PE 0.00 BN4 C100 T 5.50 PF 1.34 PT 26.15 (122) 126 127 1.049 L 9.00 0.1253 PT 8.51 (127) O 16.33 F=E F 1.00 PE 0.00 BN4 C100 T 10.00 PF 1.25 125 12600 16.50 O 32.84 1.049 L 9.00 0.4563 PT 9.76 (126) F=0/E F 1.00 PE 0.00 BN4 C100 T 10.00 PF 4.56 124 125D0 21.19 1.380 L 8.50 0.3015 PT 14.32 (125) O 54.02 F=T F 4.00 PE 0.00 BN4 C100 T 12.50 PF 3.77 123 124DQ 23.81 Q 77.83 1.610 L 2.50 0.2796 PT 18.09 (124) F=#/T F 6.00 PE 0.00 BN4 C100 T 8.50 PF 2.38 122 12300 39.64 1.610 L 9.50 0.5989 PT 20.47 (123) 0 117.48 F=0 F 0.00 PE 0.00 BN4 C100 T 9.50 PF 5.69 SUBMITTAL SERIAL NO:2022H-08 'HOMEWOOD SUITES TUKWILA, WA. ., 09-23-1991 PAGE 4 _FROM TO FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY -' LEN/FT PSI ` 12 122D0 139.53 2.469 L 2.00 0.3177 PT 26.16 (122) O 257.01 F=T F 9.00 PE 0.87 NR C100 T 11.00 PF 3.49 11 12 `~ O 257.01 3.260 L 8.50 0.0821 PT 30.52 ( 12) F=E F 6.00 PE 0.00 NC C100 T 14.50 PF 1.19 PT 31.71 ( 11) 114 115 1.049 L 9.50 0.1978 PT 13.93 (115) O 20.90 F=T F 4.00 PE 0.00 BN3 C100 T 13.50 PF 2.67 113 114DQ 22.80 O 43.69 1.049 L 3.50 0.7740 PT 16.60 (114) F=0/T F 4.00 PE 0.00 BN3 C100 T 7.50 PF 5.80 PT 22.40 (113) 1.049 L 9.50 0.2182 PT 15.49 (111) O 22.04 F=0/E F 1.00 PE 0.00 BN3 C100 T 10.50 PF 2.29 113 112D0 23.60 1.049 L 4.50 0.8388 PT 17.78 (112) O 45.63 F=E F 1.00 PE 0.00 BN3 C100 T 5.50 PF 4.61 11 113D0 43.69 O 89.33 1.610 L 9.00 0.3608 PT 22.39 (113) F=T F 6.00 PE 3.90 NR C100 T 15.00 PF 5.41 10 11D0 257.01 3.260 L 18.00 0.1425 PT 31.70 ( 11) . 0 346.34 F=E F 6.00 PE 0.00 NC C100 T 24.00 PF 3.42 PT 35.12 ( 10) 109 110 1.049 L 9.00 0.3156 PT 23.08 (110) O 26.90 F=E F 1.00 PE 0.00 BN2 C100 T 10.00 PF 3.16 20 109D0 28.66 1.380 L 4.50 0.3175 PT 26.24 (109) O 55.56 F=T F 4.00 PE 0.00 BN2 C100 T 8.50 PF 2.70 10 20 1.610 L 9.00 0.1499 PT 28.94 ( 20) O 55.56 F=T F 6.00 PE 3.90 NR C100 T 15.00 PF 2.25 9 10D0 346.34 3.260 L 8.50 0.1877 PT 35.09 ( 10) O 401.90 F=E F 6.00 PE 0.00 NC C100 T 14.50 PF 2.72 PT 37.81 ( 9) SUBMITTAL SERIAL NO:2022H-08 ''HOMEWOOD SUITES ..TUKWILA, WA. .FROM TO 09-23-1991 PAGE 5 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI '.107 108 1.049 L 9.50 0.2563 PT 18.43 (108) Q 24.04 F=E F 1.00 PE 0.00 BN C100 T 10.50 PF 2.69 105 107D0 24.62 1.049 L 1.50 0.9447 PT 21.12 (107) O 48.66 F=T F 4.00 PE 0.00 BN C100 T 5.50 PF 5.20 104 105D0 25.71 1.380 L 7.50 0.5445 PT 26.32 (105) O 74.37 F=E F 2.00 PE 0.00 BN C100 T 9.50 PF 5.17 1103 104 102 103 O 74.37 O 74.37 1.610 L 8.00 0.2570 PT 31.49 (104) F=0/E F 3.00 PE 0.00 BN C100 T 11.00 PF 2.83 1.610 L 2.50 0.2570 PT 34.32 (103) F=0 F 0.00 PE 0.00 BN C100 T 2.50 PF 0.64 1/4.101 102 2.067 L 9.50 0.0761 PT 34.96 (102) O 74.37 F=0 F 0.00 PE 0.00 BN C100 T 9.50 PF 0.72 '^ 19 101 O 74.37 2.067 L 1.00 0.0761 PT 35.68 (101) F=T F 7.00 PE 0.00 BN C100 T 8.00 PF 0.61 9 19 2.067 L 2.00 0.0761 PT 36.29 ( 19) ` 0 74.37 F=T F 7.00 PE 0.87 NR C100 T 9.00 PF 0.68 8 9D0 401.90 3.260 L 6.50 0.2569 PT 37.84 ( 9) O 476.27 F=E F 6.00 PE 0.00 NC C100 T 12.50 PF 3.21 6 8 3.260 L 16.50 0.2569 PT 41.05 ( 8) O 476.27 F=2E F 13.00 PE 0.00 NC C100 T 29.50 PF 7.58 2 6 3.260 L 16.50 0.2569 PT 48.63 ( 6) Q 476.27 F=GV,CV F 16.00 PE 7.14 FR C100 T 32.50 PF 8.35 1 2 4.260 L 1.50 0.0498 PT 64.12 ( 2) Q 476.27 F=0 F 0.00 PE 0.65 FR C120 T 1.50 PF 0.07 0 1 4.155 L 44.00 0.0423 PT 64.84 ( 1) Q 476.27 F=2T,E,2GV/DDC F 265.00 PE 1.73 UN C140 T 309.00 PF 13.07 SUBMITTAL SERIAL NO:2022H-08 -HOMEWOOD SUITES TUKWILA, WA. PRESSURE AVAILABLE AT NODE 0 AT 726.3 GPM ''MAXIMUM PRESSURE UNBALANCE IN LOOPS 0.097 PSI MAXIMUM VELOCITY IN PIPES 18.51 FPS `' 09-23-1991 PAGE 6 138.8 PSI • _1 SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD TUKWILA, WA BLDG NO. C5 2ND FLR UNIT F (8 SPKR. FLOWING) FLOW TEST RESULTS STATIC RESIDUAL AT 3157.0 GPM PRESSURE AVAILABLE AT 505.7 GPM SUMMARY OF SPRINKLER OUTFLOWS ACTUAL MINIMUM SPR FLOW FLOW K -FACTOR 101 38.81 14.82 102 38.79 22.08 103 36.84 14.82 104 36.82 14.82 206 34.56 34.56 207 34.20 14.82 108 35.64 14.82 5.60 5.60 5.60 5.60 5.60 5.60 5.60 TOTAL WATER REQUIRED FOR SYSTEM OUTSIDE HOSE STREAMS AT 0 TOTAL WATER REQUIREMENT PRESSURE REQUIRED AT 0 PRESSURE 48.03 47.98 43.29 43.23 38.09 37.29 40.51 10-03-1991 PAGE 1 141.00 PSI 108.00 PSI 139.89 PSI 255.66 GPM 250.00 GPM 505.66 GPM 103.92 PSI MAXIMUM PRESSURE UNBALANCE IN LOOPS 0.058 PSI MAXIMUM VELOCITY IN PIPES 17.51 FPS • SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES ' 6925 SOUTHCENTER BLVD TUKWILA, WA FROM TO 10-03-1991 PAGE 2 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI • 106 206 1.049 L 2.00 0.3580 PT 38.09 (206) Q 34.56 F=T F 5.00 PE 0.00 AO C120 T 7.00 PF 2.51 PT 40.60 (106) 107 207 1.049 L 4.00 0.3510 PT 37.29 (207) Q 34.20 F=T F 5.00 PE 0.00 AO C120 T 9.00 PF 3.16 108 107DQ -16.28 1.380 L 2.50 0.0279 PT 40.45 (107) Q 17.91 F=0 F 0.00 PE 0.00 BL C120 T 2.50 PF 0.07 26 108DQ 35.64 1.380 L 6.00 0.2117 PT 40.52 (108) Q 53.55 F=0/E F 3.00 PE 0.00 BL C120 T 9.00 PF 1.91 25 26 1.380 L 8.50 0.2117 PT 42.43 ( 26) Q 53.55 F=0 F 0.00 PE 0.00 CM1 0120 T 8.50 PF 1.80 PT 44.23 ( 25) 106 107 1.380 L 6.00 0.0234 PT 40.46 (107) Q 16.28 F=0 F 0.00 PE 0.00 BL C120 T 6.00 PF 0.14 16 106DQ 34.56 1.380 L 100.00 0.1923 PT 40.60 (106) Q 50.84 F=E F 3.00 PE 0.00 BL C120 T 103.00 PF 19.81 15 16 1.610 L 8.50 0.0908 PT 60.41 ( 16) Q 50.84 F=0 F 0.00 PE 0.00 CM C120 T 8,50 PF 0.77 PT 61.18 ( 15) 105 104 1.380 L 9.00 0.0530 PT 43.23 (104) Q 25.33 F=0 F 0,00 PE 0.00 BL 0120 T 9.00 PF 0.48 25 105 1.380 L 4.00 0.0530 PT 43.71 (105) Q 25.33 F=0/T F 6.00 PE 0.00 BL C120 T 10.00 PF 0.53 24 25D0 53.55 1.380 L 10.50 0.4334 PT 44.24 ( 25) Q 78.88 F=0 F 0.00 PE 0.00 CM1 C120 T 10.50 PF 4.55 PT 48.79 ( 24) 103 104 Q 11.49 1.380 L 5.50 0.0123 PT 43.23 (104) F=0 F 0.00 PE 0.00 BL C120 T 5.50 PF 0.07 SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD TUKWILA, WA . FROM TO •-1 10-03-1991 PAGE 3 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 15 103D0 36.84 1.380 L 96.00 0.1751 PT 43.30 (103) Q 48.33 F=T F 6.00 PE 0.00 BL C120 T 102.00 PF 17.86 14 15DQ 50.84 1.610 L 10.50 0.3124 PT 61.16 ( 15) Q 99.18 F=0 F 0.00 PE 0.00 CM C120 T 10.50 PF 3.28 PT 64.44 ( 14) 24 102 Q 32.10 1.380 L 4.50 0.0821 PT 47.98 (102) F=0/T F 6.00 PE 0.00 BL C120 T 10.50 PF 0.86 23 24DQ 78.88 1.610 L 5.50 0.3847 PT 48.84 ( 24) O 110.98 F=0 F 0.00 PE 0.00 CM1 C120 T 5.50 PF 2.12 PT 50.96 ( 23) 101 102 Q 6.69 1.380 L 11.00 0.0045 PT 47.98 (102) F=0 F 0.00 PE 0.00 BL C120 T 11.00 PF 0.05 14 101D0 38.81 1.380 Q 45.50 L 99.00 0.1566 PT 48.03 (101) F=T F 6.00 PE 0.00 BL C120 T 105.00 PF 16.44 13 14D0 99.18 2.067 L 5.50 0.1861 PT 64.47 ( 14) O 144.68 F=0 F 0.00 PE 0.00 CM C120 T 5.50 PF 1.02 PT 65.49 ( 13) 13 23 Q 38.50 1.380 L 114.50 0.1149 PT 50.90 ( 23) F=T/T F 12.00 PE 0.00 BL C120 T 126.50 PF 14.53 5 13D0 144.68 2.067 L 9.50 0.2879 PT 65.43 ( 13) Q 183.17 F=0 F 0.00 PE 0.00 CM C120 T 9.50 PF 2.74 PT 68.17 ( 5) 22 23 O 72.49 1.380 L 10.50 0.3706 PT 50.90 ( 23) F=0 F 0.00 PE 0.00 CM1 C120 T 10.50 PF 3.89 12 22DQ -35.75 1.380 Q 36.74 21 22 O 35.75 L 114.50 0.1054 PT 54.79 ( 22) F=T/T F 12.00 PE 0.00 BL C120 T 126.50 PF 13.33 PT 68.12 ( 12) 1.380 L 8.50 0.1002 PT 54.79 ( 22) F=0 F 0.00 PE 0.00 CM1 C120 T 8.50 PF 0.85 SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD TUKWILA, WA FROM TO 11 21 10-03-1991 PAGE 4 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI Q 35.75 1.380 L 114.50 0.1002 PT 55.64 ( 21) F=E/E F 6.00 PE 0.00 BL 0120 T 120.50 PF 12.07 12 11 1.610 L 8.50 0.0473 PT 67.71 ( 11) Q 35.75 F=0 F 0.00 PE 0.00 CM C120 T 8.50 PF 0.40 5 12DQ 36.74 2.067 L 1.00 0.0518 PT 68.11 ( 12) Q 72.49 F=0 F 0.00 PE 0.00 CM C120 T 1.00 PF 0.05 4 5DQ 183.17 2.635 L 1.00 0.1635 PT 68.16 ( 5) Q 255.66 F=E F 8.00 PE 0.00 FR C120 T 9.00 PF 1.47 3 4 2.635 L 9.00 0.1635 PT 69.63 ( 4) Q 255.66 F=T F 16.00 PE 3.90 FR C120 T 25.00 PF 4.09 2 3 2.635 L 14.00 0.1635 PT 77.62 ( 3) Q 255.66 F=T,3E,CV/GV F 60.00 PE 2.81 FR C120 T 74.00 PF 12.10 1 2 4.124 L 1.50 0.0185 PT 92.53 ( 2) Q 255.66 F=0 F 0.00 PE 0.65 FR C120 T 1.50 PF 0.03 0 1 4 155 L 67.00 0.0134 PT 93.21 ( 1) Q 255.66 F=T,2E,2GV/DDC F 603.00 PE 1.73 UN C140 T 670.00 PF 8.98 PRESSURE AVAILABLE AT NODE 0 AT 505.7 GPM MAXIMUM PRESSURE UNBALANCE IN LOOPS 0.058 PSI MAXIMUM VELOCITY IN PIPES 17.51 FPS PT103 .92 ( 0) 139.9 PSI SUBMITTAL SERIAL NO:2022H-08 'HOMEWOOD SUITES TUKWILA, WA. .BLDG C5 ATTIC DRY SYSTEM DESIGN DENSITY .16/1950 FLOW TEST RESULTS STATIC RESIDUAL AT 3157.0 GPM PRESSURE AVAILABLE AT 777.8 GPM SUMMARY OF SPRINKLER OUTFLOWS ACTUAL MINIMUM ' SPR FLOW FLOW K -FACTOR PRESSURE ____ ---- 201 25.91 16.00 5.60 21.41 202 24.59 16.00 5.60 19.27 ^103 23.11 16.00 5.60 17.03 104 20.70 16.00 5.60 13.67 205 16.00 16.00 5.60 8.16 ''106 16.48 16.00 5.60 8.66 108 27.88 16.00 5.60 24.78 109 22.76 16.00 5.60 16.51 _~110 21.44 16.00 5.60 14.65 111 28.40 16.00 5.60 25.71 113 24.54 16.00 5.60 19.20 114 22.92 16.00 5.60 16.75 ''115 16.86 16.00 5.60 9.07 216 16.40 16.00 5.60 8.58 117 21.35 16.00 5.60 14.53 '118 23.80 16.00 5.60 18.06 219 24.26 16.00 5.60 18.77 220 24.15 16.00 5.60 18.59 ~222 27.55 16.00 5.60 24.20 223 27.86 16.00 5.60 24.76 127 30.85 16.00 5.60 30.34 TOTAL WATER REQUIRED FOR SYSTEM -'OUTSIDE HOSE STREAMS AT 0 TOTAL WATER REQUIREMENT PRESSURE REQUIRED AT 0 MAXIMUM PRESSURE UNBALANCE IN LOOPS MAXIMUM VELOCITY IN PIPES 487.78 250.00 737.78 107.18 09-23-1991 PAGE 1 141.00 PSI 108.00 PSI 138.76 PSI GPM GPM GPM PSI 0.045 PSI 19.98 FPS SUBMITTAL SERIAL NO:2022H-08 .HOMEWOOD SUITES TUKWILA, WA. .FROM TO 09-23-1991 PAGE 2 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI .' 105 205 1.049 L 2.00 0.1207 PT 8.16 (205) O 16.00 F=T,E F 5.00 PE 0.87 SG C100 T 7.00 PF 0.84 PT 9.87 (105) ' .123 223 1.049 L 2.00 0.3367 PT 24.76 (223) O 27.86 F=T,E F 5.00 PE 0.87 SG C100 T 7.00 PF 2.36 `122 123 1.049 L 0.50 0.3367 PT 27.99 (123) O 27.86 F=0 F 0.00 PE 0.00 BN C100 T 0.50 PF 0.17 PT 28.16 (122) ' 122 222 1.049 L 7.00 0.3297 PT 24.20 (222) O 27.55 F=T,E F 5.00 PE 0.00 AO C100 T 12.00 PF 3.96 121 122D0 27.86 1.380 L 5.00 0.3159 PT 28.16 (122) O 55.41 F=T F 4.00 PE 0.00 ' BN C100 T 9.00 PF 2.84 PT 31.00 (121) 120 220 1.049 L 7.00 0.2584 PT 18.59 (220) . O 24.15 F=T,E F 5.00 PE 0.00 AO C100 T 12.00 PF 3.10 PT 21.69 (120) 119 219 1.049 L 2.00 0.2606 PT 18.77 (219) O 24.26 F=T,E F 5.00 PE 0.87 ^ SG C100 T 7.00 PF 1.82 PT 21.46 (119) 116 216 1.049 L 2.00 0.1263 PT 8.58 (216) ^ O 16.40 F=T,E F 5.00 PE 0.87 SG C100 T 7.00 PF 0.88 PT 10.33 (116) ' 102 202 1.049 L 2.00 0.2671 PT 19.27 (202) O 24.59 F=T,E F 5.00 PE 0.87 SG C100 T 7.00 PF 1.87 PT 22.01 (102) 101 201 1.049 L 7.00 0.2944 PT 21.41 (201) O 25.91 F=T,E F 5.00 PE 0.00 AO C100 T 12.00 PF 3.53 PT 24.94 (101) 126 127 O 30.85 1.049 L 10.00 0.4065 PT 30.34 (127) F=0 F 0.00 PE 0.00 BN C100 T 10.00 PF 4.06 SUBMITTAL SERIAL NO:2022H-08 ' HOMEWOOD SUITES TUKWILA, WA. FROM TO FLOW DIAM GPM IN • 125 126 O 30.85 124 125 ' 19 124 9 19 Q 30.85 Q 30.85 Q 30.85 116 115 O 16.86 • 117 116D0 0 .., ` ' 16.40 33.26 118 117DQ 21.35 O 54.61 1.049 1.380 1.380 2.067 1.049 1.049 1.380 119 118D0 23.80 1.610 O 78.40 120 119D0 24.26 1.610 O 102.66 121 120D0 24.15 1.610 O 126.81 ' 12 121D0 55.41 2.067 Q 182.22 11 12 O 182.22 113 114 0 22.92 3.260 1.049 L F=0 F BN C100 T BN BN L F=0 F C100 T L F=T F C100 T L F=T,E F NR C100 T L F=0/E F BN C100 T BN L F=E F C100 T L F=0/E F BN C100 T BN BN L F=E F C100 T L F=0 F C100 T L F=0/T F BN C100 T NR NC L F=T F C100 T L F=T F C100 T L F=0/E F BN C100 T EOUIV PIPE LEN/FT 09-23-1991 PAGE 3 P -LOSS PSI/FT PRESSURE SUMMARY PSI 10.00 0.4065 PT 34.40 (126) 0.00 PE 0.00 10.00 PF 4.06 10.00 0.00 10.00 5.00 4.00 9.00 10.50 11.00 21.50 8.50 1.00 9.50 0.1069 PT 38.46 (125) PE 0.00 PF 1.07 0.1069 PT 39.53 (124) PE 0.00 PF 0.96 0.0149 PT PE FF PT 0.1330 PT PE PF 40.49 ( 19) 4.55 0.32 45.36 ( 9) 9.07 (115) 0.00 1.26 8.00 0.4673 PT 10.33 (116) 1.00 PE 0.00 9.00 PF 4.21 9.50 0.3075 PT 14.54 (117) 2.00 PE 0.00 11.50 PF 3.54 9.00 0.2834 PT 18.08 (118) 3.00 PE 0.00 12.00 PF 7.40 0.50 0.4667 PT 21.48 (119) 0.00 PE 0.00 0.50 PF 0.23 7.50 0.6898 PT 21.71 (120) 6.00 PE 0.00 13.50 PF 9.31 1.00 0.3995 PT 31.02 (121) 7.00 PE 0.43 8.00 PF 3.20 11.00 14.00 25.00 9.50 1.00 10.50 0.0434 PT 34.65 ( 12) PE 0.00 PF 1.08 PT 35.73 ( 11) 0.2346 PT 16.75 (114) PE 0.00 PF 2'46 SUBMITTAL SERIAL NO:2022H-08 HOMEWOOD SUITES TUKWILA, WA. . FROM TO 09-23-1991 PAGE 4 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 112 1131)0 24.54 1.049 L 7.50 0.9018 PT 19.21 (113) O 47.46 F=T F 4.00 PE 0.00 BN C100 T 11.50 PF 10.37 PT 29.58 (112) 112 111 O 28.40 1.049 L 7.00 0.3488 PT 25.71 (111) F=0/T F 4.00 PE 0.00 BN C100 T 11.00 PF 3.84 11 112D0 47.46 1.610 L 6.50 0.2666 PT 29.55 (112) O 75.85 F=T F 6.00 PE 2.81 NR C100 T 12.50 PF 3.33 10 11D0 182.22 3.260 O 258.07 ' 109 110 O 21.44 L 11.00 0.0827 PT 35.69 ( 11) F=T F 14.00 PE 0.00 NC C100 T 25.00 PF 2.07 PT 37.76 ( 10) 1.049 L 8.00 0.2073 PT 14.65 (110) F=E F 1.00 PE 0.00 BN C100 T 9.00 PF 1.87 108 109D0 22.76 1.049 L 9.50 0.7904 PT 16.52 (109) O 44.19 F=0/E F 1.00 PE 0.00 BN C100 T 10.50 PF 8.30 107 108D0 27.88 1.380 L 7.50 0.5138 PT 24.82 (108) Q 72.07 F=T F 4.00 PE 0.00 BN C100 T 11.50 PF 5.91 13 107 O 72.07 1.610 L 6.50 0.2425 PT 30.73 (107) F=T F 6.00 PE 2.81 NR C100 T 12.50 PF 3.03 PT 36.57 ( 13) ' 105 106 1.049 L 8.50 0.1275 PT 8.66 (106) O 16.48 F=E F 1.00 PE 0.00 BN C100 T 9.50 PF 1.21 104 105D0 16.00 1.049 L 7.50 0.4472 PT 9.87 (105) O 32.48 F=0/E F 1.00 PE 0.00 BN C100 T 8.50 PF 3.80 103 104D0 20.70 1.380 L 9.50 0.2929 PT 13.67 (104) Q 53.19 F=E F 2.00 PE 0.00 BN C100 T 11.50 PF 3.37 102 1031)0 23.11 1.610 L 9.50 0.2695 PT 17.04 (103) Q 76.30 F=T/E F 9.00 PE 0.00 BN C100 T 18.50 PF 4.99 SUBMITTAL SERIAL NO:2022H-08 HOMEWOOD SUITES TUKWILA, WA. FROM TO 09-23-1991 PAGE 5 FLOW DIAM EOUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 101 102D0 24.59 1.610 O 100.88 L 0.50 0.4518 PT 22.03 (102) F=0/T F 6.00 PE 0.00 BN C100 T 6.50 PF 2.94 ' 24 101D0 25.91 1.610 L 7.50 0.6897 PT 24.97 (101) O 126.79 F=T F 6.00 PE 0.00 BN C100 T 13.50 PF 9.31 ' 14 24 2.067 L 1.00 0.2043 PT 34.28 ( 24) O 126.79 F=T F 7.00 PE 0.43 NR 0100 T 8.00 PF 1.63 13 14 3.260 O 126.79 10 13D0 72.07 3.260 O 198.86 9 10D0 258.07 3.260 O 456.94 8 9D0 30.85 3.260 O 487.78 7 8 3.260 O 487.78 6 7 3.260 O 487.78 2 6 O 487.78 1 2 0 1 O 487.78 O 487.78 L 10.50 0.0222 PT 36.34 ( 14) F=0 F 0.00 PE 0.00 NC C100 T 10.50 PF 0.23 L 10.00 0.0511 PT 36.57 ( 13) F=T F 14.00 PE 0.00 NC 0100 T 24.00 PF 1.23 L 32.00 0.2380 PT 37.80 ( 10) F=0 F 0.00 PE 0.00 FM 0100 T 32.00 PF 7.62 L 38.00 0.2685 PT 45.42 ( 9) F=T F 14.00 PE 0.00 FM 0100 T 5^.00 PF 17.96 L 12.50 0.2685 PT 59.38 ( 8) F=T F 14.00 PE 0.00 FM 0100 T 26.50 PF 7.12 L 29.00 0.2685 PT 66.50 ( 7) F=E F 6.00 PE 0.00 FM C100 T 35.00 PF 9.40 3.260 L 16.50 0.2685 PT 75.90 ( 6) F=GV,CV F 16.00 PE 7.14 FR 0100 T 32.50 PF 8.73 4.260 L 1.50 0.0521 PT 91.77 ( 2) F=0 F 0.00 PE 0.65 FR C120 T 1.50 PF 0.08 4.155 L 67.00 0.0442 PT 92.50 ( 1) F=T,2E,26V/DDC F 227.00 PE 1.73 UN 0140 T 294.00 PF 12.99 PRESSURE AVAILABLE AT NODE 0 AT 737.8 GPM ''MAXIMUM PRESSURE UNBALANCE IN LOOPS 0.045 PSI MAXIMUM VELOCITY TN PTPF9 1P_QR Ppq PT107.22 ( 0) 138.8 PSI fir HOMEWOOD 5UITES HYDRAULIC CALCULATIONS (BuIwJ!Jc ND. 8 REVISED) W. 8. `Prut�ection ASSOCIATES nSiO ele sES Fire ._.�-.--- 0 ACCEPTED PTED AS NOTED RESUBMIT QREJECTED 1. 1 21991 ro TUKb"WILA FIRE ;tii'iliaiVII='tVT He se cal: :'_;/b -44u7 End lob 7eGI d a::,ur6,Js for shut - C40 wr or resLoratiorJ apdroval. SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD. TUKWILA, , WA. BLDG. NO. 8 SECOND FLR. UNIT 8 7 SPKR FLOWING FLOW TEST RESULTS STATIC RESIDUAL AT 3157.0 GPM PRESSURE AVAILABLE AT 471.3 GPM SUMMARY OF SPRINKLER OUTFLOWS ACTUAL MINIMUM SPR FLOW FLOW K -FACTOR 215 33.43 17.92 216 31.54 17.92 117 31.35 14.82 218 29.44 29.44 119 31.33 14.82 220 31.79 18.72 121 32.46 14.82 5.60 5.60 5.60 5.60 5.60 5.60 5.60 TOTAL WATER REQUIRED FOR SYSTEM OUTSIDE HOSE STREAMS AT 0 TOTAL WATER REQUIREMENT PRESSURE REQUIRED AT 0 PRESSURE 35.63 31.73 31.34 27.64 31 .30 32.23 33.60 10-07-1991 PAGE 1 141.00 PSI 108.00 PSI 140.02 PSI 221.35 GPM 250.00 GPM 471.35 GPM 84.57 PSI MAXIMUM PRESSURE UNBALANCE IN LOOPS 0.089 PSI MAXIMUM VELOCITY IN PIPES 20.05 FPS ti - SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD. TUKWILA, WA. FROM TO 10-07-1991 PAGE 2 FLOW DIAM EQUIV P --LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 118 218 1,049 L 9.00 0,2661 PT 27.64 (218) Q 29.44 F=T F 5.00 PE 0.00 AO 0120 T 14.00 PF 3.73 PT 31.37 (118) 120 220 1.049 L 1.00 0.3067 PT 32.23 (220) Q 31.79 F=T F 5.00 PE 0.00 AO C120 T 6.00 PF 1.84 PT 34.07 (120) 116 216 1.049 L 1.50 0,3023 PT 31.73 (216) Q 31.54 F=T F 5.00 PE 0.00 AO C120 T 6.50 PF 1.96 PT 33.69 (116) 115 215 1.049 L 1.50 0.3365 PT 35.63 (215) O 33.43 F=T F 5.00 PE 0.00 AO C120 T 6.50 PF 2.19 PT 37.82 (115) 115 31 O 187.92 2.067 L 2.00 0.3019 PT 37.25 ( 31) F=0 F 0.00 PE 0.00 NC C120 T 2.00 PF 0.60 21 115D0 33,43 2.157 L 10.00 0.3320 PT 37.85 (115) Q 221.35 F=0 F 0.00 PE 0.00 NC C120 T 10.00 PF 3.32 PT 41.17 ( 21) 41 119 1.380 L 24.50 0.0732 PT 31.30 (119) Q 30.18 F=0/E F 3.00 PE 0.00 BL2 C120 T 27.50 PF 2.01 42 41 1.380 L 8.00 0.0732 PT 33.31 ( 41) O 30.18 F=0 F 0.00 PE 0.00 CM4 C120 T 8.00 PF 0.59 43 42D0 9.91 1.380 L 5.00 0.1239 PT 33.90 ( 42) O 40.08 F=0 F 0.00 PE 0.00 CM4 C120 T 5.00 PF 0.62 44 43D0 -20.49 1.380 L 8.00 0.0330 PT 34.52 ( 43) Q 19.59 F=0 F 0.00 PE 0,00 CM4 C120 T 8.00 PF 0.26 113 44 1.380 L 5.50 0.0330 PT 34.78 ( 44) Q 19.59 F=0/E F 3.00 PE 0.00 BL2 C120 T 8.50 PF 0.28 SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD. TUKWILA, WA. FROM TO 112 113 34 110 33 34 10-07-1991 PAGE 3 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI Q 19.59 Q 19.59 Q 19.59 Q 19.59 Q 19.59 109 43 108 109 33 108 O 20.49 O 20.49 Q 20.49 1.380 L 8.50 0.0330 PT 35.06 (113) F=0 F 0.00 PE 0.00 BL2 C120 T 8.50 PF 0.28 1.380 L 0.50 0.0330 PT 35.34 (112) F=0 F 0.00 PE 0.00 BL2 C120 T 0.50 PF 0.02 1.380 L 2.00 0.0330 PT 35.36 (111) F=0 F 0.00 PE 0.00 BL2 C120 T 2.00 PF 0.07 1.380 L 25.00 0.0330 PT 35.43 (110) F=E F 3.00 PE 0.00 BL2 C120 T 28.00 PF 0.92 1.610 L 8.00 0.0156 PT 36.35 ( 34) F=0 F 0.00 PE 0.00 CM3 C120 T 8.00 PF 0.12 PT 36.47 ( 33) 1.380 L 6.00 0.0358 PT 34.51 ( 43) F=0/T F 6.00 PE 0.00 BL2 C120 T 12.00 PF 0.43 1.380 L 10.50 0.0358 PT 34.94 (109) f F=0 F 0.00 PE 0.00 BL2 C120 T 10.50 PF 0.38 1.380 L 25.00 0.0358 PT 35.32 (108) F=T F 6.00 PE 0.00 BL2 C120 T 31.00 PF 1.11 15 33D0 19.59 2.067 L 2.50 0.0173 PT 36.43 ( 33) O 40.08 F=0 F 0.00 PE 0.00 CM3 C120 T 2.50 PF 0.04 32 15 O 40.08 Q 42 121 9.91 120 121 Q 22.55 2.067 L 2.50 0.0173 PT 36.47 ( 15) F=0 F 0.00 PE 0.00 CM3 C120 T 2.50 PF 0.04 PT 36.51 ( 32) 1.380 L 25.50 0.0093 PT 33.60 (121) F=0/T F 6.00 PE 0.00 BL2 C120 T 31.50 PF 0.29 PT 33.89 ( 42) 1.380 L 10.50 0.0427 PT 33.60 (121) F=0 F 0.00 PE 0.00 BL2 C120 T 10.50 PF 0.45 SUBMITTAL SERIAL NO:2480HY1 HOMEW00D SUITES 6925 SOUTHCENTER BLVD. TUKWILA, WA. FROM TO 10-07-1991 PAGE 4 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 32 120DQ 31.79 1.380 L 5.50 0.2175 PT 34.05 (120) O 54.35 F=T F 6.00 PE 0.00 BL2 C120 T 11.50 PF 2.50 31 32DQ 40.08 2.067 L 8.00 0.0845 PT 36.55 ( 32) Q 94.43 F=0 F 0.00 PE 0.00 CM3 C120 T 8.00 PF 0.68 PT 37.23 ( 31) 118 119 Q 1.16 1.380 L 2.00 0.0002 PT 31.30 (119) F=0 F 0.00 PE 0.00 BL2 C120 T 2.00 PF 0.00 117 118D0 29.44 1.380 L 0.50 0.0751 PT 31.30 (118) O 30.60 F=0 F 0.00 PE 0.00 BL2 C120 T 0.50 PF 0.04 116 117D0 31.35 1.380 L 8.50 0.2771 PT 31.34 (117) Q 61.95 F=0 F 0.00 PE 0.00 BL2 C120 T 8.50 PF 2.36 31 116D0 31.54 1.380 L 6.00 0.5934 PT 33.70 (116) Q 93.49 F=0 F 0.00 PE 0.00 BL2 C120 T 6.00 PF 3.56 PT 37.26 ( 31) 22 21 Q 73.67 1.380 L 8.00 0.3819 PT 41.15 ( 21) F=0 F 0.00 PE 0.00 CM2 C120 T 8.00 PF 3.06 23 22DQ -29.94 1.380 L 5.00 0.1455 PT 44.21 ( 22) Q 43.74 F=0 F 0.00 PE 0.00 CM2 C120 T 5.00 PF 0.73 24 23DQ -22.78 1.380 Q 20.96 Q 20.96 Q 20.96 14 24 1.380 13 14 13 23 Q 22.78 1.380 L 8.00 0.0373 PT 44.94 ( 23) F=0 F 0.00 PE 0.00 CM2 C120 T 8.00 PF 0.30 L 41.50 0.0373 PT 45.24 ( 24) F=E/E F 6.00 PE 0.00 BL C120 T 47.50 PF 1.77 L 8.00 0.0373 PT 47.01 ( 14) F=0 F 0.00 PE 0.00 CM1 C120 T 8.00 PF 0.30 PT 47.31 ( 13) 1.380 L 41.50 0.0435 PT 44.93 ( 23) F=T/T F 12.00 PE 0.00 BL C120 T 53.50 PF 2.33 SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD. TUKWILA, WA. FROM TO 10-07-1991 PAGE 5 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 12 13DQ 20.96 1.380 L 5.00 0.1455 PT 47.26 ( 13) Q 43.74 F=0 F 0.00 PE 0.00 CM1 0120 T 5.00 PF 0.73 PT 47.99 ( 12) 12 22 Q 29.94 1.380 L 41.50 0.0722 PT 44.21 ( 22) F=T/T F 12.00 PE 0.00 BL C120 T 53.50 PF 3.86 11 12DQ 43.74 1.380 L 8.00 0.3819 PT 48.07 ( 12) O 73.67 F=0 F 0.00 PE 0.00 CM1 C120 T 8.00 PF 3.06 PT 51.13 ( 11) 11 21 2.067 Q 147.67 L 41.50 0.1933 PT 41.15 ( 21) F=T F 10.00 PE 0.00 BL 0120 T 51.50 PF 9.95 7 11D0 73.67 2.635 L 1.50 0.1253 PT 51.10 ( 11) 0 221.35 F=2E F 16.00 PE 0.00 FM C120 T 17.50 PF 2.19 6 7 2.635 L 9.00 0.1253 PT 53,29 ( 7) Q 221.35 F=T F 16.00 PE 3.90 FR C120 T 25.00 PF 3.13 5 6 2.635 L 14.50 0.1253 PT 60.32 ( 6) O 221.35 F=T,2E,GV/CV F 52.00 PE 2.81 FR C120 T 66.50 PF 8.33 4 5 4.124 L 1.50 0.0141 PT 71.46 ( 5) Q 221.35 F=0 F 0.00 PE 0.65 FR C120 T 1.50 PF 0.02 3 4 4.155 L 140.00 0.0103 PT 72.13 ( 4) O 221.35 F=3E F 48.00 PE 1.73 UN C140 T 188.00 PF 1.94 2 3 4.155 L 49.00 0.0103 PT 75.80 ( 3) Q 221.35 F=EE F 6.00 PE 0.00 UN C140 T 55.00 PF 0.57 1 2 6.215 L 35.00 0.0014 PT 76.37 ( 2) Q 221.35 F=EE,GV F 16.00 PE 0.00 UN C140 T 51.00 PF 0.07 0 1 8.325 L 14.00 0.0003 PT 76.44 ( 1) O 221.35 F=T,GV,DDC F %23394.00 PE 0.00 UN C140 T %23408.00 PF 7.02 PRESSURE AVAILABLE AT NODE 0 AT 471.3 GPM MAXIMUM PRESSURE UNBALANCE IN LOOPS 0.089 PSI MAYTMl1M VP"! nri-TY TN PTPPc 'NA (21 FDS PT 83.46 ( 0) 140.0 PSI SUBMITTAL SERIAL NC:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD. TUKWILA, WA. BLDG. NO. 8 SECOND FLR. REMOTE ROOM WITH GREATEST DEMAND 6 SPKR. FLOWING FLOW TEST RESULTS STATIC RESIDUAL AT 3157.0 GPM PRESSURE AVAILABLE AT 442.2 GPM SUMMARY OF SPRINKLER OUTFLOWS ACTUAL MINIMUM SPR FLOW FLOW K -FACTOR 108 34.13 14.82 209 33.10 18.72 110 32.14 14.82 211 29.44 29.44 112 32.05 14.82 213 31.35 29.12 5.60 5.60 5.60 5.60 5.60 5.60 TOTAL WATER REQUIRED FOR SYSTEM OUTSIDE HOSE STREAMS AT 0 TOTAL WATER REQUIREMENT PRESSURE REQUIRED AT 0 PRESSURE 37 .15 34.93 32.94 27.64 32.75 31.34 10-07-1991 PAGE 1 141.00 PSI 108.00 PSI 140.13 PSI 192.21 GPM 250.00 GPM 442.21 GPM 84.90 PSI MAXIMUM PRESSURE UNBALANCE IN LOOPS 0.093 PSI MAXIMUM VELOCITY IN PIPES 18.38 FPS J SUBMITTAL SERIAL N0=2480HY1 HOMEW00D SUITES 6925 SOUTHCENTER BLVD. TUKWILA, WA. FROM TO 10-07-1991 PAGE 2 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 1.049 L 9.50 0.2661 PT 27.64 (211) Q 29.44 F=2T F 10.00 PE 0.00 AO C120 T 19.50 PF 5.19 PT 32.83 (111) 115 31 2.067 L 2.00 0.3147 PT 45.58 ( 31) Q 192.21 F=0 F 0.00 PE 0.00 NC 0120 T 2.00 PF 0.63 21 115 2.067 L 10.00 0.3147 PT 46.21 (115) Q 192.21 F=0 F 0.00 PE 0.00 NC C120 T 10.00 PF 3.15 PT 49.36 ( 21) 113 213 1.049 L 1.50 0.2989 PT 31.34 (213) Q 31.35 F=T F 5.00 PE 0.00 AO C120 T 6.50 PF 1.94 PT 33.28 (113) 109 209 1.049 L 1.00 0.3305 PT 34.93 (209) Q 33.10 F=T F 5.00 PE 0.00 AO C120 T 6.00 PF 1.98 PT 36.91 (109) 113 112 1.380 L 8.50 0.0564 PT 32.75 (112) Q 26.19 F=0 F 0.00 PE 0.00 BL2 C120 T 8.50 PF 0.48 44 113DQ 31.35 1.380 L 5.50 0.2418 PT 33.23 (113) Q 57.54 F=0/E F 3.00 PE 0.00 BL2 C120 T 8.50 PF 2.06 43 44 1.380 L 8.00 0.2418 PT 35.29 ( 44) Q 57.54 F=0 F 0.00 PE 0.00 CM4 C120 T 8.00 PF 1.93 PT 37.22 ( 43) 111 112 1.380 Q 5.86 110 111DQ 29.44 1.380 Q 35.30 34 110DQ 32.14 1.380 Q 67.44 L 0.50 0.0035 PT 32.75 (112) F=0 F 0.00 PE 0.00 BL2 C120 T 0.50 PF 0.00 L 2.00 0.0979 PT 32.75 (111) F=0 F 0.00 PE 0.00 BL2 C120 T 2.00 PF 0.20 L 25.00 0.3243 PT 32.95 (110) F=E F 3.00 PE 0.00 BL2 C120 T 28.00 PF 9.08 SUBMITTAL SERIAL NO 2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD. TUKWILA, WA. FROM TO 33 34 10-07-1991 PAGE 3 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI Q 67.44 43 109 Q 15.91 1.610 L 8.00 0.1531 PT 42.03 ( 34) F=0 F 0.00 PE 0.00 CM3 C120 T 8.00 PF 1.22 PT 43.25 ( 33) 1.380 L 6.00 0.0224 PT 37.00 (109) F=0/T F 6.00 PE 0.00 BL2 C120 T 12.00 PF 0.27 42 43D0 57.54 1.380 L 5.00 0.3798 PT 37.27 ( 43) Q 73.45 F=0 F 0.00 PE 0.00 CM4 C120 T 5.00 PF 1.90 PT 39.17 ( 42) 108 109 Q 17.18 1.380 L 10.50 0.0258 PT 37.00 (109) F=0 F 0.00 PE 0.00 BL2 C120 T 10.50 PF 0.27 33 108DQ 34.13 1.380 Q 51.32 L 25.00 0.1956 PT 37.27 (108) F=T F 6.00 PE 0.00 BL2 C120 T 31.00 PF 6.06 15 33DQ 67.44 2.067 L 2.50 0.1291 PT 43.33 ( 33) Q 118.75 F=0 F 0.00 PE 0.00 CM3 C120 T 2.50 PF 0.32 32 15 2.067 L 2.50 0.1291 PT 43.65 ( 15) Q 118.75 F=0 F 0.00 PE 0.00 CM3 C120 T 2.50 PF 0.32 PT 43.97 ( 32) 121 42 120 121 32 120 Q 33.64 Q 33.64 Q 33.64 31 32DQ 118.75 2.067 Q 152.39 1.380 1.380 1.380 41 42 Q 39.81 L 25.50 0.0896 PT 39.16 ( 42) F=0/T F 6.00 PE 0.00 BL2 C120 T 31.50 PF 2.82 L 10.50 0.0896 PT 41.98 (121) F=0 F 0.00 PE 0.00 BL2 C120 T 10.50 PF 0.94 L 5.50 0.0896 PT 42.92 (120) F=T F 6.00 PE 0.00 BL2 C120 T 11.50 PF 1.03 L 8.00 0.2049 PT 43.95 ( 32) F=0 F 0.00 PE 0.00 CM3 C120 T 8.00 PF 1.64 PT 45.59 ( 31) 1.380 L 8.00 0.1223 PT 39.16 ( 42) F=0 F 0.00 PE 0.00 CM4 C120 T 8.00 PF 0.98 • SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD. TUKWILA, WA. 10-07-1991 PAGE 4 , FROM TO FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 119 41 118 119 117 118 116 117 31 116 O 39.81 Q 39.81 Q 39.81 Q 39.81 O 39.81 22 21 Q 63.92 1.380 L 24.50 0.1223 PT 40.14 ( 41) F=0/E F 3.00 PE 0.00 BL2 C120 T 27.50 PF 3.36 1.380 L 2.00 0.1223 PT 43.50 (119) F=0 F 0.00 PE 0.00 BL2 C120 T 2.00 PF 0.24 1.380 L 0.50 0.1223 PT 43.74 (118) F=0 F 0.00 PE 0.00 BL2 C120 T 0.50 PF 0.06 1.380 L 8.50 0.1223 PT 43.80 (117) F=0 F 0.00 PE 0.00 BL2 C120 T 8.50 PF 1.04 1.380 L 6.00 0.1223 PT 44.84 (116) F=0 F 0.00 PE 0.00 BL2 C120 T 6.00 PF 0.73 PT 45.57 ( 31) 1.380 L 8.00 0.2936 PT 49.37 ( 21) F=0 F 0.00 PE 0.00 CM2 C120 T 8.00 PF 2.35 23 22DQ -25.91 1.380 L 5.00 0.1122 PT 51.72 ( 22) O 38.00 F=0 F 0.00 PE 0.00 CM2 C120 T 5.00 PF 0.56 24 23DQ -20.00 1.380 Q 18.01 O 18.01 O 18.01 14 24 1.380 13 14 13 23 Q 20.00 1.380 L 8.00 0.0282 PT 52.28 ( 23) F=0 F 0.00 PE 0.00 CM2 C120 T 8.00 PF 0.23 L 41.50 0.0282 PT 52.51 ( 24) F=E/E F 6.00 PE 0.00 BL C120 T 47.50 PF 1.34 L 8.00 0.0282 PT 53.85 ( 14) F=0 F 0.00 PE 0.00 CM1 C120 T 8.00 PF 0.23 PT 54.08 ( 13) 1.380 L 41.50 0.0342 PT 52.28 ( 23) F=T/T F 12.00 PE 0.00 BL C120 T 53.50 PF 1.83 12 13D0 18.01 1.380 L 5.00 0.1122 PT 54.11 ( 13) O 38.00 F=0 F 0.00 PE 0.00 CM1 C120 T 5.00 PF 0.56 PT 54.67 ( 12) SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD. TUKWILA, WA. 10-07-1991 PAGE 5 FROM TO FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 12 22 Q 25.91 1.380 L 41.50 0.0553 PT 51.72 ( 22) F=T/T F 12.00 PE 0.00 BL C120 T 53.50 PF 2.96 11 12D0 38.00 1.380 L 8.00 0.2936 PT 54.68 ( 12) Q 63.92 F=0 F 0.00 PE 0.00 CM1 C120 T 8.00 PF 2.35 PT 57.03 ( 11) 11 21 O 128.29 2.067 L 41.50 0.1490 PT 49.37 ( 21) F=T F 10.00 PE 0.00 BL C120 T 51.50 PF 7.67 7 11D0 63.92 2.635 L 1.50 0.0965 PT 57.04 ( 11) Q 192.21 F=2E F 16.00 PE 0.00 FM C120 T 17.50 PF 1.69 6 7 2.635 L 9.00 0.0965 PT 58,73 ( 7) O 192.21 F=T F 16.00 PE 3.90 FR C120 T 25.00 PF 2.41 5 6 2.635 L 14.50 0.0965 PT 65.04 ( 6) Q 192.21 F=T,2E,GV/CV F 52.00 PE 2.81 FR C120 T 66.50 PF 6.42 4 5 4.124 L 1.50 0.0109 PT 74.27 ( 5) Q 192.21 F=0 F 0.00 PE 0.65 FR C120 T 1.50 PF 0.02 3 4 4.155 L 140.00 0.0079 PT 74.94 ( 4) O 192.21 F=3E F 48.00 PE 1.73 UN C140 T 188.00 PF 1.49 2 3 4.155 L 49.00 0.0079 PT 78.16 ( 3) Q 192.21 F=EE F 6.00 PE 0.00 UN C140 T 55.00 PF 0.43 1 2 6.215 L 35.00 0.0011 PT 78.59 ( 2) Q 192.21 F=EE,GV F 16.00 PE 0.00 UN C140 T 51.00 PF 0.06 0 1 8 325 L 14.00 0.0003 PT 78.65 ( 1) Q 192.21 F=T , GV ,DDC F %23394.00 PE 0.00 UN C140 T %23408.00 PF 7.02 PRESSURE AVAILABLE AT NODE 0 AT 442.2 GPM MAXIMUM PRESSURE UNBALANCE IN LOOPS 0.093 PSI MAXIMUM VELOCITY IN PIPES 18.38 FPS PT 85.67 ( 0) 140.1 PSI SUBMITTAL SERIAL NO:2480HY1 HOMEW00D SUITES 6925 SOUTHCENTER BLVD. TUKWILA, WA. BLDG. NO 8 FIRST FLR. REMOTE ROOM WITH GREATEST DEMAND 6 SPKR. FLOWING FLOW TEST RESULTS STATIC RESIDUAL AT 3157.0 GPM PRESSURE AVAILABLE AT 436.0 GPM SUMMARY OF SPRINKLER OUTFLOWS ACTUAL MINIMUM SPR FLOW FLOW K -FACTOR 101 31.96 14.82 202 31.08 18.72 103 31.52 14.82 204 29.44 29.44 105 31.37 14.82 206 30.59 29.12 5 .60 5.60 5.60 5.60 5.60 5.60 TOTAL WATER REQUIRED FOR SYSTEM OUTSIDE HOSE STREAMS AT 0 TOTAL WATER REQUIREMENT PRESSURE REQUIRED AT 0 PRESSURE 32.58 30.80 31.68 27.64 31.38 29.83 10-07-1991 PAGE 1 141.00 PSI 108.00 PSI 140.15 PSI 185.96 GPM 250.00 GPM 435.96 GPM 91.67 PSI MAXIMUM PRESSURE UNBALANCE IN LOOPS 0.089 PSI MAXIMUM VELOCITY IN PIPES 18.01 FPS SUBMITTAL SERIAL NO:2480HY1 HOMEW00D SUITES 6925 SOUTHCENTER BLVD. TUKWILA, WA. FROM TO 10-07-1991 PAGE 2 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 104 204 1.049 L 9.50 0.2661 PT 27.64 (204) Q 29.44 F=T F 5.00 PE 0.00 AO C120 T 14.50 PF 3.86 PT 31.50 (104) 115 31 2.067 L 2.00 0.2961 PT 54.17 ( 31) Q 185.96 F=0 F 0.00 PE 0.00 NC C120 T 2.00 PF 0.59 21 115 2.067 L 10.00 0.2961 PT 54.76 (115) Q 185.96 F=0 F 0.00 PE 0.00 NC C120 T 10.00 PF 2.96 PT 57.72 ( 21) 106 206 1.049 L 1.50 0.2856 PT 29.83 (206) Q 30.59 F=T F 5.00 PE 0.00 AO C120 T 6.50 PF 1.86 PT 31.69 (106) 102 202 1.049 L 0.50 0.2941 PT 30.80 (202) Q 31.08 F=T F 5.00 PE 0.00 AO C120 T 5.50 PF 1.62 PT 32.42 (102) 15 50 2.067 L 10.00 0.2961 PT 47.09 ( SO) Q 185.96 F=T/T F 20.00 PE -4.33 NC C120 T 30.00 PF 8.88 PT 51.64 ( 15) 106 105 1.380 L 8.50 0.0255 PT 31.38 (105) Q 17.06 F=0 F 0.00 PE 0.00 BL3 C120 T 8.50 PF 0.22 29 106DQ 30.59 1.380 L 5.50 0.1705 PT 31.60 (106) Q 47.64 F=0/E F 3.00 PE 0.00 8L3 C120 T 8.50 PF 1.45 28 29 1.380 L 8.00 0.1705 PT 33.05 ( 29) Q 47.64 F=0 F 0.00 PE 0.00 CM6 C120 T 8.00 PF 1.36 PT 34.41 ( 28) 104 105 1.380 L 0.50 0.0184 PT 31.38 (105) Q 14.31 F=0 F 0.00 PE 0.00 BL3 C120 T 0.50 PF 0.01 103 104DQ 29.44 1.380 L 2.00 0.1457 PT 31.39 (104) Q 43.75 F=0 F 0.00 PE 0.00 8L3 C120 T 2.00 PF 0.29 SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD. TUKWILA, WA. FROM TO 10-07-1991 PAGE 3 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 19 103D0 31.52 1.380 Q 75.27 18 19 O 75.27 28 102 O 24.04 L 25.00 0.3974 PT 31.68 (103) F=E F 3.00 PE 0.00 BL3 C120 T 28.00 PF 11.13 1.380 L 8.00 0.3974 PT 42.81 ( 19) F=0 F 0.00 PE 0.00 CM5 C120 T 8.00 PF 3.18 PT 45.99 ( 18) 1.049 L 6.00 0.1828 PT 32.53 (102) F=0/T F 5.00 PE 0.00 BL3 C120 T 11.00 PF 2.01 27 28DQ 47.64 1.380 L 5.00 0.3630 PT 34.54 ( 28) Q 71.68 F=0 F 0.00 PE 0.00 CM6 C120 T 5.00 PF 1.81 PT 36.35 ( 27) 101 102 Q 7.04 1.049 L 10.50 0.0189 PT 32.53 (102) F=0 F 0.00 PE 0.00 BL3 C120 T 10.50 PF 0.20 18 101D0 31.96 1.049 Q 39.00 L 25.00 0.4478 PT 32.73 (101) F=T F 5.00 PE 0.00 BL3 C120 T 30.00 PF 13.43 50 18D0 75.27 1.610 L 2.50 0.4061 PT 46.16 ( 18) Q 114.28 F=0 F 0.00 PE 0.00 CM5 C120 T 2.50 PF 1.02 PT 47.18 ( 50) 33 15 O 18.52 2.067 L 2.50 0.0041 PT 51.63 ( 15) F=0 F 0.00 PE 0.00 CM3 C120 T 2.50 PF 0.01 34 33D0 -9.32 1.610 L 8.00 0.0038 PT 51.64 ( 33) Q 9.20 F=0 F 0.00 PE 0.00 CM3 C120 T 8.00 PF 0.03 110 34 111 110 112 111 O 9.20 Q 9.20 Q 9.20 1.380 L 25.00 0.0081 PT 51.67 ( 34) F=E F 3.00 PE 0.00 BL2 C120 T 28.00 PF 0.23 1.380 L 2.00 0.0081 PT 51.90 (110) F=0 F 0.00 PE 0.00 BL2 C120 T 2.00 PF 0.02 1.380 L 0.50 0.0081 PT 51.92 (111) F=0 F 0.00 PE 0.00 BL2 C120 T 0.50 PF 0.00 SUBMITTAL SERIAL NO:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD. TUKWILA, WA. FROM TO 10-07-1991 PAG` 4 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 113 112 1.380 L 8.50 0.0081 PT 51.92 (112) Q 9.20 F=0 F 0.00 PE 0.00 BL2 C120 T 8.50 PF 0.07 44 113 • 9.20 1.380 L 5.50 0.0081 PT 51,99 (113) F=0/E F 3.00 PE 0.00 BL2 C120 T 8.50 PF 0,07 43 44 1.380 L 8.00 0.0081 PT 52.06 ( 44) Q 9.20 F=0 F 0.00 PE 0.00 CM4 C120 T 8.00 PF 0.06 PT 52.12 ( 43) 108 33 1.380 L 25.00 0.0083 PT 51.68 Q 9.32 F=T F 6.00 PE 0.00 BL2 C120 T 31.00 PF 0.26 109 108 43 109 Q 9.32 Q 9.32 33) 1.380 L 10.50 0.0083 PT 51.94 (108) F=0 F 0.00 PE 0.00 BL2 C120 T 10.50 PF 0.09 1.380 L 6.00 0.0083 PT 52.03 (109) F=0/T F 6.00 PE 0.00 BL2 C120 T 12.00 PF 0.10 42 43DQ 9.20 1.380 L 5.00 0.0297 PT 52.13 ( 43) O 18.52 F=0 F 0.00 PE 0.00 CM4 C120 T 5.00 PF 0.15 PT 52.28 ( 42) 32 15 2.067 L 2.50 0.2438 PT 51.63 ( 15) Q 167.44 F=0 F 0.00 PE 0.00 CM3 C120 T 2.50 PF 0.61 120 32DQ -165.41 1.380 L 5.50 0.0005 PT 52.24 ( 32) O 2.03 F=T F 6.00 PE 0.00 BL2 C120 T 11,50 PF 0.01 121 120 1.380 L 10.50 0.0005 PT 52.25 (120) O 2.03 F=0 F 0.00 PE 0.00 BL2 C120 T 10.50 PF 0.01 42 121 Q 2.03 1.380 L 25.50 0.0005 PT 52.26 (121) F=0/T F 6.00 PE 0.00 BL2 C120 T 31.50 PF 0.02 41 42D0 18.52 1.380 L 8.00 0.0360 PT 52.28 ( 42) O 20.55 F=0 F 0.00 PE 0.00 CM4 C120 T 8.00 PF 0.29 SUBMITTAL SERIAL NO:2480HY1 HOMEW00D SUITES 6925 SOUTHCENTER BLVD. TUKWILA, WA. FROM TO 119 41 118 119 117 118 116 117 31 116 10-07-1991 PAGE 5 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI Q 20.55 Q 20.55 Q 20.55 Q 20.55 Q 20.55 17 27 Q 25.29 26 27 16 26 Q 46.39 Q 46.39 1.380 1.380 1.380 1.380 1.380 1.049 1.380 1.380 L 24.50 0.0360 PT 52.57 ( 41) F=0/E F 3.00 PE 0.00 BL2 C120 T 27.50 PF 0.99 L 2.00 0.0360 PT 53.56 (119) F=0 F 0.00 PE 0.00 BL2 C120 T 2.00 PF 0.07 L 0.50 0.0360 PT 53.63 (118) F=0 F 0.00 PE 0.00 BL2 C120 T 0.50 PF 0.02 L 8.50 0.0360 PT 53.65 (117) F=0 F 0.00 PE 0.00 BL2 C120 T 8.50 PF 0.31 L 6.00 0.0360 PT 53.96 (116) F=0 F 0.00 PE 0.00 BL2 C120 T 6.00 PF 0.22 PT 54.18 ( 31) L F=T/T F BL3 C120 T 41.50 0.2009 PT 36.31 10.00 PE 0.00 51.50 PF 10.35 PT 46.66 27) 17) L 8.00 0.1623 PT 36.31 ( 27) F=0 F 0.00 PE 0.00 CM6 C120 T 8.00 PF 1.30 L 41.50 0.1623 PT 37.61 ( 26) F=E/E F 6.00 PE 0.00 8L3 C120 T 47.50 PF 7.71 17 16 1.380 L 8.00 0.1623 PT 45.32 ( 16) Q 46.39 F=0 F 0.00 PE 0.00 CM5 C120 T 8.00 PF 1.30 50 17DQ 25.29 1.610 L 2.50 0.1714 PT 46.62 ( 17) Q 71.68 F=0 F 0.00 PE 0.00 CM5 C120 T 2.50 PF 0.43 PT 47.05 ( 50) 22 21 Q 61.91 1.380 L 8.00 0.2768 PT 57.71 ( 21) F=0 F 0.00 PE 0.00 CM2 C120 T 8.00 PF 2.21 23 22DQ -25.16 1.380 L 5.00 0.1055 PT 59.92 ( 22) Q 36.75 F=0 F 0.00 PE 0.00 CM2 C120 T 5.00 PF 0.53 SUBMITTAL SERIAL NO 2480HY1 HOMEW00D SUITES 6925 SOUTHCENTER BLVD. TUKWILA, WA. FROM TO 10-07-1991 PAGE 6 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI 24 23DQ -19.11 1.380 Q 17.64 Q 17.64 Q 17.64 14 24 1.380 13 14 13 23 Q 19.11 1.380 L 8.00 0.0271 PT 60.45 ( 23) F=0 F 0.00 PE 0.00 CM2 C120 T 8.00 PF 0.22 L 41.50 0.0271 PT 60.67 ( 24 F=E/E F 6.00 PE 0.00 BL C120 T 47.50 PF 1.29 L 8.00 0.0271 PT 61.96 ( 14) F=0 F 0.00 PE 0.00 CM1 C120 T 8.00 PF 0.22 PT 62.18 ( 13) 1.380 L 41.50 0.0315 PT 60.45 ( 23 F=T/T F 12.00 PE 0.00 BL C120 T 53.50 PF 1.69 12 13D0 17.64 1.380 L 5.00 0.1055 PT 62.14 ( 13) Q 36.75 F=0 F 0.00 PE 0.00 CM1 C120 T 5.00 PF 0.53 PT 62.67 ( 12) 12 22 O 25.16 1.380 L 41.50 0.0523 PT 59.93 ( 22) F=T/T F 12.00 PE 0.00 BL C120 T 53.50 PF 2.80 11 12D0 36.75 1.380 L 8.00 0.2768 PT 62.73 ( 12) Q 61.91 F=0 F 0.00 PE 0.00 CM1 C120 T 8.00 PF 2.21 PT 64.94 ( 11) 11 21 2.067 O 124,05 L 41.50 0.1400 PT 57.71 ( 21) F=T F 10.00 PE 0.00 BL C120 T 51.50 PF 7.21 PT 64.92 ( 11) 31 32 2.067 L 8.00 0.2384 PT 52.25 ( 32) O 165.41 F=0 F 0.00 PE 0.00 CM3 C120 T 8.00 PF 1.91 PT 54.16 ( 31) 7 11 6 7 Q 185.96 Q 185.96 2.635 L 1.50 0.0908 PT 64.94 ( 11) F=2E F 16.00 PE 0.00 FM C120 T 17.50 PF 1.59 2.635 L 9.00 0.0908 PT 66.53 ( 7) F=T F 16.00 PE 3.90 FR C120 T 25.00 PF 2.27 SUBMITTAL SERIAL N0:2480HY1 HOMEWOOD SUITES 6925 SOUTHCENTER BLVD. TUKWILA, WA. FROM TO 5 6 10-07-1991 PAGE 7 FLOW DIAM EQUIV P -LOSS PRESSURE GPM IN PIPE PSI/FT SUMMARY LEN/FT PSI O 185.96 4 5 4.124 L 1.50 0.0102 PT 81.55 ( 5) Q 185.96 F=0 F 0.00 PE 0.65 FR C120 T 1.50 PF 0.02 2.635 L 14.50 0.0908 PT 72.70 ( 6) F=T,2E,GV/CV F 52.00 PE 2.81 FR C120 T 66.50 PF 6.04 3 4 O 185.96 2 3 O 185.96 1 2 O 185.96 0 1 Q 185.96 4.155 L 140.00 0.0074 PT 82.22 ( 4) F=3E F 48.00 PE 1.73 UN C140 T 188.00 PF 1.39 4.155 L 49.00 0.0074 PT 85.34 ( 3) F=EE F 6.00 PE 0.00 UN C140 T 55.00 PF 0.41 6.215 L 35.00 0.0010 PT 85.75 ( 2) F=EE,GV F 16.00 PE 0.00 UN C140 T 51.00 PF 0.05 8.325 L 14.00 0.0003 PT 85.80 ( 1) F=T,GV,DDC F %23394.00 PE 0.00 UN C140 T %23408.00 PF 7.02 PRESSURE AVAILABLE AT NODE 0 AT 436.0 GPM MAXIMUM PRESSURE UNBALANCE IN LOOPS 0.089 PSI MAXIMUM VELOCITY IN PIPES 18.01 FPS PT 92.82 ( 0) 140.2 PSI c_DU 55 sc- GIv iJ W B LEHNER & ASSOCIATES FIRE PROTECTION ENGINEERS 307 N. Olympic Ave., *208 Arlington, WA 98223 (206) 435-2549 FAX: 435-6424 TO: Fred Bowman 9924 NE 200th Bothell, WA 98011 RE: Homewood Suites Tukwila, WA Dear Fred, OCTOBER 12, 1991 `1111-V!!J\ 1I"~ DEPARTMENT 9) 5 3 . J.A.; �:;:..�• ✓.� tie �-.a..�:a We have reviewed the fire sprinkler system shop drawings No. SP -2 thru SP -6 of 6, submitted by you 10/11/91. They are ACCEPTED AS NOTED, (notes on second sheet and attached to plans): Positions: A. Sprinkler spacing: 1. Ordinary hazard requires 130 and 15 ft. maximum spacing (4-2.2.3) 2. Sprinklers may be positioned in accordance with their listing and occupancy (4-1.1.1. (d) exception no. 2) and (4-1.1.3). 3. Tukwila code requires ordinary hazard - Groupl, which equates to .16 over largest room in this case. 4. Occupancy is R-1 for which residential sprinklers are recommended because of their "lifesaving" spray patterns and fast sensitivity. Conclusion: Residential sprinklers may be installed, recognizing their extended coverage listings. However, to satisfy the Tukwila code, a density of .16 must be achieved also. This results in 1/2" residential sprinklers generally. B. Corridor Sprinklers: 1. Residential sprinklers are recommended and used in the hotel rooms. It is allowed to use residential sprinklers in adjoining corridors (3-11.2.9.1 and 2 / formal interpretation attached). 2. Resident sprinklers are recommended for their superior fast response and water distribution characteristics. (A-3-11.2.9.1). 3. Residential sprinklers are allowed in corridors with ceilings less than 10 ft. high (NFPA-13R, 2-4.5.6 Exception 1). Conclusion: I recommend the installation of residential sprinklers in those heated corridors less than 10 ft. high serving the hotel rooms. Plans are acceptable as noted for pipe fabrication. installation may be performed by some fitters relatively inexperienced with dry systems. Because of that and the omission of most pipe hangers and sway bracing, I believe a corrected set of drawings should be used for contruction. These should be logged thru the city's permit process to insure revised plans are being used. Should you have any questions please call at your convenience. Sincerely, W. B. Lehner, P.E. Fire Protection Engineer W 8 LEHNER & ASSOCIATES WBLlaw c.c. Marshal Nick Olivas 91902-R4.WPS 4 Subject: Review of Sprinkler Drawings prepared by Fred Bowman for Homewood Suites, 6925 Southcenter Blvd., Tukwila, WA. Notes: All references in parenthesis are to NFPA-13, exceptions noted. SP -1: Approved as previously noted. SP -2 thru SP -5: Approval is contingent on the following items being properly addressed: 1. The supply side of sprinkler transfer lines that directly serve a Hose Station must be 2", minimum (3-3.7). 2. The supply piping traversing cold breezeways shall be protected from freezing with supervised heat trace and 1" minimum of pipe insulation (3.5.1.2). A formal interpretation exists, denying the validity of heat tracing branch lines 3. Sprinklers served by wet piping traversing cold areas is unacceptable. It must be replaced by dry sidewalls or served by the dry system; but not the wet system as drawn. 4. it is recommended to inspect draft stops to confirm they are installed as shown in order to maintain the integrity of the sprinkler spacing and coverage. 5. Hose station omissions for Buildings 8, E5 and C5 require written approval by the Tukwila Fire Marshal (review has been conducted per verbal approval). -- 6. One hundred feet of lined hose for the stations of building B require written approval by the Tukwila Fire Marshal (review has been conducted per verbal approval). 7 Adjustable (fog type) plastic or brass shut off nozzles and shut. off valves shall be provided with the hose station assemblies. 8. Sprinkler protection is required at the top and at the bottom of the elevator shaft, complete with shut off and drain valves, heat detectors, elevator power shunt trip and associated controls per the state elevator code. Machine room is not indicated, but it must be protected similar to the "top -of -shaft" 9. Electrical Rooms require sprinklers. 10. Sway Bracing is not shown on drawings SP -2 & 3 and for wet piping on SP -5 & 6. 11. Hangers are not shown except for dry attic mains. 12. The hydraulic information block of SP -5 should be revised to reflect the revised hydraulic calculations: ie., base of riser rate and pressure. • 13. Future Hydraulic Calculations for similar construction with attic dry systems and interior hose stations on a wet systems should add the hose at the first common connection point, although in this case the effect is insignificant. 14. Future Hydraulic Calculations Summary Sheet should reflect the Design Area of Application. 15. it is recommended that the 1st, 2nd, and 3rd levels of piping be interconnected at the remote end of the systems, particularly for Building B (2), for greater system reliability. 16. Comment withdrawn. 17. Auxiliary drain valves required. 18. Sheets SP -3 thru SP -5 should note the applicability of the General Notes of Sheet SP - 2. lg. Sprinkler is over spaced. 20. Add the contractor's Fire Sprinkler License * to SP -1. 21. "Seal of Competency" should be dated. 22. Dry pendent sprinklers must be continuous (single piece) from tee outlet in dry arrnover. 23. Two names for each building is confusing. 24. The location and elevation of water supply should be indicated on the site plan. 25. Riser diagrams inadequately detail switch requirements. Flow switch should be 2 PDT, flow alarm pressure switch should be 2PDT (switch not indicated on SP -5) and low air pressure trouble switch is not shown (should be SPDT). 26. A note describing dry pipe slope requirements or appropriate elevations should appear with each plan of dry (attic) piping. W B LEHNER & ASSOCIATES FIRE PROTECTION ENGINEERS 307 N. Olympic Ave., 11208 Arlington, WA 98223 (206) 435-2549 FAX: 435-6424 TO: Fred Bowman 9942 NE 200th Bothell, WA 98011 RE: Homewood Suites Tukwila, WA Dear Fred, November 5, 1991 We have reviewed the fire sprinkler system shop drawings No. SP -7 and 5P-8 submitted by you. They are ACCEPTED AS NOTED, which follow and are attached to plans: 1. Type and locations of hangers omitted. 2. Sprinklers more than 3 feet vertically from peak. 3. It appears that more than 5 gal. is trapped in mezzanine piping and a two valve drain in accordance with NFPA 13, 3-6.3.3.2 is needed. 4. Provide wiring instructions for local alarm bell, pressure switch, and describe central station hookup. Include tamper switch and low air pressure trouble alarm circuits. 5. Type of drain and access to valve (s) is not noted. 6. Inspection test not provided. 7. Seismic brace omitted. 8. Provide hose shutoff valve and tamper. 9. Pitch all pipe 1/2" in 10'-0" to drain back to dry valve or approved auxiliary drain. Should you have any questions please call at your convenience. Sincerely, W. B. Lehner W B LEHNER & ASSOCIATES WBL1aw c.c. Marshal Nick Olivas 91902-R5.PS W B LEHNER COMMENTS 1. Type and locations of hangers omitted. 2. Sprinklers more than 3 feet vertically from peak. 3. It appears that more than 5 gal. i s• trapped in mezzanine piping and a two valve drain in accordance with NFPA 13, 3-6.3.3.2 is needed. 4. Provide wiring instructions for local alarm bell, pressure switch, and describe central station hookup. Include tamper switch and low air pressure trouble alarm circuits. 5. Type of drain and access to valve (s) is not noted. 6. Inspection test not provided. 7. Seismic brace omitted. 6. Provide hose shutoff valve and tamper. 9. Pitch all pipe 1/2" in 10'-O" to drain back to dry valve or approved auxiliary drain. •"/2 W B LEHNER COMMENTS 1. Type and locations of hangers omitted. 2. Sprinklers more than 3 feet vertically from peak. 3. It appears that more than 5 gal. is. trapped in mezzanine piping and a two valve drain in accordance with NFPA 13, 3-6.3.3.2 is needed. 4. Provide wiring instructions for local alarm bell, pressure switch, and describe central station hookup. Include tamper switch and low air pressure trouble alarm circuits. 5. Type of drain and access to valve (s) is not rioted. 6. Inspection test not provided. 7. Seismic brace omitted. 6. Provide hose shutoff valve and tamper. 9. Pitch all pipe 1/2" in 10'-O" to drain back to dry valve or approved auxiliary drain. ?4,e c I:" EE' /-8"-GV I-Ic" Gv ;-1278' RED(/CER COaC. BLOCK. . OTS or -6-12..e-v>0144------L.-&140 (-t=(P.) STA 3+9 4 MAINTAIN MI BETWI EN WA AT CR• SIN OF 18' R b A ( TYP. L SEW 8C 221.1 P-0 • CAP ED ---•5ea..t,,,':..+wzsittts lstak.i•rirNw.. .ViwetalPlikiw.wwtt,iWows/wrrY •Yr r**** m...�/•monta _ � 168.53' PO LF 8" 0 PVC SEE SI -1T C-5 OF FOR CONTINUATION STA 0+20 8' LT. :12X8"TEE 1278" REDUCER 8" GV CONC. BL O CK. I7LF 12" 0 0.1. 12"0 D.1. 12"x8"T...E(MJxF_I 29LF 8'0 D,1. 8" 45' BEND (MJ.MJ1 W/ CONC. BLOCKING • \ 0L.52 4 1 �� 4-"C L 52 p,1. 7.r1-\ c131. e.c�,i6 u�v( 5�) e�7 C 51 A, • ,=j Awdde uera.e.rers9a Ants Jo} Ssalppe 'r--. Eat .114301.t. V a 11.E Vi Nat STA 4 6.5 STA 6+98, 8' RT. 8" 90' BEND W1.1xMJ1 W/ CONC. BLOCKING STA 6+85 STA 0+48 8' L.T. 8"x6"TEE (MJx'L- 6" GATE VALVE( M.J.FL1 6" F.1 -L ASSY W/ CONC. BLOCKING 1. STATE APPROVED DOUBLE-CHECK VALVE ASSEMBLY, COMPLETE WITH O.S.&Y GATE VALVES AND BRASS OR COPPER BY-PASS. 2. STATE APPROVED 3/4" DOUBLE-CHECK VALVE ASSEMBLY. 3. SHUT OFF VALVES. (3/4" GLOBE) 4. 5/8" METER WITH READING AS REQUIRED BY CITY OF TUKWILA. 5. UNI -FLANGE WITH SETSCREWS. 6. ACCESS LADDER. 7. 1 -CONCRETE VAULT PER CITY OF TUKWILA REQUIREMENTS 8. WATER TIGHT GROUT AT PENETRATIONS. 9. DRAIN WITH SLOPE TO DAYLIGHT WHERE APPLICABLE. - 10.. TWO ADJUSTABLE PIPE STANCHIONS OR CONCRETE SUPPORT PADS. 11. SWING CHECK VALVE FOR PUMPER CONNECTION. 12. 4" DUCTILE IRON CLASS 52 TO FIRE DEPARTMENT CONNECTION. 13. VAULT ACCESS WITH VALVE ASSEMBLY CENTERED IN VAULT 14. CL 52 D.I. M.J. WITH RETAINER GLANDS. 15. POST INDICATOR VALVE. 8" SS LIB S • OX /4/ 6 FB"0 D 3H -C1 8" SS STUB -!r�• MIN SS C.O. RIM EL. • 25.90 I.E.. 19.67 t M• STA 5.00.5, 10' RT. ! W/ CONC. BLOCKING • 4" TKR. STUB SS D.0. L. • 5.7,0 {• I.E.. 0.7.7 SCALE: / I / • = 20' NOTE: ALL CONSTRUCTION SHALL BE IN ACCORDANCE WITH "STANDARD SPECIFICATIONS FOR MUNICIPAL PUBLIC WORKS CONSTRUCTION" PREPARED BY WASHINGTON CHAPTER APWA, CURRENT EDITION, AND BY THE CITY OF TUKWILA STANDARDS AND SPECIFICATIONS. I - NO TE FINAL LOCATION AND ALIG MENET_ , OF S.SEWER SERV/CE CONNECTJOICW1i1 _ • PROVIDED BY OTHERS 44- z-c� c. j tri I 1 lef// 1,0.5> STA 6+14 14' RT. 8" x 6" TEE (MJ.FLJ 6" GATE VALVE (MJJFLJ 6" F.14 ASSY W/ CONC. BLOCKING FLOW - PLAN SPRINKLE VAULT PETAI NOTE: ALL UNDERGROUND FIRE PROTECTION WATER MAINS TO BE INSTALLED PER NFPA 24 AND CITY OF TUKWILA GENERAL NOTES: 1. OCCUPANCY TYPE IS R-1 WITH 1 -HR. TYPE - 5 CONSTRUCTION 2. MINIMUM DEPTH OF BURY IS 4=0 (TYP) 3. SYSTEM CONTROL VALVE TO BE LOCATED IN- SIDE BUILDING ON RISER ASSEMBLY AND ACCESSIBLE FROM OUTSIDE. 4. WATER FLOW FOR SITE: STATIC: 141 P.S.I. RESIDUAL: 108 P.S.I. W/ 3157 G.P.M. a__ _30 JNITS I L01717 -9L9 V1IMm. 3O A1I0 •Aa fire -- `/31va lu3WJ2dep sial }o ani;eluesaadeJ a /Cq uo!}oadsui -plat} ollcafgns s! aoueldeoo8 Ieu13 'S2u!MP.lp paS!A8J }o Ielllwgnsaa e a.Ilnbaa IIIM pue a. u. caooe sly; pion IIIA\ alep slL�l Jai}e SfU!M Jp asaijl Cl sUclslr.eJ JO SUOL alap•'sucll!ppV 'Idea OJI3 8llm1nl }o 40 eql i q peldaooe put pamalna.I uaeq anal Olaaaq pax!}}e s2ulme.ip aLll 2131131 GJ 3VL1V 3H1 Lad C8NI031'71NSV •S!N L":V 03 1flOH1IM . - STA 6+07 110' LT. 8" x 6" TEE (MJxFL1 6" GATE VALVE (MJxFLJ 6" F.h{ • ASSY W/ CONC.BLOCKING rss co. RiM EL. = 26.50 i.E. - 20.88 STA 2+87 8' LT. 8" x 6" TEE IMJxFLJ 6" GATE VALVE (MJKFLJ 6" F.1-1 ASSY W/ CONC. BLOCKING • 24/ 6" GATE VI t 1 SS C.O. 6" F.I-1 A95Yt j ' M -Et . 26.50 W/ COI�G. Bf 0 K1l�G r i l.C-. • -22.88 94 STA 2+92, 10' RT. SSM -1..2 RIM EL. • 25.62 I.E. . 19.56 =_nvbonmont 22.5LF 8" 0 D.1. SS C.O. RIM EL. = 26.50 LE.. 19.80 200LF 8- m PVC A 4, 28' LT 8'22 I/2' BE:N0 IMJxM.A W C C BLL.0KING ` \\.\ STA 5+00, 10' LT. STA 6+12, 7' RT. 8" 22 1/2' BEND (MJ.MJ1 W/ CONC. BLOCKING STA 3+12, 7' RT. 8" 90' BEND (MJxMJI W/ CONC. BLOCKING .25. 1/2 ONC. LT. ND 1MJJMJJ CK'^!G 2OLF 8 •• 1 1 • 4 EDGE OF RIVE Green fTh,I r r• REVISIONS NO.I DESCRIPTION/DATE BY i PR OTECT/ ON Diz 0 LI Li 1. JOB NO. DESIGNED DRAWN P. E301444AN COMP. CHECKED DATE - 5/ 2/9/ -OF SHEETS This system as shown on ..DFP%TT company print no. for ... HD•M woof S at O t" Z contract no (L/min) per sq ft of floor area over a maximum area of / 95-° sq ft (m2) when supplied with water at a rate ofd 40 gpm (L/min) at 0 psi (bars) at the base of the riser. Hose stream allowance of 0 gpm (L/min) is included in the above. TH15 .SHOWS 3'�O rue ONLY SCALE:1/8"- Q?d Nuc 2 eq 11 ti",.54 � s GENERAL NOTES: 1. Occupancy type is R-1 with 1 -Hr type 5 construction. 2. Tenant separation and exterior walls 1 -Hr fire rated. 3. Corridor separation and interior partition wall in 3 story building 1 -Hr fire rated. SPRINKLER SYSTEM DESIGN CRITERIA 1. Design based on ordinary hazard Group 1. 2. All piping ; (wet and dry systems) to be schedule 40 steel for sizes 1".-;_2" and schedule 10 ,steel for sizes 2 1/2" - 4". 3. Piping on floors below attic level to be_.$AW pipe and fittings - As ,JoTEP A0ovE . L''? 4. Pipe sizing for wet systens based on hydrau'lic calculations c cct.4-Lw`` per 2-+.2.3- of NFPA 13°1989 edition. 5. Dry systems calculated to provide .16 GPM/sq. ft. over 1950 sq. ft. 6. All materials and equipment to be listed for use'in sprinkler systems. 7. All pipe hangers, earthquake bracing and fasteners to be per code requirements. TD A'T1 G PRY sYSTir/ut PRY 1Z1seR.. 1• • • BY /e -/-q/ . - I .--- .. _ -- _ _ _ _ I _ ,,..._ /0-T" 4, 4.-G`IL ti. ♦ 1i rb � I��=Z 1. Architects (206) 883-1200 2661 Bel -Red Rood Sults #202 B.II"vu• /o=7" /3 IL • /1. 6%" _� �.. r� /o -7r I i. • 8 6i'" /4.. y • (p-l�• tD=� HOMEWOOD SUITES HOTEL Franchised by Holiday Corporation to =8 13-4" 10-71" 8 `Si." Developer • • * e926 B. CENTER BLVD. L:_Ii JOB NUMBER: 9434 11- / r 1� Ii1 /�• Orli• Pn t7 00v iy91 I�- ----------------- 1. �\ Z w 0 0(c • (I� % On w).H.:". QZ 0 ox �; 2 mw ¢W 0 1_ Z0_1.e Itib- ,, 5 Q k 4 1. Date ?...../4-9/ = Drawn F-1_13 • . 8A7T/ • p i,viA/ k-:. 5P -Z If 41 3 -0 4- ' ' ' " ` -�-T --r-.�-- 1 10-7 • -� ` N 4 4 . 10 -7 _ ^--8- 4, "J LL - t o - � " i 3 - 8 /S " t o 1 Q O m 0 0 ®4 O o --� I ; 4' /o -a- �, /f -o" I l to=o" 8-ro" lr=o" e - r r r l ) 1 if -v" A, t�?o' log=( to=v" k 14=v` 7 el / 0 7 l 3- B f / a'- g i� r �- �" I i` / -84. /S- Z? # -6 '\ I ( 2" 1/3-8i T • 'SLK . 4 • • �l t n-7 ♦ --1 3 ♦ /0-7 --r ♦ - 8-84 4-o' 4-° D„ Z l0 7 B-8 i- {10-7 • t` t 1 - /� / ,. /{. /4 `t /f ri l� 1/i i� ILI 1 IL - /4 - r4,- t /i- t !f `( _1Q t Z.,U' 4-o" z=% • j Gv=G" _ z=// 6 I N 1 7 J-i'P I Trp Ti -ft.: r i� ill - __- it _ (._ �tlz Half F 1� ( L I �' 1 1 14- A � r4, t� !�' -• : `1 _ !_4- 4 • I - ! • Q o o* to -o' o t4 o -o" 11 11 , 1 t2 -o" 0 r) 0 1 1, (' ©0 o Jo -o j, 0 -o U 1 1 1 I Q 1,l C+}- !P-�O 11 11 I• /oiR ` 0 0 , Jv-o d o o® lf=o I l I L -7 01 l� i !�-o` Irl -� ,if- 2 Z AP i 13 s • j j } © /� r /i -__ iI • 1 » • i i / / L • /4 • • /i. -- .. ._ I /� l� — 1 -- .. e • 1 1& • • 1 N 1 IL /�-Q ':, - - r--* TH15 .SHOWS 3'�O rue ONLY SCALE:1/8"- Q?d Nuc 2 eq 11 ti",.54 � s GENERAL NOTES: 1. Occupancy type is R-1 with 1 -Hr type 5 construction. 2. Tenant separation and exterior walls 1 -Hr fire rated. 3. Corridor separation and interior partition wall in 3 story building 1 -Hr fire rated. SPRINKLER SYSTEM DESIGN CRITERIA 1. Design based on ordinary hazard Group 1. 2. All piping ; (wet and dry systems) to be schedule 40 steel for sizes 1".-;_2" and schedule 10 ,steel for sizes 2 1/2" - 4". 3. Piping on floors below attic level to be_.$AW pipe and fittings - As ,JoTEP A0ovE . L''? 4. Pipe sizing for wet systens based on hydrau'lic calculations c cct.4-Lw`` per 2-+.2.3- of NFPA 13°1989 edition. 5. Dry systems calculated to provide .16 GPM/sq. ft. over 1950 sq. ft. 6. All materials and equipment to be listed for use'in sprinkler systems. 7. All pipe hangers, earthquake bracing and fasteners to be per code requirements. TD A'T1 G PRY sYSTir/ut PRY 1Z1seR.. 1• • • BY /e -/-q/ . - I .--- .. _ -- _ _ _ _ I _ ,,..._ /0-T" 4, 4.-G`IL ti. ♦ 1i rb � I��=Z 1. Architects (206) 883-1200 2661 Bel -Red Rood Sults #202 B.II"vu• /o=7" /3 IL • /1. 6%" _� �.. r� /o -7r I i. • 8 6i'" /4.. y • (p-l�• tD=� HOMEWOOD SUITES HOTEL Franchised by Holiday Corporation to =8 13-4" 10-71" 8 `Si." Developer • • * e926 B. CENTER BLVD. L:_Ii JOB NUMBER: 9434 11- / r 1� Ii1 /�• Orli• Pn t7 00v iy91 I�- ----------------- 1. �\ Z w 0 0(c • (I� % On w).H.:". QZ 0 ox �; 2 mw ¢W 0 1_ Z0_1.e Itib- ,, 5 Q k 4 1. Date ?...../4-9/ = Drawn F-1_13 • . 8A7T/ • p i,viA/ k-:. 5P -Z If 3 -0 4- ' 1 -�-T --r-.�-- 1 _ 0 o .� 1 I 1 _ ' t _ o lien x _ �e!o �i I I 1-1 1 Q _ 0 el Q _ 0 0 _ Q I I Q. 1 Q O m 0 0 ®4 O o --� I ; 4' /o -a- �, /f -o" I l to=o" 8-ro" lr=o" Q r r l ) 1 if -v" A, t�?o' log=( to=v" k 14=v` 7 el �, 4, I , I .i' E ---I I. N 4/ s ;' / i r �- �" I i` / -84. /S- Z? # -6 '\ I ( 2" 1/3-8i T • 'SLK . 4 • • �l t n-7 ♦ --1 3 ♦ /0-7 --r ♦ - 8-84 4-o' 4-° !o-7 ; `'-_l Z l0 7 B-8 i- {10-7 • / .r,>< !f `( t Z.,U' 4-o" z=% • j Gv=G" �'-G ` z=// 6 I N 1 7 J-i'P I Trp Ti -ft.: r i� ill - __- it _ (._ �tlz Half F 1� ( L I �' 1 1 14- A � r4, t� !�' -• : `1 _ !_4- 4 • VdE=T Rls>r R GONNEGTtoN t?Ry" Pt PE VA.+'// PR.I_tSURE S*Jrr.H P tITTEiZt't-'r RA . w/-rT.MPE S Jrr .t4 SEE- SflE-?LAr-4 i} /R GOMPQFSSox gr -L. t6LE Moor& /i -3/474.P. //5/230v /8!9 AMPS .oyz /p tAoR / 5 -r I ;z PC7tA I L v l c c, No $GALE J I I I• -I I m 1 SPRINKLERS FIRST FLOOR PLAN UPRIGHT PENDENT Rr SaIDEWALL Pew PENT 77-/ls 54T W. B. LEHNER & ASSOCIATE' Fire Protection Engineers 0 ACCEPTED 1 ACCEPTED AS NOTED RESUBMI, 10RE -:T4 Dale: _ 1 )13 loo Ill TorxL /s sorer 32-4 REVISIONS BY /e -/-q/ r-13 Edward A McHugh Architects (206) 883-1200 2661 Bel -Red Rood Sults #202 B.II"vu• Washington 98008 HOMEWOOD SUITES HOMEWOOD SUITES HOTEL Franchised by Holiday Corporation HORIZON HOTELS Owner DIMENSION DEVELOPMENT COMPANY. INC. Developer • PROJECT ADDRESS: e926 B. CENTER BLVD. TUKWILA. CA.9131136 JOB NUMBER: 9434 /".-4,1=;',-----------,- , 4,t=-.._ ler. l � it/%' Pn t7 00v iy91 ----------------- U ..... c �\ Z w 0 0(c NEQ °'v ti w 4 (I� % On w).H.:". QZ 0 ox �; 2 mw ¢W 0 1_ Z0_1.e Itib- ,, 5 Q k ` Z w 0 1. Date ?...../4-9/ Scale /ip rep Drawn F-1_13 Job BLVD Z. Sheet 5P -Z Of Sheets 7` 34 X 36 PRINTED ON NO. 100014 CLEARPRINT • N( SEE SHEET SP -2 prig. CONT -IN 1/A71DN ( �_�TH15 SHOWS Z 'DFLOOZ. FOR /srt 3141'PLRS 5EE SHEET sr- Z. SPRINKLERS 2. •1- 1 1 UPRIGHT 16S'^ Ositohme C EI.4T1,AL,. M c'D6-1 A (o 3 11 -44 (04 1 PENDENT 1%0' • 3 • ( StraALL 1I.S' f e.MADL.- M.OD4FL FI/Res 1I2," os l -/C f c•uTRA!. Mover- It -I GH-IROME 29 ce•Nr)AL. Mop✓` A SOMI-REGeSsED CHR4l,4E .3 /4:4•41 - AS. CENT 41- MODEL -A -I RECESSEP CHMAPP.A 74, 97 71 TOTAL 774/$ SHEET z. 8 • Unit A i 1 Y ' Y t • o =: � Box : Dimensions- K. C At • • .4. I � A 1 i • II fl I L • • 75 50' • • • 273/4 4 25 31 6 - 4 23/. 1004 Recessed U 75' 24 36 51h 27'/4 393/4 25 37 6 % 4 23/4 1006 Recessed — 100' 24 40 51h _ 433/4 25 41 6 y 4 23/4 1012 Trimless 75 50' 24 30 61/4 27 33 25 31 63/4 e-4.• /o -7` 23/4 1014 Trimless 100' liar 24 ID=7& l3=Bi° 61/4 to=7` 39 8 .� � " 4 l0-7 " 13r 8�-� y tp=7� — , • li '1 Jt-�-1 �` 27 43 f4 — r. • • /i--- 23/4 14 t,_ , iL ' /4. 30. li , -t 14 (0 331/ i4. /1 ii 4 23/4 1024 Semi -Recessed 100' 75 24 36 51h 271/ 391/ 25 37 4 2 • 4. + 1028 Semi -Recessed — 100' 24 40 5112 271/ 431h 1-1-r---. -.-�- 4 23/4 L - _ .---- -. -- 26 32 6 _—,r..: -_ _____�..- — — — - ZJ 1 I .-e 'CI 71+.. O /o -o" 1ib boµose o o ll:o" 1 1 1 ©® I ©o 7T4 ± • or�,�+ 0 / -p- 1 1 I I/o=o" I— I loo $=cp I .,, /Z-6' Nr -i' f .1-I•/Z_ H — - — 7-.:n...._ - ; ,t;ri — 1056 — - 26 `f 6 — 7 E — — •— 6 �j (" I) — A ® I� !i lei !4. !% l4. al /i ® I !4 . , l4- .y•.. 14. UII�i 1� 1L ,[Intl E?,, • , /4 • -•-Ia�lni{ ''t�, E / �p 11 10 /illnttx oL •' I = A 11, a• • SECOND & THIRD FLOOR-- SCALE:1/8'-1'-0' 1--_r------a r 1 Unjt D —I BED RM. 1 fOGGUpAnlc/BS TYP. I�1 Uu,TS fj, D J L — - — a4 I s 44 00 L 3 -i see Per/4n_E3 oN DWG. SP -S- I 712°F UpgiGHT d\ 5PKiz /N AT -77G WET SPKR. P1 PING IN ATTIC. TO 5E oN WARM 5117E of INSU Fe=D MAIN la CROTCH of TroSS .5 rGlige i-H0014w//NVE,e7�D 3/4LuWDeR1J►YM'f �~/g"Tie PLYWD. 0! 1 UNIT CORA 1 a • Klo i/tI Int Zx/O ( sr. cHANMEL 11_2±44_ 1.1X117- SEMI-RECESSED IJIT SEMI-RECESSED THIS ontE 1 Unit E I 4 LD E Unlit D -'�- • a --T- --a— -- 4 FIRST FLOOR PLAN SCALE:1/8'-1'-0' ( cj SroRA6E pier sy.sreA4 A LIK . PRA !IV 4 1/4sPFGT(/ies 1 DFsT G0wNECT7Otl S EC77OPJ t3-55 SPECIFICATION: Provide and install where indicated on drawings Potter -Roemer Fig. No. /0 2.4- Fire Hose Cabinet with Door style Suffix C containing Fig. No. 1S'/P Fire Hose Rack Assembly. Flg. No r �J . _.. , -Wall . Mounting. ... , . MAX. CAPACITY .:. - PR Poli- _Super Flex Flex =: � Box : Dimensions- K. C At ` Overall Frame'" 11 : Q=- WaO_ opening✓ Bequfred rF - F - - _ i 4 == Tile - r_ L a E� 2 --^ Inle Lecattan 11 Erin 1002 Recessed 75 50' 24 30 5 Y2 273/4 33'/4 25 31 6 3/4 4 23/. 1004 Recessed 100' 75' 24 36 51h 27'/4 393/4 25 37 6 % 4 23/4 1006 Recessed — 100' 24 40 51h 27'/4 433/4 25 41 6 y 4 23/4 1012 Trimless 75 50' 24 30 61/4 27 33 25 31 63/4 — 4 23/4 1014 Trimless 100' 75' 24 36 61/4 27 39 25 37 63/4 — 4 23/4 1016 Trimless — 100' 24 40 61/4 27 43 25 41 63/4 — 4 23/4 1022 Semi -Recessed 75' 50' 24 30. 53 271 331/ 25 31 4. 2 4 23/4 1024 Semi -Recessed 100' 75 24 36 51h 271/ 391/ 25 37 4 2 • 4. 23/4 1028 Semi -Recessed — 100' 24 40 5112 271/ 431h 25 41 4 2 4 23/4 1052 Surface 75' 50' 26 32 6 — — — — — 6 — — 1054 Surface 100' 75' 26 38 6 — — — - — 6 — — 1056 Surface — 100' 26 42 6 — — — — •— 6 — — _ _ .. ALL DIMENSIONS 114 INCHES FIRE HOSE CAP/NET" L 0 e ectir 1.12 0 HEATER W. B. LEHNER & ASSOCIATES Fire Protection Engineers D ACCEPTED EL ACCEPTED AS NOTED El RESUBMIT D 1 sb. e7° -572-Z Ay,,,ly T 24 X 34 PRINTED ON NO. 100014 CLEARPRINT • REVISIONS BY 0-1-9/ Edward A McHugh Archtt•cts (206) 883-1200 2661 B01—R.d Road Sults #202 B.Il.vu• Washington 98008 HOMEWOOD SUITES HOMEWOOD SURES HOTEL Franchised by Holiday Corporation HORIZON HOTELS Owner DIMENSION DEVELOPMENT COMPANY, INC. Developer PROJECT ADDRESS: 6926 B. CENTER BLVD. TUKWILA. CA. 96198 JOB NUMBER: 9434 • +0\1,+ '--.•' . - ......-_,........../... •rte ii ..„,...----.7".7-----.- . . \ • OCT ; -. 1291 03 03 O) Date Scale /y o rut, Drawn PL,B Job BLP 2. Sheet SP -3 Of Sheets 714 Tb IL 1 Roof Framing Plan Scale • 1/8'=-1'-0" ATTIC DRY SYSTEM (SES ESCDG Z CALGS) r l4Ir �-e erckl V V -Co,W t V� W. B. LEHNER & ASSOCIATES 1 Fire Protection Engineers ❑ ACCEPTED El ACCEPTED AS NOTED `P3 RESUBMIT 13 B 24 X 36 PRINTED ON NO. 1000H CIEARPRINT • +I= Ifrausin P N TD S P. I . :1111 UPRIGHT PEN DENT SIDEWALL SPRINKLERS Key Plan REVISIONS BY 47'. of LEVE! 1!! _ H J ,c. 1 S'�M .---YC PI RV -117j 1 1 � Alra �iir/ Arilir A Inc. FIRE PROTECTION ENGINEERING INSTALLATION REPAIR PO BOX 58721 This system as shown on , &Ff'/r company print no. 5P -S , dated -/4-9/ for 110MEwool? .5"v1TZ`x (DRY SYsasii at eL Def- 8 - contract no is designed to discharge at a rate of • / gpm (L/min) per sq ft of floor area over a maximum area of hen supplied with ater at a rate of Building No. 8 Roof CROSS ttit A N J St E HAWGEP. :T"Il. O A'TTt C- G1zY 5}(STFr.t /Am GCMPR 5Sofz To RELM eter MODec. A a/t ElN4L /13 N.P. 11S -V, 8.2.4HPS� 60 Hz /f (pox SYS. cAIDA ceries up r> \.\\I t 80 GALL -OMS, WoT : coNNeGT THe CoMPigeSS®R l our7-eT ToTti/e DALY SYS. VI,4 AN AIR M.4/NT. / �bEVecr SuCN '4S RL`L//16t1E MDDEL TO 2.0K' FLK WET 5P).(:. W. B. LEHNER & ASSOCIATES Fire Protection Engineers D ACCEPTED GS ACCEPTED AS NOTED RESUBMIT O EVE OCT. 1 21991 L_ pNlx ro Aux. DRAI4 INSP. 'QST GGNPI. pVTA1L Aik..GoMvszessR` (SEEaTT.fEisve; t"t.AtN st Tr T--� GONNEclleN W,ATERH • bT WET SP'KR t-1n'ATEf`F: DW 5 W ITC:) •ro et -6 CT. f: CUL ?AC H VC -t4. VA . d.e?JT tt. Ma 1 L.f 3 � SuTTEFzrLY TAMPSR S Jrrr.I4 `MZLWAU:GE)r) SECTION A -A 118r'_1_o" PN 1,( iToDRY 5YS. Aux. DRAWN 9 11NSPtCTDRS I TE sr t ewnr . To ,Z no'r a ,;r x SUPPL'r�-/! FRGM ATT1G .I - W N "*+ W KI5ER PE.TA1L- N.T.S. cc m LtvING rM ±it. c -,i STAT B t2RM --i �'� e�Al.C1 LINT Cti_ 'AR l -t 5! ::r: � r tN�ut..4,TZ,-;1-J /ne vEierrA v-HO0Jt51 6" Zi`- V4 rrJfj�' 1,,, �TAlf A __ UTA1L, 5 (/IrE: TH se HANGEFL GETA/LS TMP• ,4LL euiLat,s1GS 5 7 Gv 48 1L 48 PENDENT 12 SPRINKLERS UPRIGHT Z.' e - • SIDEWALL 1Lo' lief' PRY PEND`. CeaJ *AL Mopec A seesaw RE: L1AUi MOOit.. Fr/RES 4eeoeirice ' lesj:G�'.• CBNnci MeeEL ►{-i GNI*OMF Dey NO RL 514 ce,.ITAAL #4.001L.4 -J . REgessei> cNRD/NC REVISIONS BY 0-1-9/ 03 Edward A McHugh Architects (206) 883-1200 2661 Bei -Red Road Suite 1202 Beli•vu• Washington 98008 HOMMEWOOD SUITES HOMEW000 SUITES HOTEL Franchised by Holiday Corporation HORIZON HOTELS Oester DIMENSION DEVELOPMENT COMPANY. INC. Developer PROJECT ADDRESS: 6921 B. CENTER BLVD. TUKWILA, CA. 911159 JOB NUMBER: 9434 t S.. ci Ptt S Zi r 1:6 .-eu N p1 N. W� m 1 i‘kI" n Q Qg.2 x 0. III% Di mW 1 0 F.. - -nLL3VYW - 11. 1!1:W - V Date 9-/(0_ f/ Scale Nor -el) Drawn pi_ a Job 131-P6 8 Sheet -, SP -5 Of Sheets 24 X 34 PRINTID ON NO. 1000H CLEARPRINT • 1151.1YllIL11LLEM 111/11M IIIIIIIfhliI111WIWWIMMYYWWIIWYI 'MtYY11Y4MWYWM1411WYVWNIIU.'lll'Jyll'Ll' Id 11 ' P5W0re5 0 vTzI N E - Of REMOTE A RCA pe'S/GN ./4//9.00 .y: .PENorEs ourchve OF QeMorE AReA n`-f./6� tgso p lea Pr £T ai° . o ID+Io 5-o Js ---o —v 3 1 -I 0. - 4 Isrnk. v 114 — STAIR • PORCH ATTIC PRY SYSTEM( compar dated 4? -/-47/ / 8vi 7-r; i SfirrFM) contract no is designed to discharge at a rate of • / G gpr: (L/min) per sq ft of floor area over a maximur area of ....1. ? 57E2. .... sq ft (m2) when supplie'. AIR CAPACITY = 133 GALL-o14S —1 /1. i with water at a rate of 4 8 8 gpm (L/min at psi (bars) at the base of the riser Hose stream allowance of P gpm (L/min) is included in the above. ATTIC DRY SYSTEM, //23"--/:-0 Al J� COMPPESSOR Ti SE RELIAIne MooEL ` O R r R viV• ILFNT: %3. NP. /1.5-V a 8. z /fMPJ o HZ /p ( foie SYS77-iv1 CA PAci77E5 up ro /80 Get61-49/tl.19 use /teL,A0 .E Ado Pet- $-/ A/R Mit /IVT- ,OL'tr/6e To come/tes1'0A Ovrte-T `®�— BY g-- C. /3 /16 . S'G-z L3\r\ J /i2---‘ /t- 85._ l1 i4 317i '4- S'L . t @ r•/DL 5.-- 42- Z L(1) _ ©. 3ell-c CO k g z M r A McHugh K / orf -- r � /4 _ C9 I /4 /4 •SI//,} HOMEWOOD r I SUITES - ,- ii HOMEWOOD SURES HOTEL Franchised by �-t1 HORIZON HOTELS Owner ), < COMPANY. INC. �/ 7//r r .. TUKWILA, CA.98198 JOB NUMBER: 9434 „,"'tvv'( L=VEL r1f .h L—_ ! \ :i ,,,Jol 4�P I --- ' ,I !�r , '0 CI i ' • • V N o¢ ) p... 6 - . NoQ ", 1 km 4 0�, c,g Q o ¢Z x 3 p II 9 otYl I� W 4 QQo I- b � Date 9•-/G-9/ I Drawn /=LB Job $W(, GS f 63" _ 114• i4 • l� l 114 ® /4 t rr _ TT' /4 I4• /4 //4/, : — _ 1141 i • 1141. 1t • 1 - • 1 4 • ♦ I it 1 11{ / 1 f 1 !�f- ® // 111- 111 r l 14 I u Ito- I14-� t 111 t / 12 Q 8sI UNIT F. { 6 /0 3i• S-, G UNIT - 8 Si /1-7a F b -BL UNIT H - 5-0 UNIT H //-riL 8-5-i. UNIT • S -G F • ` 31- S" eo _ UNIT F 5' :._�/ r.f -� p X / Z//1—I' d 1 m 1 /4 1f.00 ' l4 • , 0 1� t` • I-1II II, i.b.e - . e+---• /4.Ilf • /(,l !I� • • •� 11{ r1! ! • ifs Ila • 114 I 'r. /!s'i 0-9 !a- Si 10-9 ,5-/ i- z• 11-0j ' 4- L 8-/L . 10-9 • 121 84_ • /a-9 • / �) J l 14 j l l 14 11 t- / 14- / t r / 14 /4 114 / /14 f if LM 01 1 _ I�T _ ---�� KIT PINING GI—OS, X1 ��' UNIT V� ► i 4- F ® ► 1° Q 11; ► UNIT - F t t4 I I•i- 114 I I t UNIT F 11+ 11+ ► t3AM �. r VANITY 14_• UNIT 114- F is I 1 H UNIT S,G` S'G• 1 17e— 4< i 4:34� • _f o x BED / / / • RM. ., 0 �,�/� !' x t o 7 x LIVING :J I <•r/V ` -1 t I I �°� I'@ 07 /1'� (� I0 i+ (0z i+ O. '� Y `Y ft4- SI ,ria I�I �,./1+ 1 . 114 , illI I' 1�1 T II I SPRINKLERS So tr UPRIGHT 2.12' -0-- -de," 77144, MOPE L A 14-4 S', PENDENT 155' • REL/A$LE MO 'EL P'//#e S 30 14- SI5MALL /G5 CENTi .4L DRT S•IJ. MdPEL H-1 GHR#M ZO 12 blrPEAW---- 11.-5a Mop01-4-I CHRoNE zi4 - 121- TOTAL THIS SHEET 39G 0 '1 CO x r PORCH r , 5TOR. BEPRM. BUILDING :NO. C5 FIRST SECOND FLOOR PLAN SCALE:1/8' - 1'-0' fL TYP. OCCUPANCY A.5 SN014N ABoV5 vi r� } } - ut 11.3wo • iv t 144 v 40v rn o ° 1E PRY/r1.5/4,z R Z ON >=! T FLJZ —� oNLy 0-rp3k Sr�1z E. his isystem as shown on ... crfet J'T.. comp. pr jno... SE. -4 dated. '51"/4..71/. Kr for ..H /4atYoP.P.ACV,.rg; . 17.YcrTlr/!4) at .... ,> 4-O.G.. a 5 contract no is designed to discharge at a rate of • / 6... gr. n (L/min) per sq ft of floor area over a maximi :1 area of / SD sq ft (m2) when suppli . j with water at a rate of ...4'.74...gP m L mi ) ( / at ....%4:.... psi (bars)'at the base of the rise -. Hose stream allowance of <3 gpm (L/min) is included in the above. 6Le c77.1 D Go /4 ) To fnlsP• TEST (SCE /.57 -Pi le.) To ATTIC PRY 5Y'ST V TO 2N"' 1:L12._/ Vs/ t r 5YST: -1-0 ) sr FL12. WET SYSTEM--" G' A WATEfa FL/2W 5K/11tH TD ELECT. BELL Z.ls" C!4 Ecl< VA. �--� Z4:i4M-rT R.FLY v,0, 1&// TA SWITctj -7-=-11" w SLEI±VE Ai Ft.12� RI5 f? DETAIL ( 'P1 cAL f31 -V65 c-5- ¢ E 5 /"/4 LX.DrZN. e I ►JSP. TEST GoNNECT7oN To ovTS/DE ISYsr ivf r777e- r pLR .ONLY _ etc • - tt f tC/ l Ve Hoj'i''Ir i .evt e v . 1 ©4-e 14;_s" Dr BUILDING NO. E5 FIRST I 1 !I.... i - W. A. LEHNER & ASSOCIA — i Fire Protection Engineer. ❑ ACCEPTED XI ACCEPTED AS NOTED QRESUBMIT i SECOND FLOOR PLAN SCALE:1 /8'-1'-pl1 24 X 34 PRINTED ON NO. 100011 CLEARMWB. REVISIONS BY i4 y_.l�" o x t @ Edward I 3ell-c CO k g z M r A McHugh K / orf -- r � /4 _ C9 I /4 /4 •SI//,} HOMEWOOD • SUITES - ,- ii HOMEWOOD SURES HOTEL Franchised by Holiday Corporation HORIZON HOTELS Owner DIMENSION DEVELOPMENT COMPANY. INC. Developer PROJECT ADDRESS: 8925 6. CENTER BLVD. TUKWILA, CA.98198 JOB NUMBER: 9434 „,"'tvv'( L=VEL r1f .h L—_ ! \ :i ,,,Jol 4�P I --- 'l i1 I ,I !�r , '0 CI i ' • • V N o¢ ) p... 6 - . NoQ ", 1 km 4 0�, c,g Q o ¢Z x 3 p II 9 otYl I� W 4 QQo I- b � Date 9•-/G-9/ I Drawn /=LB Job $W(, GS f 63" _ 114• i4 • l� E 0 114 ® /4 t rr _ TT' /4 I4• /4 //4/, : — _( '11 it :• ij i1 ® // 111- I` - ' I 114• �� It `I I I/f / 14 1• IZ • ', '-(1)0Z :._�/ r.f -� p X / Z//1—I' d 1 m 1 /4 1f.00 ' l4 -7-=-11" w SLEI±VE Ai Ft.12� RI5 f? DETAIL ( 'P1 cAL f31 -V65 c-5- ¢ E 5 /"/4 LX.DrZN. e I ►JSP. TEST GoNNECT7oN To ovTS/DE ISYsr ivf r777e- r pLR .ONLY _ etc • - tt f tC/ l Ve Hoj'i''Ir i .evt e v . 1 ©4-e 14;_s" Dr BUILDING NO. E5 FIRST I 1 !I.... i - W. A. LEHNER & ASSOCIA — i Fire Protection Engineer. ❑ ACCEPTED XI ACCEPTED AS NOTED QRESUBMIT i SECOND FLOOR PLAN SCALE:1 /8'-1'-pl1 24 X 34 PRINTED ON NO. 100011 CLEARMWB. REVISIONS BY Edward A McHugh Archtt•cts (206) 883-1200 2661 Bel–Red Road Suite #202 Bellevue Washington 98008 S HOMEWOOD SUITES - HOMEWOOD SURES HOTEL Franchised by Holiday Corporation HORIZON HOTELS Owner DIMENSION DEVELOPMENT COMPANY. INC. Developer PROJECT ADDRESS: 8925 6. CENTER BLVD. TUKWILA, CA.98198 JOB NUMBER: 9434 „,"'tvv'( L=VEL r1f .jam :•"...-- �`' -...----7-_:_:;.,/ .-.� -- /,W/ \ :i ,,,Jol 4�P si-� VAA 'l i1 I ,I !�r , '0 CI i ' • • V N o¢ ) p... 6 - . NoQ ", 1 km 4 0�, c,g Q o ¢Z x 3 p II 9 otYl I� W 4 QQo I- b Rigor w c � Date 9•-/G-9/ Scale /41,7 -op Drawn /=LB Job $W(, GS f 63" Sheet sp__& Of Sheets t 4E4-449 w t 1t • -44 ite Fd?r� SER lief Th N 0 t ate s�•�� ri o -44934 A€ r4VI Y RNt • 1 A r GENERAL NOTES s } } 1 ORT SYSTEM'S PIP 16 We 8E PITCHED AT LEAS 1/2 P IO 0 FOR BRACH LINES AND 1/4 1N 10 0 FOR CROSS MAINS 2 IN ATTIC AREAS SPRINKLERS SHALL 8F 'OLATED 0 -LATERAL- FROM TRUSS ME."'BERS 3 DEFLrtTORS OF SPRINKLERS triALL BE LOCAtED 4 1/2 MINIMUM TO 1/ MAXIMUM BEL O ROOF DECK (FOR CENTER LINE OF PIPING THIS✓ WOULD 8E B M1 IMUM TO 13 1/2 MAXIMO BELOO BOTTOM OF ROOF -- DECK } 4 2-944.4,494. Lt IW$ULA"T7,Jf�/ OVE-R P I Pl A7 L_�r /XOZ 111PILE 1/4 VtRTZ'D 11-/1OD/ (�R �v Dei -4f f 114- aiN /14- PA iv my • 0 9 Roof *To' 4444 tzli • ,71 934 0 0 t43.r. .-- 4. IUD eill rife NS 33 • NIL OW Pair exAstpoi' imrrE0 war ea um Om "IAA Wt.03tu-usTrin*TrAosseirs in. gums PM** ON rwIL Ws rismiammrnms. NIL on irasra, ross IXONSUOMLIOACIL formsousensm .4949 0 44, 333 ONEINATION BOOK NIL INN 4to IINITOLYND imoullinAt -- rs 993 -r 41/62.2MRAT 316. ION NUITCLA$61. 4 4.02146111611644.46441 16064441401116646/41.6r L. FPIceieLassitool 13, - 1 117.341T4 WITTialffetilEill. 4.6411 IMO SRA& ,I imex i ./ ..- 1106611113 ONITANCI 313e zgrA 4 a 13 <14 -144 ITOLCO FAST CLAMP I iWAY B RACE ATTACHMENT 4-24 TratASS ,cot44estLei, W/ - WHIM 4OVEX PLATE' -TYPICAL- HANIeR3 CCEPTED WIT UT COMMENTS AS OTED IN RED D PE THE ATTACHED LETTER The dr gs affixed hereto have been - viewed and accepted by the City of Ukwila Fire Dept Additions deletions or rsevisions to tnese drawings after this - date will void this acceptance and will require a resubrnittarof revised draw Final acceptance is subject to 575 4407 7-0 sY.SrrAil lc -LIABLE MODEL:if' Abe ;1230 V ail # 44443 tvl wt, 14. 0 axemciso 3-11 1 Rff16,1Z-tii. riga 4° SPX VI4 147 IrI*0 600 --SPRINKLER SYSTEM DESIGN CRITER/A 4.4 DESIGN BASED ON ORDINARY HAZARD GROUP 1 OCCUPANCY WITH , PIPE siziNp_ PER ORDINARY HAZARD PIPE SCHEDULE (SEE NEPA ALL PIPING TO BE SCHEDULE 40 STEEL FOR SIZES 1 .72 AND - SCHEDULE 10 STEEL PIPE FOR SIZES 112 -4 - MATERIALS,. AND EOUIPMENT TO BE LISTED FOR USE IN SPRINKLER SYSTEMSr ALL PIPE HANGERS' FASTENERS AND .EARTHOUAKE BRACING TO BE` $. r'''';":-..`4'•:' ' -1 DENOTES PIPE HANGER; ' A 44 sts 44 93. o 4 SPRINKLERS Ktvit- 1.4 ADM TN srizArto 0 NIP 4 • 4. 04* 4. SIDEWALL pa y 1,72. rorAL 11-11s .5 3-0 Si 4 .9.4443 I 0-61 9,3 -17 smCrr 039 404444* Fire Protection Engmeers ACCEPTED - ACCEPTED AS NOTED -- - D RESUBMIT BUILDING _NO 1 Dale NOV 05 1991 .% 3-4 REVISIONS BY Edward A McHugh Architects S ire #202 IIOMEWOOD SUITES HOIIEVA100 SLOES HOTEL Owner COUPANY INC. Developer -"PROJECT ADDRESS 6921 6 CENTER 111.90 TUKWILA CA 9111118 .108 NUMSER 9134 TS tij r9 40 ea as 0 X ID c 114, il * ir use) o_.' ;131 0 t x ; t-3 1 iill a. : tu : tit,Pi! 0 1 -.1. - it 0 f65 Drawn 'r Le Sheet Of Sheets - 24 X 36 1604t6.13 ON NO 10001$ CLEANOW4146 939 .5 61\ -33 4 £N TRY PORCH pa RCN b 7 r r / 7 i J. i% 7/ /7 iZ 90 f v p 1247r4 (T'Yt',19 Tar V- or -1 J 1(4 4.4 S \ PCUce,r .SPK, A. w/ WHITE ( Vff1( FLItrr }T Tr) 1 r (sr—ft i441- 4 k .- Z4ANlt/6 DECK 3e`YOONP GREAT ROOM s cot V JF tN PlJ TDP F BOT cHoR,D _,mac%eE t*/f tNVEIS=T'FD y —t1 ttoK -; - s i t9 0" /p QP SERVICE FEED MA,N" VEST78LE i _t T S G T7 o tJ T 1 a L?AY P.'IAJAI o1/ ror, 3 ` ti n7Ot J f '"'/turt�reo # x(i'CROSS Y ,4A /Al 1' /14N}1 -o s _--14 S�G"1-1QN 11443.1 -fou _ t _ c - 4 �M�Z2. DEcf� _; J "tYfL 7 Tito' Gt tip pc.tt o Z x+BLK6 t eYe Ler espt x; 4:7/ 4. Lit itlitt12:11e:::: 712:11: .517:41:: a - Pi. Dog Petit ENT PETAIL. A- 4 ir 0,4 4 W. B. LEHNER & ASSOCIATES Fire Protection Engineers AK ACCEPTED AS NOTED D RESUBMIT - i PENDENT '711.4" SIDEWALL • REVISIONS BY Edward A McHugh - Architects (206) 883-1200 2881 84.1—Rod Road Suite #202 tisliesu• Washington saws HOMEWOOD SIJITES HOMEWOCO SUITES HOTEL Franchised by Holiday Corporobon HORIZON HOTELS Owner DIMENSION DEVELOPMENT couPyrr INC. — Developer PROJECT ADDRESS •926 9. CENTER BLVD JOR NUMBER: 9434 A.'4EPris_st-f-c444 :9 1 tit Drawn yL,E3 Job 54,i7 - L Sheet _ Ot Sheets -=a N 83'35'44" E 158.18' . DEs IPTICw/VATE BY N 6335'44- E SU WING D 0+41.84 0-1-50 1+32.50 D - 084447" R - 5(x0000' L - diMOW BUILDING 84' 139'-7 1/2" x 61'-5 1/4" CO 03 0) 0 m 1E w 0 0 C1) • a 2 0 0 i7 co CD t: ' C5 BUILDING C5 134'-3 1/2" x 63'9" 0 = 1836'38' R — 28.00' L — 9.09' 17.00' BUILDING B3 BUILDING 82 117'-6 1/2" x 61'4" 41'-10 1/2" x 31'-3 5/8" 6.- N 4 O S NO. 645--001-901 �RAV1Y RA COMP. MHT CHECKED MHT DATE March 25, 1992 A = 105'51'58' R = 32.07' L = 59.26' DWG NO. 64501CTL OF l SHEETS ' oo,e'.IELP1Luiwur 30' 20 /0 EXISTING GROUND LOW IMPACT LINE PROPERTY Li NE 1 3 DIKE ffSE ENT ~ !2' TRAIL • 6 MAINTAINANCE ROA' EL = 24.50 MIN. ul /PR'POSED PROFILE • MIN. 30- 20 10 0 30 20 /0 PROPOSED BLDG. FF 26.50 TOP = 69.68 z . SECT/ON A - A PROPERTY LINE EXISTING GROUND 2 2:/ 12' 30' MIN. DIKE EMSEMENT 6 TRAIL !2' TRAIL. ( & MAINTAINA N EL = 24.50 MI 2:/ E ROAD ct Lo Li0 c0 O Lam. O0 ED 0 L EU La/ C PROPOSED PROF/LE- PROPOSED BUILDING FF = 26.50 TOP = 69.68 SECTIONB - B 2 -J ti v 0. O EXISTING GROUND PROPERTY LINE I 0 a 2:/ 30'MIN. DIKE EASEMENT 6 TRAIL 12' TRAIL & MAINTAINANCE ROAD EL = 24.50 MIN. PROPOSED PROFILE 0 --- 30 PROPOSED BUILDING FF = 26.50 TOP = 69.68 20 /0 0 EXISTING EX/STING GROUND SECTION C - C PROPERTY LINE �I ml 2r--- ---' 7',... v 2:1 - - 2.l 2 Li 0 0. 30 30 PROJECT 100 YR. FLOOD EL. = 22.50 - 12000 CFS ( 100 YR. FLOOD EL. = 22.30 20 9000 CFS EL.. = 18.30 /0 0 • 20 /0 PROPERTY LINE PROPOSED PROFILE mcnt- 30'. DIKE EASEMN'), & TRAIL • EXISTING GROUND 0- 30 30 - PROJECT 100 YR. FLOOD EL. = 22.50 12000 CFS (100 YR. FLOOD 1 EL. = 22.30 209000 CFS EL. = 18.30+ 0.50' = 18.80 20 - ---/0 0 30 PROJECT /00 YR. FLOOD EL. = 22.50 F2000 CFS ( 100 YR. FLOOD EL. = 22.30 20 9000 CFS EL. = /8.30 { 0.50' = /8.80 30' MIN, .� DIKE EASEMENT & TRAIL 12' TRA/L .& MAYNTA/NANCE ROAD EL = 24.50 MIN. PROPOSED PROFILE 30---- 20 /0 0- PROPOSED BUILDING FF = 26.50 TOP =-59.00 EXISTING GROUND SECTION D - D PROPERTY L INE 2:1 12' 10 0 /0 0 PROPOS i S4CTION G - G BUILDING FF = 26.50 /TOP = 59.00 PROPERTY L INE .2 12' 12' TRAIL 4 MAINTAINANCE R0.40 EL = 24. . 0 MIN. 2::/ 2:1 30' M/N. DIKE EASEMENT & TR IL cr j2 pT • 0 W 12' TRAIL & MAINTAINANCE ROA EL = 24.50 MIN. o Lu Is al XISTING GROUND 30 PROJECT 100 YR. FLOOD EL. = 22.50 12000 CFS 1100 YR. FLOOD 1 EL. - 22.30 20 9000 CFS EL. _ /8.30 + 0.50' s 18.80 /0 0 PROPOSED PROFILE 121 30 PROJECT 100 YR. FLOOD EL. = 22.50 12000 CFS ( 100 YR. FLOOD 1 EL. = 22.30 -2° 9000 CFS EL. = 18.30 • 0.50' = 18.80 /0 30---- 20- /0 0 -30 30 PROJECT 100 YR. FLOOD EL. = 22.50 12000 CFS (100 YR. FLOOD 1 EL. =22.30 30' MIN. DIKE EASEMENT 6 TRAIL W 2Q-9000 CFS EL. = 18.30 • 0.50' = /8.80 TRAIL / & MAINTAINANCE ROAD EL = 24.50 MIN: 30L 0 { LOW IMPACT LINE PROPOSED PROFILE SECTION E - E PROPERTY LIN 1 /2' 'M DIKE EASEMENT & TRAIL PROPOSED PROFILE SECTION F - F 10 0 ' 12' TRAIL & MAINTAINANCE ROAD EL = 24.50 MIN. TOP OF BENCH J SECTION H - H _PROPOSED 0 DUILD/NO FF = 26.50 TOP =59.00 EXIS /NG GROUND _L 30' MIN D/KEEASEMENT W KLA W� 0 ct; 02 PROPERTY L LINE `r c" JI \ -I �• - -/2' TRAIL & MAINTAINANCE ROAD EL = 24.50 MIN. PROPOSED PROFILE 2 J SECTIONI - I / 3 PROPOSED BUILDING FF- 26.59 TOP - 59.00 EXISTING GROUND 1- 12 EDGE OF RIVER PROJECTFI) TOE OF RIVER 0 30 PROPERTY PROPERTY J vi ml 20 /0 0 PROPOSED PROFILE LINE 20' LMIN. DIKE6 kTF3AASEMENTI w � 0 -CEj Lu TOP OF BENCH - 12' TPAIL & MAMITAINANCE ROAD EL = 24.50 i - Tf 2:/ 2:/ 30 30_ _ PROJECT 100 YR. FLOOD EL. = 22.50 12000 CFS (/00 YR. FLOOD 1 - EL. =2230 20 -9000 CFS EL. = 18,30 • 0.50' = 18.80 20 ----/0 /0 0 0 30 ti OED BUILDING 3 Z FF = 26.50 0J TOP =59.00 EXISTING GROUND GROUND SECTION J - J PROPOSED PROFILE 0 30 PROJECT 100 YR. FLOOD EL. = 22.50 12000 CFS ( 100 YR. FLOOD 1 EL. = 22.30 9000 CFS EL. = 18.30 • 0.50' = 18.80 U PROJECT 100 YR. FLOOD EL. = 22.50 12000 CFS (/00 YR. FLOOD 1 EL. = 22,30 209000 CFS EL. = 18.30 • 0.50' = 18.80 10 1- 1- W W PROPERTY L INET 1 \ -; TOP OF BENCH 30' MIN. DIKE EASEMENT & TRAIL ti 12' TRAIL & MAINTAINANCE ROAD 0 EL = 24.50 2l 0 30 20 30 PROJECT 100 YR. FLOOD EL. = 22.50 12000 CFS ( 100 YR. FLOOD I EL. = 22.30 ----20 20 9000 CFS EL. = 18.30 • 0.50' = 18.80 --- /0 /0 W of PROPOSED BUILDING FF = 2650 SECTION K ISTING GROUND F- cc z Lu >00 Pc- cc vW BUILDING PROPER Y L INE FF = 26.50 TOP = 58.57 IL 30 IN, DIKE EASEMENT & TRAIL \' .12' TRAIL & MAINTAINANCE {ROAD EC =-2450 -11111ir N J CC Lu 0 U 1,4 WCD O Wa. PROPOSED PROFILE 121. /2 0 0 ELEVATION LEGEND 18.30 = 9000 CFS FLOW ELEVATION 18.80 = LOW BENCH ELEVATION 22.30 = 12000 CFS FLOW ELEVATION ( 100 YR. FLOOD 1 22.50 = STANDARD PROJcCT FLOOD ELEVATION SR 899 .w410•MWM. w.+...,.�+ww�- .-.."--.- J 4000.1.1.0‘ SECTION L 2:/ 2:1 10 0 30 PROJECT 100 YR. FLOOD EL. = 22.50 12000 CFS ( 100 YR. FLOOD 1 EL. = 22.30 9000 CFS EL. = 18,30 • 0.50' = 18.80 HORIZ. & VERT. SCALE : l" = 20' PROJECT 100 YR. FLOOD EL. = 22.50 12000 CFS (/00 YR. FLOOD 1 -20' EL. = 22.30 /0 0 9000 CFS EL. = 18,30 • 0.50' = 18.80 NO. REVISIONS DESCRIPTION/ DATE I BY 3 s'/e. P/wn i2-ic.a9 4 c.l� 3 -i,' -9v %le C. 'oN -1 P' '//6�9A :7:7) '=4 S o/ c eY1f e f' ¢ fie _i,,. rad. .�/2s/9z pi, 2 W 0 15668 West Valley Highway Seattle, Washington 12061 255-4100 a JOB NO. • 624-001-891 DESIGNED M.T. DRAWN D.D. COMP. CHECKED M.T. DATE OCT. 23, 1989 • C eureve AWOL t . ,u rra..h,"..r**11.,.......- 12" TEE " 1-8" GV 1-1c•" GV ;-12 X8' REDUCER CONC. BLOCK. . 156.17' IE :JR Si Avera tAidu ar 'A rw...irw....t4►..swiilifiri mre,idw.wrw, twomanme1111645W M • 165,53' �-"%zt1y-2 Qsc.ot, IA. err.) op. -Q- 12-vs04i tiND Cf`(P.) STA 3.9 MAINTAIN MIN OF /8' BETWEEN WATER d ALL SEW AT CROSSINGS ( TYP. • CAPPED SPKR SNB 90 LF8"OPVC S -0.5X SEE SHT C-5 OF FOR CONTINUATION STA 0+20 8' LT. ,12"X-8" TEE 12"X8" REDUCER 8' OV CONC. BLOCK. 17LF 12" 0 D.I. 12"0 0.1. 12"x8"TEE (MJxFL. 1 29LF 8'0 D.!. DOUBLE CHECK 8" 45' BEND (MJxMJ1 W/ CONC. BLOCKING CIGU B Above 4Yc L52 D•l• STA 4096.5 STA 6.98, 8' RT. 8" 90' BEND M)JCM,l1 W/ CONC. BLOCK/NG I.E. + 18.95 STA 6+85 STA 0.48 8' LT. 8"x6"TEE (MJxr 6" GATE VALVE( MJ»FL) 6" F.I4 ASSY + W/ CLANG BLOCKING 1. STATE APPROVED DOUBLE-CHECK VALVE ASSEMBLY, COMPLETE WITH O.S.&Y GATE VALVES AND BRASS OR COPPER BY-PASS. 2. STATE APPROVED 3/4" DOUBLE-CHECK VALVE ASSEMBLY. 3. SHUT OFF VALVES. (3/4" GLOBE) 4. 5/8" METER WITH READING AS REQUIRED BY CITY OF TUKWILA. 5. UNI -FLANGE WITH SETSCREWS. 6. ACCESS LADDER. 7. 1 -CONCRETE VAULT PER CITY OF TUKWILA REQUIREMENTS 8. WATER TIGHT GROUT AT PENETRATIONS. 9. DRAIN WITH SLOPE TO DAYLIGHT WHERE APPLICABLE. 10: TWO ADJUSTABLE PIPE STANCHIONS OR CONCRETE SUPPORT PADS. 11. SWING CHECK VALVE FOR PUMPER CONNECTION. 12. 4" DUCTILE IRON CLASS 52 TO FIRE DEPARTMENT CONNECTION. 13. VAULT ACCESS WITH VALVE ASSEMBLY CENTERED IN VAULT 14. CL 52 D.I. M.J. WITH RETAINER GLANDS. - 15. POST INDICATOR VALVE. FLOW PLAN 8" SSiSTUB S• OXMft2 SS C.O. RIM EL.. 26.50 J.E.. 19.57 8" 4 D. % 8" SS STUB •-C - MIN. Ss C.O. • - RIM EL. - 25.90 1.E. - 19.67 M• STA 5.00.5. 10' RT. 8" 45' BEND (WNW, W/ CONC. BLOCKING -4' ''S'PKR - sTv8 ss Oto. �-- • - . L - : 5.70 I.E. - '0.77 •. SCALE: 1" = 20' NOTE: ALL CONSTRUCTION SHALL BE IN ACCORDANCE WITH "STANDARD SPECIFICATIONS FOR MUNICIPAL PUBL I C WORKS CONSTRUCTION" PREPARED BY WASHINGTON CHAPTER APWA, CURRENT EDI TION AND BY THE CITY OF TUKWILA STANDARDS AND SPECIFICATIONS. 1 -NOTE FINAL LOCATION AND ALIGNMENI , OF S.SEWER SERVICE CONNECTJON�WLL PROVIDED BY OTHERS STA 6+14 14' RT. 8" x 6" TEE (MJ.FLI 6" GATE VALVE (MJxFLJ 6" F.I-L ASSY W/ CONC. BLOCKING T" LI) 1 ACCESS •. . STA 6.07 1/O' LT. 8" x 6" TEE (MJ.FL1 6" GATE VALVE 114.1xFL1 6" F.14 ASSY W/ CONC. BLOCKING ELEVATION SPRINKLER VAULT PITA! L"A" NOTE: ALL UNDERGROUND FIRE PROTECTION WATER MAINS TO BE INSTALLED PER NFPA 24 AND CITX OF TUKWILA GENERAL NOTES /- OCCUPANCY TYPE IS g-/ wj 1-14R. -TYPE 5- Co I.I STR 2 . MINIMUM DEPTH Of BURY 4 -0" 7Yf• Envkortmont 5. s ysTE M CONTROL VALVE To BE , INSf t?E 1 MAINT :ETW SS C.O. C. 26.50 /.C.. 2Z88 STA 2+87 8' LT. 8" x 6" TEE (MJ»FL1 6" GATE VALVE (MJxFL1 6" F.1 -i ASSY W/ CONC. BLOCKING 2 STA 2+92, /0' RT. SSMH4.2 RIMEL -25.62 1.E - 19.56 1 HC STA 3+02 / 200LF 8•• 0 PVC S a,574. A 4, 28' LT. 8 22 1/2' BENA (MJxMJ1 W C C. BL...CKING STA 5.00, 10' LT. 13I-126. ON KISER_ ASSEM13t.y ••' W/ AGGESs FROM OUTSIpE WATER FLOW FOR SITE STAT7 C 141 P 12ESIQUAL 108 Pa.I. w1 3/57 GPM STA 3.12, 7' RT. 8" 90' BEND (MJxMJ1 W/ CONC. BLOCKING STA 6.12, 7' RT. 8" 22 1/2' BEND (MJxMJ1 W/ CONC. BLACKING W. B. LEHNER & ASSOCIATES Fire Protection Engineers 0 ACCEPTED 0CCEPTED AS NOTED 'RESUBMI REJECT /2 /0 iimmitiminni.mnim !minima*, 1, i_ REVISIONS NO. DESCRIPTION/DATE I BY O¢O,N Nop 0toto ao W( a (7). PROTECTION S JOB NO. DESIGNED DRAWN 4oWM4AN COMP. CHECKED cA • DATE . Date: AUG. 1 7 1991 EDGE ,OF RIVE Greet- Ri}rer sp--/ • 12"TEE' " 1-8" GV • 1-12- Gv ;-;2-X8". REDUCER COr1C. BLOCK. . -rtia.t1 PsLock Cri'P•) -O 1 -vi. N1t - - 71.hto C't`(P.) = -_ - •••,•aa.fi u.s �1a6'Yll.it;ri.J'k1'i1M.�1f1w�4iM/1✓:I�iI1�.M::,i lA1�./Y�MY�1wArr1/v YM�Ri _ ' 168.53' MA !N BETW AT CR IN MI EN WA SIN OF 18' R f TYP. L SEWER 22'. fi R "Q1 SEE SHT C-5 OF FOR CONTINUATION STA 4+15 90 LF 8" 0 PVC S • 0.5X STA 0+20 8' LT. :12x8" TEE (2"X8" REDUCER 8" GV CONC. BLOCK. 12.0 D.1. 12" x 8" TEE HAI. FL 1 29LF 8"0 DI. °BLIaG. B move b UT5:� 8" 45' BEND (MJxMJ) W/ CONC. BLOCKING 17L.F 12" 0 D.I. CLSz 4•"G L 52 D•i. 4.1.00.71arigisarmakrigiliorammeitaiimmegilagaldirOlitrial \\\\\ \\\ 13.) \\\\ \\)1\�I11 '. B Aave 1 C STA 4.96 1 ' STA 6.98, 8' RT. 8" 90' BEND (10,4JxMJ1 1W/ conte BLOCKING SCALE: I " = 20 I\ I.E. " 18.95 STA 0+48 8' LT. 8" x 6" TEE (MJ.PL, 6" GATE VALVE( M.J.FLJ 6" F -L ASSY W/ CONC. BLOCKING 1. STATE APPROVED DOUBLE-CHECK VALVE ASSEMBLY, COMPLETE WITH O.S.&Y GATE VALVES AND BRASS OR COPPER BY-PASS. 2. STATE APPROVED 3/4" DOUBLE-CHECK VALVE ASSEMBLY. 3. SHUT OFF VALVES. (3/4" GLOBE) 4. 5/8" METER WITH READING AS REQUIRED BY CITY OF TUKWILA. 5. UNI -FLANGE WITH SETSCREWS. 6. ACCESS LADDER. 7. 1 -CONCRETE VAULT PER CITY OF TUKWILA REQUIREMENTS 8. WATER TIGHT GROUT AT PENETRATIONS. 9. DRAIN WITH SLOPE TO DAYLIGHT WHERE APPLICABLE. 10, TWO ADJUSTABLE PIPE STANCHIONS OR CONCRETE SUPPORT PADS. 11. SWING CHECK VALVE FOR PUMPER CONNECTION. 12. 4" DUCTILE IRON CLASS 52 TO FIRE DEPARTMENT CONNECTION. 13. VAULT ACCESS WITH VALVE ASSEMBLY CENTERED IN VAULT 14. CL 52 D.I. M.J. WITH RETAINER GLANDS. 15. POST INDICATOR VALVE. FLOW - PLAN FLOW - -i ELEVATION ACCESS SPR INKLER VAULT P STA I CA" NOTE: ALL UNDERGROUND FIRE PROTECTION WATER MAINS TO BE INSTALLED PER NFPA 24 AND CITY OF TUKWILA GENERAL NOTES: 1- ocCUPANCY TYPE Is R-1 WITH 1 -HR 'TYPE S CONSTRUCTJON . Z. /v11 N/MVMt DEPTH OF SUR`( 4-0"(7YP)=nvi:onmont 3. SYSTEM CONTROL VALVE TO BE INSIDE SLOG. ON RISER. A5SBM8Ly Wl Access TO OUTSIDE-. 4. WA -re R FLO btl Fo R 5TATIC : 1+1 P.S.I. R.E51Qv .... 108 P. w -I. W/ 3/57 G•P M . i►r•• �M�1 ' i 1 . T ..-- ttt- 1 ' 1 w�i ',-r+� ,4"v.t. STA 6+85 S pKie . STUB 8"0 D. 8" SS STUB •B" SS STUB S " 2.0% MIN. M • STA 5+00.5, 10' RT. f 8" 45 BEND (MJxMJ) ....��..1k/ CONC. BLOCKING SS C.O. RIM EL.. 25.90 I.E.. 19.67 5.70 O. Z7 NOTE: ALL CONSTRUCTION SHALL BE IN ACCORDANCE WITH 'STANDARD SPECIFICATIONS FOR MUNICIPAL PUBLIC WORKS CONSTRUCTION' PREPARED BY WASHINGTON CHAPTER APWA, CURRENT EDITION, AND BY THE CITY OF TUKWILA STANDARDS AND SPECIFICATIONS. NOTE 1• FINAL L OCA TION AND AL IGNMEN.Z OF S.SEWER SERVICE CONNECTJON..WILL. PROVIDED BY OTHERS STA 6+14 /4' RT. 8" x 6" TEE (MJxFLJ 6" GATE VALVE (MJbFL1 6" F.K ASSY W/ CONC. BLOCKING UNIT.' 23 N • .1 C' STA 6.07 110' LT. 8" x 6" TEE (M.JxFL) 6" GATE VALVE /MJ.FU 6" F.H. W/ CO BLOC.K1 30 JNI T S rSS cO. RIM EL. - 26. I.E.. 20.88 SS C.O. L. = 26.50 I.E. " 22.88 STA 2.87 8' LT. 8" x 6" TEE (MJxFLJ 6" GATE VALVE (NJJxFL1 6" F.l-L ASSY W/ CONC. BLOCKING ACCL P -TED WITHOUT COMMENTS. • AS NOTED IN RED ❑ PER THE ATTACHED LETTER The drawings affixed hereto have been reviewed and accepted by the City of Tukwila Fire Dept. Additions, deletions or revisions to these :;r ,=wings afAr this date will void this acceptance and will require a resubmittal of revised d .'a v✓j ns. Final acceptance is sua!ect tD fief 9• - inspection by a representative Ot tills depart .lent CITY OF TUKWILA c 575-4407. 22' STA 2+92, 10' RT. SSMH • 2 RIM EL "25.62 I.E • 19.56 SS C.O. RIM EL - 26.50 I.E. • /9.80 A 4, 28' LT. 8 22 1/2' BEND. UNJxMJJ W C C. BLOCKING 1 STA 6.12, 7' RT. 8" 22 1/2' BEND (MJxMJ1 W/ CONC. BLOCKING • 8 'LT. B ND (MJxMJI CK': JG STA 3.12, 7' RT. 8" 90' BEND (MJxMJ1 W/ CONC. BLOCKING EDGE OF RIVE Green Ri$fer 1 Z,c114;„7 ,r.„1! ce..0Ci-d,c, Fire Protecyon Engineers 0 AC TED EPTED AS NOTED RESUBMIT 1:1 REJECTED 1 REVISIONS NO. DESCRIPTION/DATE BY o 111 PE2L34 ICW PROTECTION Lu (f) t6'.‹ kl)45 L1.1 TUKWILA IRE DEPARTMENT Please call 575-4407 - and give s job aNno. e9x1aft a ct JOB NO. DESIGNED DRAWN P.„ E3O WMA N COMP. CHECKED -OF 1991