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HomeMy WebLinkAboutPP - 771 - PROJECT 771 - PERMITS AND PLANSSEGALE BUSINESS PARK PROJECT 771 ASSOCIATED PERMITS NONE OCT 2 6 1977 1 .,TUKWILA FIRE DEPARTMEMwASHINGTON SURVEYING & RATING BUREAU • —.9"444.8"1"6"6"11"4- ..I�.d7iNNi�t.eM.YI .4 r TU1 HYDRAULIC CALCULATIONS KWILA, WASHINGTON 9] For s i= tom. A t_ .-I "1 1 4 e '1•417 = 3o3., 5 — Sheet By Date I0—zf-'I-j • Job No. 3.0 6 Nozzle Ment. & Location Flow In G. P. M. Pipe Size Pipe Fittings & Device Equiv. Pipe Length Friction Loss p•s.i./foot Pressure Summary Normal Pressure NOTES G• Lgth . o — Pt .,35'.. 8/. Pt('�) u•^+ Fit Pe Pv J< : S/. iYG 4- (T) Q 206 .IS' Tot E O Pf - Ci er Pn , .9 lamr) q 34)3 it. C Lgth . 0v 9 Pt .� Y, Y3 pilo) 2 K< 5/.•y'711c Fit Pe Pv (13) Q $ IG1. 1. Tot 1 0 Pf • G`! Pn 3 ' �� q 2 d'$ 9' C Lgth • a 2 o Pt 3'1.1-2— Pdsl) 3' i� 4 i . Q / t Fit Pe Pv 20 co 7/u., Tot 10 Pf . 14 Pn 3 (7) q 2 % . t Lgth 2. `i O 3.16 Pt 3 , l 2- Pc (12 } 3,, . 9 /c, FaV 3.err 17' Fit GC Pe Pv (Z:) Q /0,5.7, 4 Tot .. Pf / i•-11/ Pn (3 L� q /i/ j/ i1,' i � e n Lgth 2 -1 . 6 If 3 .i Pt 1, O 4, • Pit b} 3 . . 1 t= �C'_.t/ Fit Pe 1st. Sy Pv (5 Y) Q7/c( Tot 7 I PE J . J 7 Pn 8 Lgth 3 ' SSV Pt G Z. 37 Pt A V . 4 V Fit a c. Pe • Pv Q2-�/9 J Tot 2.2 PE J.E�G Pn 1,a� i� i q -2.(..3 1 0 Lgth _I ,s ,6at..a.� ' 1 Pt t 3.S' 3 Pt .o r- F•- ..-, -" Ta -r Fit S-1-: Pe 1 .11 Pv Q —' 11`E Tot iL:+ � Pf I ��is Pa 9. Lgth .-3 Z j Pt b 7. 36 Pt -r 3 (v Fit 8(� Pe 2. a 0 Pv/O ,, 61-/"."3:-" Q Z-- 11 1 I 0 Tot 11/ / , 6 111 PE S . v Pn 9 . c _ q -LS i, I v Lgth 1 0 S , O 2 Z O Pt 15. f 6 Pt • T. Fit % et Pe Pv Q 3 `f C Cj Tot 1 7 `I- Pf a 5. 3 Pn q 9 Lgth Pt —78,19 Pt a r 1 2 •• t- .a , .-- Fit Pe Pv Q Tot Pf Pn q Lgth Pt Pt Fit Pe Pv Q Tot PE Pn q Lgth Pt Pt __ Fit Pe Pv Q Tot PE Pn q Lgth Pt Pt Fit Pe Pv• Q Tot Pf Pn q Lgth Pt Pt Fit Pe Pv Q Tot Pf Pn Form 139 AL L INe <1.• For WASHINGTON SURVEYING & RATING BUREAU HYDRAULIC CALCULATIONS cry. Sti.1; l•J, Sheet of 41 By Date '7_ t f Job Na _ Nozzle (dent. & Location FlowPipe in G. P. M. Pipe SueLength Fittings & Device Equiv. Pipe Friction Lou p.s.t./foot Preaure Summary Normal Pressure NOTES 4 i Y 1Lgth q• Pt 350. St 1 Pt (coz' R.// lc S /. ti ye Fit ! /,'.:. Pe Pv 'S (3) O 1 7 6 Tot 6 Pf Pn t- a 7i /.. Lgth .G�a Pt 3 '4 ..' / Pt' F ) Fit Pe Pv O 1(2.- Tot 4— pf — Pn • 3 (j.) � q z $ y . (.. Lgth , 66' 7 Pt 3 Y. $ / N -0N-03 '' 1.,4 £!. ( 1 Fit Pe Pv (io; Q 4.5-0 Tot 1 u Pf • . a7 Pn . i q $.•3 (• Lgth • c` / "'' Pt 3". kk NC ) k 4-7, 21 Fit Pe Pv fi7) 0 73 8.3 Tot 1 0 Pf _ 17 Pn q K' ,U 6 Lgth .u37-- Pt 3 C , a S` NKr) ' Fit Pe Pv (2f Q/0273 Tot 10 Pf .3L- Pn - 3 q 2. 1 v. 3 4 Lgth • .r'S°7 Pt 3s.-37 pt (4) 4• g. r t ' Fit Pe Pv t (".) Q1317.f Tot /0 Pf .. / Pn • %t (700 q 32.41 CTot Lgth Pt 3s- k8 Pt 5 / Z% !c_>_r,s, yr Fit Pe Pv .l. t!32JQi3se S".1.-.,v5?,N Pf ?.4Y Pn 1-1 ` q 1 r 6 1 t- 0 Lgth e 1 .0S1r Pt 3 ? . e'7 Pi Z ) .:..--; T Fit 4 f Pe Pv Q `f3, Tot /3.) Pf 7,C`i Pn q Lgth Pt 4-6. S.s'` Pt !‘.) Fit Pe Pv Q Tot Pf Pn q Lgth Pt Pt _ Fit Pe Pv Q Tot Pf Pn q Lgth Pt Pt Fit Pe Pv Q Tot Pf Pn q Lgth Pt Pt Fit Pe Pv Q Tot Pf Pn q Lgth Pt Pt Fit Pe Pv Q Tot Pf Pn q Lgth Pt Pt Fit Pe Pv Q Tot Pf Pn Form 139 For WASHINGTON SURVEYING & RATING BUREAU HYDRAULIC CALCULATIONS .1 `l 1 Sheet V of By 4- J .t /V //JPL t'1 Date 1 v x"1-1• Job No. u Nozzle Mont. & Location Flow In G. P. M. Pipe Size Pipe Fittings & Device Equiv. Pipe Len?th_ Friction Loss . p-s.i-/foot Pressure Summary Normal Pressure NOTES ez / . g _ Lgth / . ,3 "g y _ Pt 3 3 . % 0 Pt .7 Fit / ,cam Pe Pv - O z Sy, 8 • 3 Tot / G Pf / . J % Pn a Lgth Pt35. Z 7 Pt Al = S'S -7 ? Y Fit Pe Py Q Tot Pf Pn q 3 Lgth / , .097 / Pt 3 3. 2 6 Pt f._ Fit pa 3 O Z B Z') - Tot . / G Pf / • SSS Pn 9 q Lgth Pt, ? IA : / Pt K == '/ 8. 8 / <- Fit Pe Pv Q Tot Pf Pn /eve' ¢ q i Z/1 Lgth / . 302— Pt,3� . ( ,7 Pt 7"-' Fit / Z Pe Pv 0360•4- - Tot 1 3 Pf 3 • 93 Pn q _ Lgth Pt3 4. 1 0 Pt P.11/0: S/•.1 1 G Fit , Pe Pv ti Q Tot Pf Pn q Lgth Pt Pt • Fit Pe Pv Q Tot Pf Pn q Lgth Pt Pt . Fit Pe Pv Q Tot Pf Pn q 3• Lgth 1 , d `I L Pt 3 3.'12 Pt Fit I J Pe Pv N C L 'L Q 7 /. �' 1 Tot i �. Pf 1• si 1 Pn q Lgth Pt 3 ,> . 19 Pt 11 1 r 41. 0 3 f Fit Pe Pv " Q Tot Pf Pn q Lgth Pt Pt Fit Pe Pv Q Tot Pf Pn q Lgth Pt Pt Fit Pe Pv Q Tot Pf Pn q Lgth Pt Pt Fit Pe Pv Q Tot Pf Pn q Lgth Pt Pt Fit Pe Pv Q Tot Pf Pn Farm 139 • WASHINGTON SURVEYING & RATING BUREAU HYDRAULIC CALCULATIONS 1 Sheet k- 014 - By Date Job No. + ai "> Neale Ident. & Location - Flow •` In ' ;` G. P. M.Device �� Sue Pipe Fittings do Equiv. Pipe Length Friction Loss p.s.i./foot Pressure Summary Normal Pressure NOTES :a- j• • ..+ i� }. Z q•• 4 .4s' v ,,, - � ,.Fit �/4 Lgth . I 1 3 Pt Z. 3 .1 l Pt Pe Pv Q'3 1. • • Tot e1 Pf i -c'(7 Pn -YtSru (IP a 31 - o :r - / 1 �Z. Lgth •2.v Pc .Z Y, 3 Pt • Fit Pe Pv ? st 14'.: „ ri i:r: C -) ., :: O 7 e-'0 Tot 9 Pf /. s v Pn . ?'Q ..; , ,.-.4 •:s, • 41 ` t y• N", ;= % Lgth • +3 9C Pt •Z 6. 43 Pt Fit Pe Pv r.. . (-33 O 141.: Z. Tot o Pf �„'}' O Pn • • -.-.---• g r ; , 4:..` -, . +Z Lgth /. x .2-3 r Pt 3 /.. et 3 Pt Fit Pe Pv UU "art °' (7'J Q,'�ef 6/3.' g / Tot / 0 J' Pf .'t li Pn ; ;,- t; : r \ , q »- Lgth • Pt 3 3 7 2- Pt Fit • Pe Pv � . r f , Q Tot PE Pn r :-k�fx- ✓,.. . 7 -. �' : ' / # 9 Lgth •1 0 • , 37Z Pt /9,• til Pt • . 40 ii er f �s Fit — Pe ..f3 Pv • 1.:P �. i.4,317.6 "JP, ' O 3�:3 Tot / 0 • PE 3 . ? � Pn rfc� r _ Lgth • Pt 2 3 •• az Pt Fit Pe Pv , t Q ' 3 ,� . 3 Tot Pf Pn w � .:. 1-1 a A0 Z qt '` 341-0' rr : Lgth s J 8 3 Pt Z 3.7 7 ' Pt • Fit Pe Pv (2.) 01.-1Y. 3L Tot / v Pf /. 8 3 Pn ... _ -: _ • y : wi* O•J q : t� 'fit'x ;: i ' Lgth 1f • S'''' . 1771- Pt .Z. G o Pc .-.. Fit ' .r $ Pe • Po �. , c 3 a Q try. .g Tot / 6•$ Pf 1. e / Pn e`•y-°' - :' ; 4 ��' ry '' q Lgth _ -r .,t Pt 3? . if 7 Pt . • Fit Pe Pv • ., :. Ca./ / S^�'2.. Tot Pf Pn • y 3 I . „ e p . - M1 -4,- •-• g t _3• 1 r3 ¢ Z -e' Lgth / 2 G V Pt 3 3.-7-z- Pt -r Fit 1 2Pe Pv ;.. (7,1 Q z 79.0 Tot / 3 Pf 7, 1 3 pn ,. -.' 4'• q ' Lgth Pt 3 7.1S” Pt /4 -1.S. 773 ---_' Fit Pe Pv sj' Q r Tot PE Pn • q • ,M . Lgth •Pt - - Pt Fit Pe Pr 0 Tot Pf Pn ' ' , " q , ice. a . Lgth Pt Pt Fit Pe Pv •_ Tot Pf Pn •Gini•}i ix:L� ER P;RO T ECTitiel i 0)7`o. ,tel a. l -ons S,-3EET !VO:._. O F_.__ CONTRACT RACT N.O.. 4.-1-511549.8(/) 1;1 4'wG�►r' t_OOaTiON T. Y.LiuA 'xi 1/2-1 10/13/77 . GRINi ELL FIRE . PROTECTION SYSTEMS CO , INC. K GPM H+W= 120 LINE %3.00 39.0 0.00 40.0 8.00 4Q.4 8.00 42-.4 4_'_4 20120.. TOTAL GPM PIPE EOUIV III ET. Ph' /I_ LINE N O.: 4 39.0 /9.0 2. '' ,c, •`i 1.38 w 2.07 %< LINE 8.00 3102 31.2 1,38 8.00 31.8' 63.0 1.38 8.00 34.1' 97.1 1.6:1. 7.82 35.4'" 132. ✓ 1.61 IT LINE SUPPLY PIPE VARIATIONS cc •-3-ertrr 2.47 ,'C SYSTEM NO..�= DATE I t'7' -T.) PAGE NO TOTAL REF PSI PT NOTES 23.77 10.0 1.18 24.95 10.0 4.!Y0 :r ; �O i -2 & 10.0 1.32. 24 1445 ;4 ; - - 3?5 8.0.,)1'4 .6n1 .. .0 .3" . .4:1 12. 55i6.!�8✓ . -2 G. Fiif t- 30.c7 15.21'1'5 :L5.83 18.12 C' 20.53 27.21 3fi3 .13.0 4- J$ 4r5c 3, `"l 4 la 2. 34.1° • • ar p HYDRAULIC DESIGN INFORMATION SHEET NA1,1E•�ra'A : ! : 112/ t"N CX; t k, LOCATION t`.%KLA)11_ 1 1, Ott DATE tO- 1A- ) BUILDING a 1.1 I CONTRACTOR Ce.' 1 V iZo E G" CPs-) CALCULATED BY 13REI W 1GK • CONSTRUCTION: ® COMBUSTIBLE ❑ NON-COMBUSTIBLE OCCUPANCY t.,) A-ikE N D i SYSTEM NO. CONTRACT NO.4(.12AI DRAWING NO. CEILING HEIGHT FT. i 0 W 0 to co ❑ NFPA 13: ❑ LT. HAZ. ❑ NFPA 231 0 NFPA 231C: ❑ OTHER (Specify) 10S e -P? ORD. HAZ. GP. 0 1 ❑ 2 0 3 0 EX. HAZ. FIGURE • CURVE O SPECIFIC RULING MADE BY DATE • AREA OF SPRINKLER OPERATION DENSITY AREA PER SPRINKLER HOSE ALLOWANCE GPM: INSIDE HOSE ALLOWANCE GPM: OUTSIDE RACK SPRINKLER ALLOWANCE zap OQ cirri I -0 SYSTEM TYPE WET ❑ DRY p DELUGE 0 PRE -ACTION SPRINKLER OR NOZZLE. MAKE 7t10k\40 , MODELU� x A 5Peiii SIZE L.O.l .K -FACTOR __E+:Qo — TEMPERATURE RATING •CALCULATION SUMMARY 'f Sr GPM REQUIRED 1A8,1 3 "C" FACTOR USED: i 9. 8S c �, a PSI REQUIRED -1 ? .'5''a'. AT s • ^°'a F.FFSER OVERHEAD 12c? . UNDERGROUND ‘A-0 HATER Fl OW TEST >. DATE & TIME STATIC PSI j RESIDUAL PSI co GPM FLOWING w ELEVATION PUMP DATA RATED CAPACITY AT PSI ELEVATION • JADIK OR RESERVOIR CAPACITY ELEVATION WELL PROOF FLOW GPM - 1 - LOCATION S- Phi kilt* 1%4" GJi..JN SOURCE OF INFORMATION S u'> COMMODITY STORAGE COMMODITY CLASS LOCATION STORAGE HEIGHT AREA AISLE WIDTH STORAGE METHOD: SOLID PILED % PALLETIZED % RACK 0 ❑ SINGLE ROW ❑ CONVENTIONAL PALLET 0 DOUBLE ROW ❑ SLAVE PALLET ❑ MULTIPLE ROW ❑ AUTOMATIC STORAGE ❑ ENCAPSULATED . ❑ SOLID SHELVING ❑ NON- E) OPEN ENCAPSULATED FLUE SPACING IN INCHES LONGITUDINAL TRANSVERSE CLEARANCE FROM TOP OF STORAGE TO CEILING FT. IN. • HORIZONTAL BARRIERS PROVIDED . •r a CUS - TOMER L ly JStw1l�'- 5A2<< ORDER OR CONT. No JOB NAME ,Sf5T E M "E DRAWN BY DATE REVISED BY DATF ttC) Lel FOR MATERIALS AND OPERATIONS SEE SKETCH No. REV. REF. DRW'G. Nos. PIPE STEEL MARK No. SKETCH No. REV 1MIMI*U..S.1. s:_:.F •! r< L.. E:I S Y S T f:: i"'I•I-! `.' ?.:!R i •t t.i !._ :!: ►- FLOW t:::`: i _ Cli L (a'T :': is?i4'.:; • (FOR P:I:i !:t:; ?:N PERIMETER) PIPE F U !:4 •is is i t C. LEN 1 t.. LOSS . � t... ,,, t- ,_..:. ::.,. t -:t F I T T x � ,7 L.. _. I , � ft I... t u S f � r, ,::. , .. I -I r z:• NO (OF'�i)i (INCIH) AND 'EV (FT) (PS:I:/!=T). (P:iI) REF NOTES COUNTERCLOKWISF 37.08 9 1.0..0 6a25 6.0 .00044 .00 37.40 8 8 17f.0 !, .:_y ` 4.0 .00!'")2 .00 37.09 7 7 464=R 6.25 10.0 .00737 .07 37.1.6. 6 753.9 6.25 10.0 .01803 .18 37.34 5 1043.8 6.25 10.0 .03291 .33 37.67 4 4 1334.8 6.25 10.0 .05187 . ;2 38.19 3 1374.4 6.25 66.0 .05475 3.61 4.1.80 2 2 1449.4 6.25 WR 46.0 .06040 2.78 44.58 1 1 1449.4 6.25 yr : 3s . 84.0 .06040 5.07 49.65 16 BULK JCT SPLIT POI:N I. 3 SHEET OF PIPE FLOW !II(? FITTING EO LEN. if LOSS I kES. HYD NO (GPM) (INCH) AND DEV •(FT) (PSI/FT) (PSI) REF NOTES CLOCKWISE 37.08 10 -210.8 6.25 10.4 .00171 .02 37.10 11 -522.6 6.25 10.0 .00915 .09 37.19 11 12 -811.9 6.25 10.0 .02067- .21 37.40 12 13 =-1101.9 6.25 4s('" 13.0 .03638 .47 37.87 13 14 -1141.9 6.2 71.0- .03638 2.58 -40.45 14 15 -1101.9 6.25 -1,--01C..11- 196.0 .03638 7.13 47.58 15 16 -1101.9 6.25 \j:0 57.0 .03638 2.07 49.6: 16 BULK JCT AVERAGE PSI AT JUNCTION 1:S . . . . . . a . 49.65 ICo 10 SPLIT POINT 17 '7'551.3 8.25 27.0 .04447 18 2351.3 8.07 16V 1ALV 21.0- .04941. HOSE= 0 ELEVATION 1 r .PSI r:'y r i_! : ' :.t:l AT F !...:" i-!': E (l 'P i 5.! i G Ci i f ': E t : E: . WITH- 2551.3 ORi !=`LOW:I:N(:i 1.20 1.04 51.89 14.52 66.42 33.5 FT GRINNELL . CONTRACT NO. NAME .7) ;\ t. �J v5( rzA"-,,: LOCATION \--k..) A SHEET N0 4 OF_/ DATE 1 0 -•11 NOZZLE TYPE 8 LOCATION FLOW IN G. P. M. PIPE SIZE FITTING 8 DEVICES PIPE EQUIV. LENGTH FRICTION LOSS PSI/ FT REQUIRED P.S.I. HYD. REF.PT 0 ELEV. NOTES •.1 LGTH. PT FTG. PF Q qt,., TOT ' PE - Q t 0 ITA -VI LGTH. 4.o PTW,0.4z '. t .--M= I7 FTG. 4. 1 PF 1.z4 Or161. 3 TOT. =; ► LGTH. ?:lea 1 .0153 'PTCj't.(Dlp PE Q 142 10 926J= t- SQ1 FTG. 31 152, PF 1. 7111QZ151. Q --'LGTH.. TOT 254 t c? a , ,O PE PT -11.5S . FTG. of —; Q775,. Q _ t c‘/'- 4,-,LGTH. JOT. leo h PE PT15 ..z, 6 FTG. '5?, 0452 PF 2Ao 07,151.3 TOT. PE Q .,-FTG. T= 50 LGTH. t o PT1 y. 43 5r PF 2.�'-► 0Z -151.•;P TOT. t?,=) .0153 PE Q LGTH. PT -11. •t----' ps % QeJ%een fir. cur -%t.1 FTG. PF TOT. PE Q TH. LGTG. - PT `tS- 80 (v,..?,Q A�A‘.. PF TOT. PE Q • 'LGTH. PT FTG. PF Q TOT SPT PE Q LGTH. FTG. PF Q TOT PE Q LGTH. PT FTG; PF Q TOT. PE Q LGTH. PT -. -• FTG. PF Q TOT. PE . Q LGTH. Pr - FTG- PF Q TOT. PE Q LGTH PT _ . FTG. PF Q TOT. PE Q LGTH. PT - - FTG- PF Q TOT. PE a LGTH. FTG. PT PF 0 TOT PE 0 LG H. PT FTG. PF 0 TOT. PE 0 LGTH. PT FTG. PF 0 TOT. PE PT GRIN; E L. -PRY_ P- ;WTECTWN SYSI7E JS CO., 13C. i ri Calculations . SHEET CONTRACT T NO 114-3/5(.08(01) Fti ?1(O '1'1 l SYSTEM NO.. LOCATION TUU ILA WA DATE t C}` t"'> -~}i HYDRAULIC FLOW CALCULATIONS BRANCH LINE NO. 1 (MOST REMOTE BRANCH LINE) SHEET OF PIPE FLOW DIA EQ. LEN FR LOSS PR S. HYD NO (GP M) (INCH) (FT) OSI/FT). (PSI) -REF NOTES COUNTERCLOCKWISE 37.05 9 101+0 6.25 6.0 .0004 .00 75.0 37.03 8176.0 6.2 5 4.-0 .0012 y.00 288.8 37.09 7 464.8 6.25 10.0 .0074 .07 289.1 37.16 6 753.9 6.25 10.0 .0180 .18 289.8 37.34 1043.8 6.25 10.0 .0329 .33 291.1 37.67 1334.8 6.25 10.0 .0519 .52 39.5 38,19 1374.4 6.25 66.0 .0547 3.61 75.0 41.80, . 1449.4 6.25 .46.0 .0604 2.78 44.58 CLOCKWISE 9 SPLIT POINT 8 Q =12.31 XSORT (37.08) = . 75.0 7 0=47.43XS0RT (37.09)=2038.8 6 0=47.43XSORT (37.16) =289.1 5 0=47.43XSQRT(37.34)=289.8 4 0=47,43XS0RT(37.67)=291.1 3 '0= 6.40XS0RT (38.19) = 39.6 o=11.60XSORT(41.80)= 75.0 BL 1 --PCN JCT 37.08 9 SPLIT POINT 10 210.8 6.25 10.0 .001.7 .02 711,8 37.10 10 0=51.2OXSORT(37.10)•---311.3 11 522.6 6,25 1.0.0 .r':)t'::''. :09 209,2 3I.19 1.1. q:_:.4%.43 Ol T(37.19) 289. 12 011.9 6.',5 10.0 .0207 .21 1101.9 290 . 1 - 37.40 12 0=47. 43XSO T (37.40) -290.0 13 6 .25 13,0 .0364 .47 37.8: 13 Et._ 1 --SCM JCT GRINNELL FIRE p; E ..i:Gi SYS irzMS Ca, MC. SHEET NO. 0 F_2_ Alylalt Calculous CONTRACT NO. i•�l-9(AA(0' Fri NAME SEL PA t4, LOCATION MY. i'tJ I L/ -'c JJA GRINNELL FIRE PROTECTION SYSTEMS CO. v INC 10/12/77 17:06 TOTAL K GPM GPM SYSTEM NQ.. DATE t4`t -T) PIPE ID EOUTV PAGE NO TOTAL REF FT PF/L PSI PT NOTES H+W= 120 LINE NO. LINE 23.77 A 9.00 39.0 39,0 1.39 10.0 1.18 24.95 8.00 40.0 79.0 1,61 10.0 ' 2.05 27.00 8.00 41,6 120.6 2.07 10.0 1.32. 28.32 8.00 42.6 163.2 2.07 ►r 12.0 2.77 31.09-,,, LINE 23+77 8.00 39.D ---39.0 39.0 1 .6 ]: 10.0 .56 24.33 9.00 39.5 78.5 1.61 10,0 2.03 26.36 8.00 41.1 119.6 1.61%t (67J 7.07 33.43 LINE SUPPLY PIPE VARIATIONS 47.43 288.8 2.471T :L3+0 3.65 ` 37.09 G C?NNEL L F!; P?O TEC T ?ON S TSri!S co., INC. • SHEET NO. NE y33a1i c Calculations alcu atiom CONTRACT NO. 11.5'1549M AYE NAME SE ,c E i!;j9t3,' /. PAy_;:,„ KG'S) } LOCATION T, Wa ILA GRINNELL FIRE PROTECTION SYSTEMS CO.,INC. 10/13/77. 26:20 SYSTEM NO_ . _=) DATE l C3~ i, •7e) TOTAL F'IF'E EOUIV TOTAL_ REF K GFII GFH ID FT PF/L_ PSI PT H+W= 120 LINE NO. LINE 23.77 A 8.00 39.0 39.0 1.38 10.0 1.18 24.95 8.00 40.0 79.0 1.61 10.0 2.05 27.00 8.00 41.6 120.6 2.07 10.0 1.32 28.32 8.00 42.6 163.2 2.07W 14,5 5 3.35 31.67 LINE 15.21 f.5. 8.00 31.2 31.2 1..38 . 8.0 .62 15.83 8.00 31.8 63.0 1.38 8.0 2.29 18.12 8.00 34.1 97.1 1.61 8.0 2.41 20.53 7.82 35.4 132.5 1.61 .r 12.5 6.68 27.21 LINE SUPPLY PIPE VARIATIONS 51.20 306.1 2.47 •t 13.0 1�- FA�so a 4.07 35,74 L� 5 L ►1`3'UKWILA FIRE DEPARTMENT • 1t.....' 4400ende 'ev P k .,.:a. TUKWILA, WASHINGTON 98188. For OCT 2 6 1977 WASHINGTON SURVEYING & RATING BUREAU HYDRAULIC CALCULATIONS S.6 G4Lt { i' 2- S' Sheet By Date Job No. NozzlsFlow !dent, & Location PiPe Size Device Friction Lo!! p.s.i./foot Pressure Summary Normal Pressure NOTES JE 1+ 7 q Lgth 1 lAi Pt 3Z . S 4 Pt 10 Z jZ K ,,t Pe Pv PL. P ,. s r F...3 �,+(/� A 0 J-11-,7 _ S Tot 1 0 , ,i:. 3 Pf . o j Pn K=yam.1 O / (Gi 2'/ -Sr .S Lth Pt 32.5 Pel( 42, ,"%a 'I ° . a 0 4/1. 5 Fit o 1 S Pe Pv te Tot 1 Li Pf . 1 � Pn �...c / q 'Z y, . `/ Pt )' 2 . 72 Pt 1 "L 1 z•-• , Fit Pe Pv C. Q GL% >. Tot 1 0 , "31' Pf ,3 Pn G. 0.7. �-,�8 q ?3 .. i c L ch . 4' . Pt 5' 3• u7 Pt 1 3 ' L %z_ 2 N Fit Pe Pv t_. t_ Q 7O /. 41 Tot I u Pf . 4. L Pn z 1/1. 1 to r 3 ��-/ Lih.'j) q 1 `! ,y 5- Lgth $ 3 .0 iO'/ Pt 33.E 1 Pt 14 4/./4/ .. . b V,, Ce.Z'�� Q //".0.) TIME',/Ill PE 7,../y Pn • • q 6 Lgth .5 / •, 036 3 Pc 4/. ? Pt 1-S T. Fit 1 0.1 Pe Pv O // v U Tot (n %. 1/ PI 2...q..( Pn q 6' ?it 6 Ptri/ Y y 7) Pt I Fn ____./4✓L; . Pe 4 v. s-7 -po----- Q / 7/ fly Pf s—, / 7 Pn q it U ,` .1 Lgth 2.. • (`r `/ Pt 4 9_•7' . Pt0hl T-o,i;�.•r„ 3 3, 8 E4 Fit Pe / `/ . -,' Pv - Q Z S 3� Tot L Pf /, l '� Pn q g Lgth 2 ' Y 7 Pt (S • Y 7 Pt y . (, V Pe Pv , Q L 3" 7 Tot 2. Pf / i v 3 Pn = J J Lgth , •,' /1-/ /7 7 Pt 66, r(.! Pt Pe / , 1 3 Pv T Q 2131 Tot / Pf / ,' / Pn q 1 -' Lgtb%'-, 0 / `// / Pt -1v• u4. Pt %L/.,... c.t. i' ► C Fit ZiL I -e Z,o h Pv /c, ' Q 2- -/ _i I Tot -r S 4 Pf 4 , 6 5 Pn 0/ :, k �. q 1 S u L tli: i d !. c " • Lf Pt / G. % Pt Pe Pv Q i '1 ,i' I / ✓ Tot / 7 ." Pf . I. i Pn 9 Lgth Pt 11 . 7 Z Pt R r / Z ' 11- '•' ( _ ...........-- Fit Pe Pv 0 Q Tot Pf Pn qFit L: th Pt Pc Pc Pv Q Tot Pf Pn Form 139 •1. 519 For WASHINGTON SURVEYING & RATING BUREAU HYDRAULIC CALCULATIONS Sheet 2— of By tate Ica/z.iri7 Job No. Nozzle !dent. & Location FlowPipe In G. P. M. Pipe Sue Fittings & Device Equiv. Pipe Length Friction Loss p.s.i. foot Pressure Sunaxnary Normal Pressure NOTES ). Pt or F.--.... _ Lgth Pt 3 2 . `' Pt O °% 72A- ..-. .. Ic 4 ,t z • Fit Pe Pv Lq ..ie t 2 ` O 70 S Tot ✓ v _ Pf Pn ", 2 .i -i •1 5- Lgth ,u'a't Pt - 2- • ; `t Pt"4 ? K -- y' .' Fie pe Pv '(1 0314.1 Tot /U Pf • - Pn 1 3 q• 2 3c, I ( Lgth . 02 s Pt .32.6S Pty K Z elf , I G . Fit Pe pv (/q) Q Syct•F Tot i" Pf .Z‘''' pn I ;' 134.0 ! Lgth . ' '-/ ? Pt 3 f' pt' � k- 4I ,, 2 Fit Pe Pv r 2 °I Q 7, C. e Tot ' J pi . "eA Pn 1 / q % •Y 7. 1 Lgth • .._ Pt 33, 3 e Pi4) Fit Pe ' Pv C' i 0/:133.% Tot / J Pf . .) Pn rI�. q ? S • 7 S Lgth L . 1 1 if 7 Pt 3 tet. G Pt S ) •-r 7 , e -t -, . >. C Fit .} . I _/ Pe Pv / 1�?ZJ / 2 Pr.? Tot 7 . r Pf c? S Pn q 6 Lgth S 7. d . 6 `/ci3 • Pt 3,i • 0 / Rif ) G. re- Fit lo• Y Pe Pv Q /I7Y.3 Tot Gly PE 3„ 2G Pn c. ,-. F"...., w q % Lgth G y . G/ fj 3 Pt 3 g..2 7 Pt( 3) L .—c= Fit / a • y Pc Pv Q . 74 0• Tot 7 it..r Pf /. 36 Pn q S . Lgth/•7S 0 . 0YS3 Pt 3 5,..6 3 Pt( 7 ) (?.)S)'G Fit •/o.Z Pe Pv i Q 76O Tot / ?.!. Z Pf 8. 39 Pn q G Lgth zi 0 . O /g 3 Pt l5J . 0 2_ P(1) 7e t' °`' j n L_7?F r Fit vs. y Pe Pv Q 1 (j o Tot 5 S-. `i•- Pf l'"6-17 Pn btfli q Lgth • Pt 41 e s9 Fit Pe Pv PE Pn q J Lgth 3 P ,02 3 Pt 37-2 7 Pt (4 7- Fit Z S .6 Pe Pv . Q S.. H Tot d•(•• . '. Pf /. 5'' / Pn q 7.5* J.- Lgth • i `'u .• 0 2-9 Z Pt .3 /.. 7g tt Pi. . / bit. Fit Pe Pv Q .599 Tot / o o Pf 2 . G/Z Pn q 7 Lgth .37 •O 317 3 r t 2.. 7b Pt LJ T Fit 2 F • t, Pe Pv Q 67 `/ S Tot i• ' • %. pf Z.3' Pn Form 139 /4) For WASHINGTON SURVEYING & RATING BUREAU HYDRAULIC CALCULATIONS Se1 Sleet Date ,177 . job No. Nozzle !dent. & Location Flow In C. P. M. Pipe Sue Pipe Fittings & Device Equiv. Pipe Length 8 Friction Loss ps.i. foot Pressure Summery Normal Pressure NOTES q Lgth 3. 8 Pt 2 7. a 4 Pt T Fit / v Pe Pv • .w4- 7(3' co /2o. (0 2 • Tot ' 3. 8 . /33 Pf /.SY pn Lgth Pt Z V . * 5' Pt CI 0 Fit Pe Pv Tot • Pf Pa q Z Lgth G C. Z Pt 2.1 .0 O Pt --- Fit 1 V Pe Pv 1,44: / (3) co 1_.).(.. Tot 1 G• 1.- .133 Pf Z.•Y Pn 9 12 1 .3 t 211- Lgth 1 Pt 2.S . r J Pt T" Fit 1 7 Pe Pv - %-4--_1 (G) Q 2j L. r1 Tot t 3 .1. 0-3 Pf -2.4.5/ pn --\_____ . � 1yPe'Z.---•tip Pt 3/.7? Pt kZYz = .Lt Z.`Io .... .----..„41.Lgth v. -N._ Q -. ...--‘_----N._. Fits....... -1 i1 -Py Tot Pf Pn q Z " Lgth 3 •133 Pt 2.1 .0 ° Pt --r Fit 1 Pe • Pv i 3 Q 12 u . (, Tot 13 Pf 1.1 3 • Pn q Lgth Pt 2i.73 Pt Fit Pe Pv Q . Tot PE Pn q Z Lgth " 7 •133 Pt L 7. o co Pt 4-- Fit 1 u Pe Pv �y. Q fL...L Tot /7 Pf •2.ifi pn q 1 L3. V 2t/3- Lgth 1 ,2.uStt Pt 2" y. 81 Pt Fit / Z. Pe Pv 3 -9 (G) Q 2`13.4. Tot 1 5 Pf 2.Z/ pn q Lgth Pt 32. S( Pt k7 %L z Qt.e!/ Fit Pe Pv Q Toi " Pf ----Pnr----- _. 9 7- Lgth 1. 2 .1LSPf Pt 2 1. 65 Pt `r Fit t .. �— �=r o Pv L �-� g. Q11G... Tot II.L 2y.°1 Pn 9 Lgth s .: I Z Pt z -► . 4.S Pt -r Fit I o Pe Pv LI•'`' 2- Q 1IC-t Z Tot /a. h Pf Z. Pn L.....^.17 ti /40•1 q 11P,y Lgth 1 Pt _� u . •o `1 Pt i 7 Fit 1... Pe Pv Q - c: •I. ., `.', Tot I . 1 c1 1. Pf L• 4 u Pn 9 Lgth Pt 32•x./ Ptlt... 41. 1L1 Fit Pe Pv Q Tot Pf Pn Form 139 HYDRAULIC DESIGN INFORMATION SHEET NAME 3ZAL.E E..��.,tMEr.S PA(I.tc -- P2os` "Y)1 LOCATION -TUKL)I LAS WRSH-t . GUI LDING DATE 10 -t3 -'Yl SYSTEM NO.... 4 CONTRACT NO.4t .2G�LAl CALCULATED BY Gam. c32CIWIUC_ Ld RCN TON DRAWING NO. "..a CEILING HEIGHT FT. CONTRACTOR &et ON EU Pt P.c F t o i E Crl flN CONSTRUCTION: .O COMBUSTIBLE ❑ NON-COMBUSTIBLE OCCUPANCY L.1Air=1-1DUSE z 0) • w 0 ❑ NFPA 13: 0 LT. HAZ. O NFPA 231 0 NFPA 231C: O OTHER (Specify) ORD. HAZ. GP. FIGURE Q 2 Q 3 CURVE EX. HAZ. O SPECIFIC RULING MADE BY DATE AREA OF SPRINKLER OPERATION DENSITY y AREA PER SPRINKLER HOSE ALLOWANCE GPM: INSIDE HOSE ALLOWANCE GPM: OUTSIDE RACK SPRINKLER ALLOWANCE 514,00 i c ton SYSTEM TYPE el` WET Q DRY ❑ DELUGE [J PRE -ACTION ' SPRINKLER OR NOZZLE MAKE ((1-10ONFZt MODEL GoR.A f)47-7613 SIZE 11/32 .K -FACTOR _.. TEMPERATURE RATING RATING t �S CALCULATION SUMMARY - 344 - GPM GPM REQUIRED451""4 PSI REQUIRED 'r.t • AT EAPAROPAPHeiiiR . "C" FACTOR USED: OVERHEAD %-7-'a UNDERGROUND 1 AA) w -rt." L -L. ' /t'.. ". yalg Ft OW TFST - >. ! DATE & TIME • ! STATIC PSI j 1 RESIDUAL PSI 1S"430 A'JAtt- '1> GPM FLOWING to ELEVATION H - 1 LOCATION -7.'6 - 8v = - SOURCE OF INFORMATION PUMP DATA RATED CAPACITY AT PSI ELEVATION TANK QR RESERVOIR CAPACITY ELEVATION WELL PROOF FLOW GPM PSi &tiAtL AT(' r.N TtcNJ • STORAGE METHOD: SOLID PILED O I -- co O I Y sp ! 0 < FLUE SPACING IN INCHES Er O • '; • LONGITUDINAL TRANSVERSE I COMMODITY ' CLASS t STORAGE HEIGHT AREA % PALLET! ZED LOCATION AISLE WIDTH 96 RACK O SINGLE ROW 0 CONVENTIONAL PALLET Q DOUBLE ROW ❑ SLAVE PALLET MULTIPLE ROW ❑ AUTOMATIC STORAGE ❑ ENCAPSULATED . ❑ SOLID SHELVING ❑ NON. - O OPEN ENCAPSULATED CLEARANCE FROM TOP OF STORAGE TO CEILING FT - IN. - HORIZONTAL BARRIERS PROVIDED CUSTOMER 5£ &AL.e - # 4 ORDER OR CONT. No JOB NAME 1• v II 3t.5 mAio 1(3 t 1, Sri 4. a 12�4,s 0 ®1-m7 2 ), e ►o r 71.3 o r 311' ®P s=s.g 0. t Iliov 1,3 vF- DRAWN BY DATG REVISED BY DATE FOR MATERIALS AND OPERATIONS SEE SKETCH No. REV REF. DRW'G. Nos. PIPE STEEL MARK No. SKETCH No REV P U�TDIN u.s.*. Cs`11NNELL FrIE P OTECT CN SYSTEMS CO. INC CO -ons SHEET NO. 3 OF\ 41 - CONTRACT COtiiRACT NO 1.1-1461.ia NAMF: 62)",-V.5. , ►'± � .'�ys .« P; OI I SYSTEM.Na LOCATION .11-31(1,J% "� 11-1/4.9.4 DA 4:&-'7" • #. • PIPE PIPE FITTINGS EQUIV F' S 0 IN DELTA NO. DIA. INCLUDED LENGTH L L :GPM P PSI 1 6.25 tr 75.00 1 0 • 766.0 1.39 2 5.19 2org 195.00 1 0 766.0 8.95 3 6.25 64.00 1 0 766.0 1.19 4 6.25 57.00 2 0 1278.6 2.73 5 5.19 t wily 11.50 2 0 1278.6 1.36 6 5.19 • 10.00 2 0 1029.9 .79 7 5.19 10.00 2 0 784.0 .48 8 5.19 10.00 2. 0 .548.8 .25 9 5.19 10.00 2 0 314.4 .09 10 5.19 10.00 2 0 71.3 .01 11 5.19 10.00 2 0 -171.7 .03 12 5.19 10.00 2 0 414.8 .15 13 5.19 10.00 2 0 -658.5 .35 14 5.19 10.00 2 0 -894.0 .61 15 5.19 I L -TE . 93.00 2 0 -1131.5 8.78 16 6.25 57.00 2 0 -1131.5 2.18 17 6.'7'5 V.( 59.00 1 0 -1794.1 5.29 18 5.19 tr. 66.00 1 2 •-512.6 1.44 19 .5.19 100.00 1 2 -587.6 2.81 20 5.19 't 65.00 1 2 -662.6 2.28 CONTRACT NO 41.11-16110:3, NAME 6./:'31.1 L PA -- PROI LOCATION akt (YAW 12.,0: 1......0A.$14 SHEET NO. k OF ± SYSTEM NO.. DATA 10-agw�� SPRINKLER -SYSTEM HYDRAULIC FL_C)W CALCULATIONS (FOR PIPES IN PERIMETER) . • PIPE FLOW PIPE r.11. !'-PIPE r-'ri:l:C:1'IUN REQUIRED HYD VEL NOTES NO. :N DIA. AND EQUIV. LOSS PSI PSI REF FT/ GPM DEV, LENGTH PER FOOT F'T. SEC. 34.75 ►0 11 -171.7 5.19 10.0 .00289 .03 2.6 2.4% t 34.78 11 K-41.1.3 12 -414.8 r 5.19 10.0 .01475 .15 6.3 2,13. 1 34.93 I . k. 4 t.2.3 13 -658.5 5.19 10.0 .03469 .35 10.0 Z35. 35.27 I K• 3qo o 14 -894.0 5..19 10.0 .06108 .61 13.6 23'I. S 35.88 '4 K= "..1.-7 o 15 -1131.5 5.19 1L-1- 93.0 .09445 8.78 17.2 44.67 15 16 -1131.5 6.25 57.0 .03820 2.18 11.8 46.8:, to 17 -1794.1 6.25 if 59.0 .08963 5.29 18.8 5?.13 11 34.75 to 10 71.3 5.19 s, 10.0 .00057 .01. 2.42). 1 34.76 9 K = 41.2'3, 9 314.4 5.19 10.0 .00884 .09 234.4 34.84 8 K: .10 8 548.8 5.19 10.0 .02477 .25 2;5.7, 35.09 1 k= 39•'19 784.0 5.19 10.0 .04791 .48 .. 11,9 -,16.1 35.57 t. Kt '4-t.2'S 1029.9 5.19 10.0 .07936 .79 15.6 PIC -7 36.36 5 K- 41.2.3 1278.6 5.19 . 1Vng 11.5 .11841 1.36 19.4 37.73 4 1278.6 6.25 57.0 .04790. 2.73 13.4. 40.46 3 64.0 .01.856 1.19 8.0 41.64 2• 2 766,0 5.19 2cTE. 195.0 .04589 8.95 11.6 /� 50.59 1 1 766.0 6..25 IT • n.0 .0.1.856 1..39 8.0 51.99 rl _ruh7_ P:1 i':r JUNCTION L . . . ► . .. . 52.06 11 TOP CF K tSCR.v - 21 25A0,1 `:; ::_'5 27.0 .04475 1.21 15.4 5T.2 7 22 2560.1 8.07 t Aw 2:L.0 .04983 1.05 16,1 1 c,./ 54.31 1.1 4.8 3 766.0 6.25 HOSE= 0 ELEVATION HEAD IN PSI 13 . . . • . . . . . 14.52 3 3. SFT PSI REQUIRE:.! ;,.i..i' FLANGE ANS ►-c : IGOT PIECE. . . 68.34 ..s--- E..YMD OF- GRINNELL • CONTRACT N0. NAME LOCATION %`1rk r I 14. SHEET N0 .__..OF DATE '47'4, r 7 1 NOZZLE TYPE 8 LOCATION FLOW IN G.P.M. PIPE SIZE FITTING 8 DEVICES ----1711.7"---I. PIPE EQUIV. LENGTH FTG. FRICTION LOSS P.S.I./FT REQUIRED - P.S.I. PTTo. .6.4 HYD. REF.PT 0 • a-, ELEV. . NOTES _ Qz,0.I PF ► 0 200 TOT. PE Q cF = 1-4 t..GTH.4 o PT 1.$u -N--- t'� A�V- ar"' KtS . 1p I1-cF-t't f'TG. 4l , PF t,25 02.100. I TOT o ( Di �}{ PE ._. Q^ -_---- t'r39 _GTH.`io-- PTlo.c^41 t o. 7-1G. AI PF i.qct 027co: TOT. Maq ' 0t54 PE Q — ...GTH. %_,oo PT 12.� FTG. , o (G4 PF /.54k Q2Z \C) ;OT. to D ' PE Q , -tot:. 4s ...GTH. PT1'�.� 7.r, U, . TG. -67.-_-, O Ifcj PF 'L4 I QZ?(00.+ 90 8 TOT. PE o-- to rr''' LGTH.lQrj 0 (64 PTi<fl.c3 • ' FTG. �� PF 2.0 � 027! 1411Nti4LL H {,`. •P OTECTEC?i. SYS CONTRACT NO.44iAttSto. 34ii r`t�►j� 5 AL►. t21) 1 5 , ,-- %RO LOCATION 1 0 11.0.14 L g 3' s1 GRINNELL FIRE PRO'T'ECTION SYSTEMS 10/14/77 16:17 TOTALi PIPE _EOUIV K GPM GPM ID FT WW2: 120 LINE NO. .\-`1 LINE (3.00 39.0 R.00 40.0 8.00 41.6 LINE 8.00 8.00 8.00 39.0 40.0 41,6 39.0 79.0 120.6 39.0 79.0 120.6 1.38 10.0 1.61 10.0 2.07 0( 160 1.38 10,0 1.61 10.0 2.07 If 14.0 LINE SUPPLY PIPE VARIATIONS 42.90 241.7 2.47 13.0 2.63 31.74 141.23 241.7 2.07 yr 11.0 5.26 34.37 ��q`tditcji-L SHEET NO.0 F14 SYSTEM Na DAT -E PAGE NO TOTAL REF PF/L PSI PT 1.18 2.05 2.11 1.18 2.05 1.85 23,77 '• 24,95 27.00 29.11 G- 23.77 24.95 27.00 28.85 NOTES • GRINNEL FIRE P OT CT ON S?SirdS CO., INC:. ' y,ira3311 Czic 3`%13o31s SHEET NO .2.0F I± CONTRACT NO.41.11.56.-4141't NAME 6 L` .ilNVZ° 5 PAi . --PRO'S 111 SYSTEM N0_ _ 44. LOCATION -i:4.J I , d 5314; 10/14/77 H+W= 120 LINE 7.82 8.00 8.00 DATE. ' `I "` / GRINNELL FIRE PROTECTION SYSTEMS CO. , INC. 16:26 TOTAL PIPE EOUIV GPM- GPM ID FT 35.4 39.0 42.1 LINE NO. - 35.4 74.4 116.5 1.05 9.0 1.38 10.0 2.07' IT 1.3.0 / q , :PAGE NO TOTAL REF PF/L .PSI PT 3.36 3.89 2.11 Z.3 r NOTES 20.44 23.80 . 27.69 29.80 LINE 20.44 7.82. 35.4 35.4 ' 1.05 9.0 3.36 23.80 8.00 39.0 74.4 1.38 10.0 3.89 27.69 13.00 42.1 116.5 2.07 tf 1.61 29.30 G L1 1►.'+- I. •-+ 0 • LINE SUPPLY PIPE VARIATIONS 41.19 234.0 2.47 13.0 2.48 A39.701 -234.0 234.0 . 2.07 rt 11.0 4.95 CUSTOMER`7`it%I^� 4 ORDER OR CONT. No JOB NAME 8,, I4 DRAWN BY DAT' REVISED BY DATE FOR MATERIALS AND OPERATIONS SEE SKETCH No _REV REF. DRW'G. Nos. P1 PE STEEL. MARK No. SKETCH No. REV 'IMMIX U.S.A. Us -Malt. t-4.1 MOTECTiUti b7Sk,N?S I)(1., MG. El arauii C i c a zi on SHEET N O. O F' tai CONTRACT NO.'41.147.Stti? a;3 Ai NAVE 6 ? L JI S' PAM.- P O 111 1 ' SYSTEM NO_. , . LOCATION 1' _ . ,x3 Ito AS DATE 104.e_'17 11 RA. 2 NAl HARtIY-CROSS HYDRAULIC FLOW ANALYSIS (FOR ALL PIPES IN THE SYSTEM) PIPE 731A FITTINGS EO LEN NO (INCH) INCLUDED, (FT) 1 6.25 1I 2 5.19 2� 3 6.25 • 5.19 \T 5 5.19 6 5.19 7 5.19 8 5.19 9 5.19 10 5.19 11 5.19 12 5.19 13. 5.L9 14 5.19 15 5.19. s T 16 6.25 tT 17 6.25 18 5.19 1.t./1.7 19 6,25 20 8.25 21 8.07 • FLOW FR LOSS FR LOSS (GPM) (PSI/FT) '75.-00 1 0 774.2 .0189 195.00 1 0 774.2 .0468 64.00 1 0 774.2 .0189 11.50 1 2 1350.1 .1310 10.00 1 2 1101.5 .0899 10.00 1 2 856.0 .0564 10.00 1 2 568.6 .0264 6.50 1 2 282.4 .0072 3.50 1 . - 2 207.4 .0041 10.00 1 2 -34.9 .0002 10.00 1 2 -277..3 .0070 10.00 1 2 -519.8 .0224 10.00 1 2 -763.1 .0456 56.00 1 2 -1052.0 .0825 47.00 1 . 2-1.127.0 .0938 65.00 . 1 0-1703.0 .0814 57.00 2 0 -576.0 .0110 195.00 2 0.-576.0 .0271 57.00 2 0 -576.0 .0110 27.00 2477.1 .0421 .21.00 2477.1 .0469 (PSI) VEL. -(FPS) 1.42 8.1 9.13 11.7 1.21 8.1 1..51 20.5 .90 16.7. .56 13.0 .26 8.6 .05 4.3 .01 3.1 .00 5 .07 4.2 .22 7.9 .46 11.6 4.624.41 17.1 5.29 17.8 .62 6.0' 5.28 8.7 ..62 6.0' 1.14 14.9 .98 -.15.5- - • 14. I< 2 KA*,) : `> irt c1 rSYSYrq• "YD^ Ai,, :•=i)hCALCULATIONS f CFPIPES IN. PERl`E1j • PIPE FLOW DTA FITTING E+! LEN FR LOSS PRES. HYD NCS (GPM) (INCH) AND DEV (F -""T) .(;"':r:i./I=T) (PaT) REF 1'lJTES COUNTEPCLOC KWISF 9 207.4 5.19 8 282.4 5.19 7 568.6 5.19 6 856.0 5.19 5.-.1101.5 5.19 1350.1 5.19 3 774.2 5.25 :? 774.2 5.19 :l 774.2 6.25 :34.52 3,5 .00409 .01. 34.53 6.5-, .00724 .05 34.58 10.0 .02645 .26 34.85 10.0 .05636 .56 35.41 10.0 .08986 .90 36.31 11.5 .13095 1.51 37.8:L 64.0 .01893 1.21 39.0:.3 195.0 .04680 9.13 48.15 75.0 -.01_893 1.42 49.57 D or 4 d SHEET -OF PIPE FLOW DIA FITTING E0 LEN FR LOSS PRES. HYLI NO "-WPM) (INCH) AND DEV (FT) (PSI /FT) CPS I) REF NOTES CLOCKWISE 10 -34.9 . 5.19 11 .-277.3 5.19 '12 -519.8 5.19 •13 -763.1 5.19 14 -1052.0 5.19. 15 -1127+0 5.19 16 -1703.0 6.2.5 34.52 (' SPLIT POINT 10.0 .00015 .00 34.52 .G 10.0 .00700 .07 :34.59- 10.0 4.59 10.0 .02240 • .22 34.82 1- 10.0 .045 57 .46 35.27 AS 56.0 .08254 4.62. 39.89 L 47.0 .09375 4.41 44.30 65.0 .081.39 5.29 49.59 'p 11 AVERAGE PSI AT.'UNCT:i:ON 7:6 . . , • . . . 49.58. 17 20 2477,1 8.'15 21 2477.1 8.07 2.7.0 .04210 1.14 50.72 21.0 .04588 .98 51.7() HOSE _= 0 ELEVATIO,! HEAP IN. PSI IS . . . . PST PEOUIRE[r AT FLANGE AND Sp:WOT• PIECE., WITH 2477.1. GPM FLOWING • 14.52 • 66.22 BULK JCT .�-- TOP CF I2.J44:72 33.5 FT s /tS-,e. of tZts GKfNNELL - CONTRACT NO. NAME Gam= e A 1. t_ W) LOCATION 1\1 1 r - SHEET NOI <OF . [ DATES 4 - RA NOZZLE TYPE B LOCATION FLOW IN G.P. M. PIPE SIZE FITTING 8 DEVICES PIPE EQUIV. LENGTH - FRICTION LOSS PSI/FT REQUIRED P.S.I. HYD. REF PT 0 ELEV. - NOTES- 0Lem.I LGTH. PTCo:a,IA. --' FTG. PF 1 fak-V, 0 Soo .TOT PE 1 0 Mr zA- LGTH. 44, PT ld..o.'L2 FTG- -4 t PF 1. pr- SG 02101/.1 ICJ t, = t1 : TOT. t 'ol-1-C° PE of R�e 0 - O `° 0 \ d 11r- 2,,k LGTH. ct PT 6.-7. a FTG. 3°1 PF I, $ �' 0246-71./ CI `TOT t7 9 LGTH. lco ©E 4.(a , °I i"'''' 0 3 ,614,40 PE PT 6.1.2.2, FTG. — PF t•4co 0 ?. 17. r 0 4 l c.v. 5 JOT. tb© LGTH. PE PT 10.7 4 96V/' v FTG. r.33 PF -z.ie Q t,7 . i 0 ri-� TOT. t.GTII. 1 c's PE PT -77. 94. FTG11 PE I' 02°77•! TOT.' MG 0 LGTH. PT7 4, 5 -F kr C..—o,—t.): PF Ta cart tIAI4 Q TOT PE • 0 LGTH. PT 15 . ao py /w f t t-. FTG. PF Q TOT PE 0 LGTH. PT . • FTG. PF Q 0 TOT LGTH. PE PT FTG. PF 0 TOT PE 0 ' LGTH. PT FTG: PF 0 TOT. PE 0 LGTH. PT •.. - FTG- PF Q - TOT. PE o LGTH. PT • rt 6 FTG- PF 0 TOT. PE 0 LGTH Pr - FTG. PF 0 TOT. PE 0 LGTH. PT FTG- PF 0 TOT. PE o - LGTH. PT FTG. PF 0 TOT. PE 0 LGTH. PT FTG. PF 0 TOT. PE o .LGTH. PT FTG- PF 0 TOT. . PE PT Gr13?i `t.EL ; FIRE P OTECT CN SYSTEMS CO., IN E y r ii tic Cz;caalatio s CONTRACT N O.41. : Sts' to NAM S ALE. 005INIZS5 PARA- PRO'S 111 LOCATION altinWit0AL.COAcag PIPE FLOW NO (GPM) • •HYDRAULIC FLOW CALCULATIONS• BRANCH LINE NO. 1 (MOST REMOTE BRANCH LINE) DIA EU LEN FR LOSS PRES. HYD (INCH) (FT) (PSI/FT) (PSI) REF COUNTERCLOCKWISE 9 207.4 75,0 8 282.4 .286+2 7 568.6 287.4 6 856.0 245.5 5 1101.5 248.6 4 1350.1 CLOCKWISE 5.19 3.5 +0041 5.19 6.5 .0072 5.19 10.0 .0264 5.1.9 10.0 .0564 5.19 10.0 .0899 5.19 11.5 .1310 34.52 .01 34,53 .05 .34.58 .26 34.85 .56 35.41 .90 36.31 1.51 37.81 SHEET NO. J . OF 1 SYSTEM NO.. 4 DATE 10-__"11 HA2 SHEET OF - NOTES SPLIT RUINT 0=12.77XSQRT(34.5)= -75.0 c O=48.67XSORT (34.58)=286.2 O=48.67XSQRT(34.85)=287.3 6 0=41.24XS%RT(35.41)=245.4 0=41.24XSORT (33.31) =248.5 BL 1 -SCM JCT :10 34.9 5.19 i.0.0 242,3 11 277.3 242.5 12 519+8 5.19 10.0 243.3 1.3 763.1. 5.19 10.0 288,9 14 105240 5 56.0 75.0 15 112740 5,19 47.0 .0002 5.19 10.0 .0070 .0224 ,0456 .0825 0938 -34.52 00 34.52 . 07 34.59 . A 2 34.82 .46 35.27 4.62 39r 99 4,41 44430 F. SPLIT POINT ot. 0=41.. 24XSQRT (34.52) =242.3 -. 0=41.24XSORT(34.59)=242.6 0=41..24XSORT(34.82)=243.3 I{� O=48.67XSORT(35.27)=289.0 C1-11. 89X ORT (39 . R9) 7- 75.1 BL i -PCM JCT Ico GRINNELL ; FIRE PROTECT CN SYST E S Elydrac lit CP1a ions CONTRACT NO.A1.12. 6'�.. a At, . N: M AL .051 '"a PARA- M t 11. % LOCATION #1.0i4C.UltotS R.A GRINNELL FIRE PROTECTION SYSTEMS CO. v INC. 10114/77 16:29 TOTAL PIPE EOUIV K GPM- GPM IO FT PF/L 14+1,4= 120 LINE : NO. 3 LINE 8.00 8.00 8.00 39.0 40.0 41.6. LINE 8.00 39.0 8,00 40.0 8.00. 41.6 39.0 79.0 120.6 39.0 79.0 120.6 1.38 1.61 2.07 10.0 10.0 13.0 1.18 2.05 1.72 CO., INC. SFIcE7 NO.22.OF 14 SYSTEM NO_ 1° DATE 10"1"; . PAGE N0 TOTAL REF PSI PT 23.77 24.95 27.00 28.72 LINE SUPPLY PIPE VARIATIONS 42.91 242.3 2.47 1/1-n2741 242.3 2.07 'r GRINNELL F ?F_ OTECTECN S'IST S CO., PA:. ElyAnilic _,blions SHEET Na 0E114_ CONTRACT NO.41.^..'.146. 0,71 5i 74) PArz PRO'S ' I I LOCATION l'oaull-A LoA.$14 10/14/77 Wi-W= 120 LINE 8+00. 8.00 8.00 SYSTEM Na 71. . __.. DATE GRINNELL FIRE PROTECTION SYSTEMS CO.,INC. 16:38 TOTAL PIPE : E( UIV TOTAL GPM GPM ID FT PF/L PSI LINE NO. 39.0 40.0 41.6 39.0 79.0 120.6 LINE 8.00 39.0 39.0 8.00 40.0 79.0 7.82 40.5 119.5 8.00 42.3 161.8 10.0 9.0 .9 .0 12.5 1.18 2.05 2.31 1.18 1.85 1.17 2.84 REF PT NOTES 23.77. 24.95 27.00 29.31 LINE SUPPLY PIPE -VARIATIONS j48.571 285.4 2.47 13.0 3.57 34.38 46.32 285.4 2.07 c .11.0 7.15 LSA /N • KT 2 6 1977 TUKWILA FIRE DEPA, 9 WASHINGTON SURVEYING & RATING BUREAU 444 Andover Park E.. .s HYDRAULIC CALCULATIONS For Sp' c.4�.� '1 Sheet of._ By Date 14.1- Z —1'' Joh No. Nozzle !dent. & Location FlowPie In G. P. M. Size Papa Fittings & Device Equiv. Pipe Length Friction Loss p.s.i:/foot Pressure Summary Normal Pressure NOTES q Lgth , Pt 3 Y. '7S-- Ptt'f 1'" s-., ... Sir - Q 133 G Fit Pe Pv 1 Tot 4a. S` ,O;.iS re Pf ..,-/ r Pa •q t.jLgth /G ..Pe 3$'.Ye. Et( -9 . Q 14 G 3 4 l X & Fit 8 - y Pe Pr Tot 2- 't."-• .n//S Pf 1.So Pn • q Lgth 20 Pt3/.`/C Pt 7 - Fit 3 '1 Q 1463 & Pc Pv Tot .. Y - o / 5 37 PF `/Y _ Pn q• Lgth Pt t'•?.' pq'S) Fit Pe A. Q /1.1 3 Y Tot 4 S .0/..c21 Pf .7 Pn q 2 o ° fl 7� Lgth c'1v/ Pt f./...1.. / Pt 2... Q /%G 3 Fit Pe Pr Tot 3S.. Pf .1/ q Lgth • Pt # 2. 3 2 ( Q Fit Pc PVr — �"' -- Pf po` q Lgth .- ,- / . G 3 Z3 Pt3 y o r p�E / 7) 7—i'nwr S-t.Ie Z L r ,r."- Fit / ..-5: o Pe PVr Q /d 3? G N;¢. Ian Tot 2 .: 'P.A. pf . S. 4.3 Pis q Lgth .7 .. .epaP33 Pt t,/ i'.. ' pt Fit 7 ? Pe Po Q/0 33 Tot }-% Pf 4 Pn Lgth 1: Pt / -'1 P(7-;:) Flt.-------- - Pe Pr Q Tot Pf Pis q F(`1 a Lgth ,340 Pt YZ , f '7 Pt q V ttr: .4 � (. 33 . J �` t. /.._ i 1Alr - Fit /".• Pe /'f ..' 'f Pvr i Q 2.4 G Tot J"'/. .✓ `/' " 7Z• Pf 2.i`1 � q Lgth 3 Pt ..`''t. T- t Pt AV c Fit / et Pe Pv Q 2G /(v �( Tot 2 Z. S t y .O ` PF /- L I Pb v 7....-. q Lgth -r' o,: -.)Pe 6 � - : / Pt `y '�� <� L.. % .� % Fit c? Pc 1. 7 q P. •oR gp' , t Q 61 6 / o / Tot / 7- v. U/ `�..t. G Pf 1 .77 Psi q Lgth G 3 j Pt 6,./.0/ Pt : •-• c- ? / Fit $.. Pc 2-vo Pv /c, '' 6i".-' Q 2.6 ye / c7 Tot 7 Z 1 _U /.37C Pf (i.9 7 Po GA) Hi— q 7.5-0 Lgth /'-'J Pt 7 if. .V ° Pt Fit 6 % Pe Pv 93Y1.'4 /0 Tot '7 .62/72# Pf 3:74 Pa Form 139 7't:14- _ 4 r /.z ,•••• Sr,Z e r- r -A 2 . For WASHINGTON SURVEYING & RATING BUREAU HYDRAULIC CALCULATIONS Sys c Sheet By Date 1 - 'L * -1 Joh No 44_44 _.-.. Nozzle Ident. & Location FlowPipe In G. P. M. pi Size Fittings & Device Equiv. Pipe Length Friction Loss p.s.i.�foot Pressure Summary Normal Pressure NOTES q Lgth - Pt 3 3. k 3 Ptd l r 2 r +e.» Fit Pe Pv t . 5 7. 3 G i.,. •.r F.—. i �3 o I u 3.2 Tot / . ...'' :.. Pf Pn 3.... 3 ?', (. Lgth Pt ...r y.; PiiS' Fit Pe Pv ( ) Q x•36,8 Tot /0 ti GI Pf 07 Pa 32G.,Q G Lgth .� i.o r Pt 3 3. `p.' Pt /6 i 3" rt.'" a.. S C. r 3 • Fit Pe Pv (Z4 O 743i. i. Tot 1 0 pi •17 Pn 221,3 (z).4re- 6 Lgth 4 . - .036s 7 Pt 3 Y: u 'j Prt '�) (1) r Fit S'::. S Pe Pv (zij Q 1041.1' Tot .; / y;. • Pf //..39 Pn`` eL • Lgth Pt it S-, Are Pt(2-°_,) Fit . Pe Pv Q Tot Pf Pn q •160'4 3 c0 Fn//. J c.. Lgth . 3v °v'9 2 Pt 4s,5? Pt (")r'e n.a c.."'.. 33..j /tc.« ✓ 1..no: Fit 1Y. S Pe /4 . 4 ;"' Pv O ZJa?S.'7 Tot ''`r . S Pf 2 •/ `r Pn q ' Lgth .3 . D -1./ f. Pt en 2-2-C Pt A Y s. f/ Fit I y Pe Pv Q Z- G9 C Tot 2 z_ Pf / . Z / Pn 2 .,,N r -• qT /0 Lgth 4 ca - G/ 386 Pt C.. 3. 't'`1 Pt 4.. F'..... • r z 0/ -r ..44!: 4 ie Fit TW Pe 1. 73 Pv 4' f-' ►SKS Q 249 & Tot / 2 .3 Pf 1.17 Pn - • q / Lgth .t.e "t UI3k" Pt G G • 4 7 ' Pt >t•....,.•r.. 0.c. T. 36✓ Fit• .8.6 Pe- 2-o o PT"" cs " Q 2414 Tot ?2 / Pf ei.et7 Pr/ q 7s" Lgth /u s , r02./74 Pt 7 .� • e, ' Pt •� Fit G 7 1 Pe Pv Q3Y'4 /O Tor / 7Z Pf 3.$ 1 Pn q Lgth Pt O 2 . 7 Pt A '7" •Z .. 11,4 1.*.. Fit Pc _. .. Tot Pf Pn • Lgth Pt Fit Pe Q Tot Pf q Lgth Pt Pt Fit Pe Pv Q Tot Pf Pn Lgth Pt Pt Fit Pe Pv Q Tot Pf Pn- WASHINGTON SURVEYING & RATING BUREAU HYDRAULIC CALCULATIONS For r_- • 77/ :s y5 "j. N&'. x,33.•1 By Date 1 t1 .. 'LO Job No. • Nozzle Idem. & Location FlowPipe In G. P. M. Pipe c: Fittings & Fittings Device Equiv. Pipe Length Friction Lou p.s.i./foot • Pressure Summary Normal Pressure NOTES E 3 q • Lgth 7W Pt 3 3._: 4' 3 Pt 1 •t z %z g N Fit . oOZ Pe Pv �,r (6) Q 2 moo. s" Tot C. 5 P1 .0 1 Pn M. , Q 75 ..> G Lgth a. 3 Pt 1• Pt 41) Fit , Pe Pv 22,.3 .J Tot 3. S Pf •o f pn 4 C41 32C.C. q (n Lgth , O/ 3 i Pt 3 3. 95 pt([ -9 3" 2••, Fit . Pe Pv I 14- • ge. 1 3• X11) Q G3Z.. I Tot / o pf .[ pnr _ q 32"1.2 G Lgth • ,02 ;i' Pt 3 3. 7 .-1 Ptl f [) Fit Pe Pv (17_) Q iSI. 3 Tot /n Pf •'1' Pn , . q q 32 ( 6 Lgth oa.'" . Pt 3 `' . 2C PO 0) Fit Pe Pv CO Q i2S1.7 Tot /0 P1 1-, Pn / j3o•`l� q • ql . ¢ 6 Lgth •06/G Pt . `�• -. Pt(4 .� Pc Pv /Fit (31� Q 13Ze).3 Tot 46..i Pf 3-'13 Pn. q 7.5. .• 6 Lgth 3 C •aS7°`r Pt 2 k. t S Pt( Y) r ., _ AC ) = Fit 3 j Pc Pv Qit,ev.3 • Tot 71 Pf 4. 0.1 Pn q 6 Lgth 7 w O 57oY Pt 4 2.2-7 Pi 3.) Fit Pe Pv • Q • / 90 r. 3 Tot 3 i{. )i ' Pf 2. 2 u Pn q C Lgth SC 6•1-' ,045-7 Pt4 4- -13 ' Pt Fit Pe Pv • I Q /yoat. 3 Tot 6.5' Pf . ¢'3 . - Pn- q 2 0 a S. Lgth / S. 31" j c A". Y. . 6 2 1 Pt 4 4-. 1/6 p4) Fit Pe Pv Q /(soY. 3 Tot t S• S PF ..-3 3 Pn q e• Lgth Z•� '%W . O it ? Pt 4S. / 1 Pe Fit Pe Pv Q //..95!_y Tot : PF . 38 Pn q Lgth Pt 95.57 Pt(Z•P) Fit Pe Pv Q Tot Pf Pn q• Lgth . Pt Pt Fit Pe Pv Q Tot ' Pf Pn • q Lgth • Pt Pt Fit Pe Pv Q Tot Pf Pn Form 139 Sec L= PA- C. rb F-0 K -t/•St oa I �n..ar o rtwTt At,4 o t, SnEEV of Z% NAME LOCATION HYDRAULIC DESIGN INFORMATION SHEET SE4AL.E 'PR.oTECr 77' I BUILDING CONTRACTOR i Likes ILA - \N ASIA • DATE to -1777 SW/m.15011 - DEAN CAR. SYSTEM NO 7 CONTRACT NO. 3256 Eva M CALCULATED BY DAN 1%N.c1.1)04 DRAWING NO. 2 Or:- CONSTRUCTION: FCONSTRUCTION: (] COMBUSTIBLE 0 NON-COMBUSTIBLE CEILING HEIGHT . FT. OCCUPANCY [] NFPA 13: ❑ LT. HAZ. ORD. HAZ. GP. 0 ❑ NFPA 231 [] NFPA 231C: ❑ OTHER (Specify) ❑ SPECIFIC RULING MADE BY . DATE CI 0 0 EX. HAZ. FIGURE ; CURVE AREA OF SPRINKLER OPERATION -DENSITY AREA PER SPRINKLER HOSE ALLOWANCE GPM: INSIDE HOSE ALLOWANCE GPM: OUTSIDE RACK SPRINKLER ALLOWANCE • 5600 160 150 750 2[b SYSTEM TYPE • ® WET 0 DRY 0 DELUGE 0 PRE -ACTION SPRINKLER OR NOZZLE MAKE AR.IN1.IE11 MODEL QUR Eb SIZE 17/32 ORIFICt K -FACTOR TEMPERATURE RATING 'CALCULATION SUMMARY 3bYG 7 If St1 GPM REQUIRED -344;4PSI R=QUIRED - '"Q" AT GUT - "C" FACTOR USED: OVERHEAD t2o . UNDERGROUND IRO_ I DATE & TIME 1 STATIC PSI 1 RESIDUAL PSI GPM FLOWING ELEVATION WATER FLOW TFST PUMP DATA RATED CAPACITY AT PSI ELEVATION • TANK OR RESERVOIR CAPACITY ELEVATION WELL PROOF FLOW GPM LOCATION _ SO SOURCE OF INFORMATION COMMODITY CLASS LOCATION i STORAGE HEIGHT AREA AISLE WIDTH 4 STORAGE METHOD: SOLID PILED % PALLETIZED % RACK Ir 0 in inI AVN.ILAgE. @ GISr -- I►.L To 12.E EXtsTII Lt. it U cc ❑ SINGLE ROW ❑ CONVENTIONAL PALLET ❑ AUTOMATIC STORAGE ❑ ENCAPSULATED . ❑ DOUBLE ROW ❑ SLAVE PALLET (] SOLID SHELVING ❑ NON - O MULTIPLE ROW ❑ OPEN ENCAPSULATED FLUE SPACING IN INCHES LONGITUDINAL TRANSVERSE CLEARANCE FROM TOP OF STORAGE TO CEILING FT. IN. HORIZONTAL BARRIERS PROVIDED VOSSIASISIMWWW GUSTOMER ORDER OR CONT. NO JOB NAME 5v1EEC' Z 21 DRAWN BY DATF REVISED BY DATE FOR MATERIALS AND OPERATIONS SEE SKETCH No. EV. PIPE REF. DRW'G. Nos. MARK No SKETCH No REV GRIN" ELL CONTRACT NO. NAME s1=GA1� Mo:-.3-eLT 771 SYS LOCATION RO 1 1114bE.R.CLAR0131.ir taw SHEET NO...LOF 21 DATE, NOZZLE TYPE a LOCATION FLOW IN G.P.M. PIPE SIZE FITTING a DEVICES PIPE EQUIV. LENGTH FRICTION LOSS P.S.I./FT REQUIRED P.S.I. HYD. REF PT 0 ELEV. ' NOTES o E=17 LoS(.� . , FTG. SLa'- ,0143 PT X3.08 @ Ft5 IOp .LGTH. T= O PF 10.98 Q2/095.1 WA T= 39 TOT. 7dz PEo _ S LGTH. -4 .0437 PT 7' .0 [o @ Lc?uN . To PIT 2L3/= 8 ►FTG• 2 PF .52 Q 2l�`1 .1 UCL TOT. Iz PE Q a" DET. Lv. _GTH. . ' T 7 .5: FTG.:. PF 2.06 QW95.1 TOT. PE Q to" T= 30 LGTH. 100 ,0148 Pr 1710.52.@ AD tf Io" LE.L Lo1su-1a PIT' @ GUT -1 N To 12." E IST. 16.v.=5 PF QZ�5.1 =QT. 135 PEZ.00 PT 78.55 P �UTStDE o 7E0 FTG. FTG. PF 11CSE 03445.1 a TOT. NUITH. PE PT 75=80 0.IIMLA FTGQ PE TOTS PE o LTH. PT FTG. TOT. PF Q Pm o LGTH. rTG. PT PF TOT. PE O LGTH. PT FTG- Pr Q TOT. PE 0 LGTH. PT FTG- PF• Q TOT PE o LGTH. PT • . FTG; PF Q TOT. PE o LGTH.PT FTG. PF Q TOT. PE o LGTH. PT FTG. PF Q TOT. PE o LTH FTG. TOT PT PF Q PE o LTH. FTG• PT 0 TOT. PE o LGTH. FTG. PT PF Q TOT. PE o LGTH. PT 1 FTG. PF 0 TOT. PE o LGTH. PT FTG. PF 0 TOT. PE -. JOB i SE!:ih}'_ 7 HA'.WIL. HOSE DEM.AT F+S ELEVATION •120,0 0 GPM . 33.5 FT. SHEET OF 21 SHEET OF SPRINKLER SYSTEM HYDRAULIC FLOW CALCLJLATIONS (FOR PIPES IN PERIMETER) PIPE FLOW DIA FITTING EO LEN FR LOSS PRES. HYD NO (GPM) (INCH) AND DEV (FT) {PCT/FT) (PSI) REF NOTES GOUNTEPCLOCKW:(St= 33.80 14 SPLIT POINT SA -43 14 230.4 6.25 6.5 .00201 .01 75.0 33.81 13 HOSE RAdc 13 305.4 6.25 3.5 .00339. .01 _32Ca.1t, 33.82 1.2 SL44 12 632.0 5.25 1.0.0 .01.301 .13 327. Z 33.96 11 a. of 4 11 959.2 6.25 10.0 .02815 .28 378. Lp 34.24 10 81.14 10 1287.8 6.25 10.0 .04854 .49 41.3 34.72 9 GL44 { ni FUMML 9 1329.1 6.25 66.5 .05146 3.42 9.4.9 38.14 8 14051E RAGk 8 1404.0 6.25 3.5 .05695 .20 38.34 7 7 1404.0 6.25 10.0 .05695 .57 38.91 6 6 1404.0 6.25 10,0 .05695 .57 39.48 5 40.05 4 1404.0 6.25 iT 32.5 .05695 1.85 41.90 3 3 1404.0 6.25 45.0 .05695 2.56 197.10 44,47 2 1603.6 8.25 20.0 .01.884 .38 44.84 1 1603.6 8.25 15.5 .01884 .29 45.13 20 B1JL.1 JCT DeFF%GE. DEkkknlp s %eEr 5 OP Zt SHEET OF PIPE FLOW ILIA FITTING ECS LEN FP .1...u56 PRES. HYD NO (GPs') (INCH) AND DEV ( FT) (PSI/FT) (PSI) REF NOTES CLOCKWISE 33.80 14 SPLIT POINT 81_313 15 -103.2 6.25 10.0 .00046 .00 v _ 333, to 33.80 15 BL 3. 16 -436.8 6.25 10.0 .00657 .07 3210, 9 33.87 16 SL.44 17 -763.7 6.25 10.0 .01846 .18 327.5 34.05 17 EL 44 18 -1091.5 6.25 I LTE 1.3.5 .03374 .48 34.54 1.8 19 -1091.5 6,25 l LTE 92.0 .03574 3.29 37.8.3. 19 20 -1091.5 6.25 %T 204.5 .03574 7.31 45.13 20 BULK JCT AVERAGE PSI AT JUNCTION IS • . 21 22 45.13 2695.1 8.25 % LTE 42.5 .04921 2.09 Loss THRotv,H BULIc l� 47.23 R%sER To ToP of ALV. 2695.1 7.98 1 RLV ILV 23.0 .0 5787 1, 33 -a--- - _ tss THRotYsH VALYES 48.56 2t" SCtt 4o PIECES ELEVATION HEAD IN PSI IS . . ++++ + 14.52 PSI REQUIRED -AT FLANGE AND SPIGOT PIECE. . 63.08 WITH .2695.1 GPM FLOWING 33,5 FT .Tcsrm... ELEV. 1 3 r Sr - To To FIINIIGRE.t FLooR Nc --- ACb1Ttc PfL..---DP. MAt�tb ._tS ::_. PtbbEfS : AT.__..__ F 'S :: 2 € AvsE. t- - -- tksmE_._ Nosi= �EMRuo WhS plctvEc uP jr TWE HosE _... ACEs .__. CoNN ECT?ONS OFICE. bE.mto.111 ):PILtc.Eb L1P aar- Tt9 nF1=►cE CcaN E.Ci10M ) oN.LY Ru _ Tri-ROL1�N- "WE C7V EeH-E_AD F S - Zoo Li'Nt FOAr l.<s REPLAC_Es Ttta bsN\AN D 1N. Titer UN1MERC IN \fl CONTRACT NO NAME LOCATION 1711 I I I 1 J L L.L. SHEET NO_ -6.. -OF -ZL_ E.cLta.E PRdEcr 771 SYS 11 DAT E 5ICYLl&tt`'r ' I& - u? k FPc'i3i25 NOZZLE TYPE £k LOCATION FLOW IN G.P.M. PIPE SIZE FITTING 8 DEVICES PIPE EQUIV. LENGTH FRICTION LOSS P.S.I./FT REQUIRED P.S.I. HYD. REF PT 0 ELEV. NOTES K'.8 •b o 1'' _.1„G H. FTG. .275 PT 15.21 FOR SL ' 3 PF . Z y 03\.Z TOT 11" PE .40 IIS,• Q .LGTH. ?T IS. 88 FTG- OT. LGTH. PF 31.2 Q o ` PE15.88.7.83 PT FTG. Pr Q r TOT. PE tC= 8.D Q LGTH. ,LGTH. .29S PT 15.21 � FoR INL P1= . Z(o o 31.2 TOT. 10/7..4 PE .38 t O . o LGTH. PT 15.85 31.2 k= 7.84 FTG. Pr Q o TOT. LGTH. PE PT .,15.85 "FTG. Pr Q TOT. PE• Q LGTH. PT FTG- PF Q TOT. PE Q LGTH- PT FTG. PF 0 TOT. PE 0 LGTH. PT FTG- PF 0 TOT PE 0 LGTH. ,PT . FTG. PF 0 TOT. P:� Q LGTH. Pr FTG: Pr 0 TOT. PE o LGTH. PT ,FTG. PF 0 TOT P o LGTH. PT FTG- PF 0 TOT. PE Q LGTH TO . PT • PE 0 v FTGH. PF o TOT. PE LGTH. PT FTG. PF 0 TOT. PE o LGTH. Pr FTG- PF 0 TOT. PE o LGTH. PT FTG- ' PF 4 TOT. �._ 10/14/77 6tAt44_, tU1sL GRINNELL FIRE PROTECTION SYSTEMS CO. v 1:NC. 13:59 TOTAL K GPM GPM ID FT PF/L PSI PT NOTES PIPE EQUIV SHEET 7 efIF 21 PAGE NO TOTAL REF H+W= 120 LINE NO. LINE 8.00 39.0 39.0 8.00 40.0 79+0 8.00 41.6 120.6 8.00 42.6 163,2 1.38 1.61 2.07 2.07 10.0 10.0 10.0 14.8 1.18 2.05 1.32 3,42 23.77® 24.95 27.00 28.32 31.74 ®B LINE 23.77 ® 8.00 39.0 39.0 1.38 10.0 1.18 24.95 8.00 40.0 79.0 1.61 10.0 2.05 27.00 8.00 41,6 120.6 2.07 9.0 1.19 28.19 7.84 41.6 162.2. 2.07 14.2 3.24 31.43®8 LINE SUPPLY PIPE VARIATIONS 56.17 326.2 3.07 54.07 326+2 2.47 13.2 4.65 36.39 16,2 1.98 • 33.72•0 ._gRANGNLi y E.. Flow gALANGL \I 31.74 / 31.A3‘ (IGZ 2 + 1GS-2 = - 3Z6D•Z 1K 32C0.2.44-373-.27 = 5(0.% _SHEET 8 c W' Z1 GR e•.':NELL FIRE PROTECTION SYSTEMS co. r INC. -10/14/77 14:01 PAGE NO TOTAL PIPE EOI.JIV TOTAL REF K GPM GPM ID FT pF/L. PSI PT H+W= 120 LINE NO. ;'.2 LINE 23.77® 8.00 39.0 39.0 1,38 10.0 1.18 24.95 . 8.00 40.0 79.0 1,61 10.0 2.05 27.00 8.00 41,6 120.6 2,07 10.0 1.32 28.32 8,00 42.6 163.2 2.07 15.1 3.49 31.81® NOTES LINE 23.77® 8.00 39.0 39.0 1.38 10.0 1.18 24.95 3.00 40.0 79.0 1.61 10.0 2.05 27.00 8.00 41.6 120.6 2.07 10.0 1.32 28.32 8.00 42.6 163.2 2,07 14.9 3.44 31.76® LINE SUPPLY PIPE VARIATIONS 56.17 • 326.5 3.07 54.07 326.5 2.47 16.2 1.98 33.79 13,2 4.65 36.46 FLow 3ALAN[E. e 131.81 / 31.7C. (.12.2) 4163.2 = 32(e.5 S //-3.17'1 .1`7 10/13/77 5HEEr OF 21 MANcRuME. 13 GRINNELL FIRE PROTECTION SYSTEMS CO. r INC. 18:33 PAGE NO TOTAL PIPE E:OUTV TOTAL REF K GPM GPM ID FT PF/L FSI PT NOTES H+W= 120 LINE NO.3 LINT 16+64 7.83 31.9 31.9 1.05 - 8.5 2.61 19.25 8.00 35.1 67.0 1.6:L 9.0 1,36 20.61 8.00 36.3 103.3 1.61 9.0 3.03 23.64 8.00 38.9 142.2 2.07 9.0 1.61 25.25 8.00 40.2 182.4 2.07 1.0.) 3.07 28.32 LINT 19.25 -8.00 35.1 - 35.1 .1438- 9.0 .87 20.12 8.00 35.9 71.0 1.61.. 9.0 1.52 21.64 8.00 37.2 108.2 1.61 9.0' 3.31 24.95 8.00 40.0 148.2 2.07 18.3 3.54 28.49 0 LINE SUPPLY PIPE VARIATIONS 59.91 331.1 3.07 16.3 2.05 30.54 57,38 331.1. 2.47 13.3 4.81 -33.30DO 53.60 331+1 2.07 11.3 9.67 38.16 FLOW BAJ CE f 28.49/z8..3Z (l8z.ti) +- 148.2 • = 33%.\ 331.1 /1/3).10` 57,38 &P 4CHL1 N E 14 GRINNELL FIRE PROTECTION SYSTEMS CO..INC. 10/13/77 18:17 TOTAL. K GPM GPfI PIPE ID H+W= 120 -`r LIME Nil. d- LINE 23.77® 8.00 39,0 39.0 1.38 10.0 1.18 24.95 9.00 40.0 79.0 1.61 10.0 2.05 27.00 8.00 41.6 120.6 2.07 10.0 1.32 28.32 8.00 42.6 163.2 2,07 15.2 3.51 31.83® EQUIV FT SHEET 10 of 21 PAGE NO TOTAL. REF PF/L PSI PT NOTES LINE 23.770 8.00 39.0 39.0 1.38 10.0 1.18 24.95 8.00 40.0 79.0 1.61 10.0 2.05 27.00 800 41.6 120.6 2.07 10.0 1.32 28.32 8.00 42.6 163.2 2.07 14..8 3.42. 31.74 LINE SUPPLY PIPE VARIATIONS 56.16 326.6 3.07 54.04 326.6 2.47 16.3 :L3.3 1.99 33.82 0 4.69 36.52 31.53 CIl03..) + 1Cn3.Z = 32(0.C. GPM FtD`,N BALANCE 32CA . fo O 4 II n A A a II 6QAn1GHLINE _ 4 vis1id1'jLLL.. CONTRACT NO. NAME SELALE, PP.c3 tT 771 SYS 7 LOCATION 0,1 CALLS SHEET NO_L.OF._Z.L.. DATE NOZZLE TYPE a LOCATION ".'......` FLOW IN G.P.M. PIPE SIZE iOh Ii& FITTING 8 DEVICES _E _%7 T= 3o PIPE EQUIV. LENGTH _GTH. Ioc<D FRICTION LOSS RSI./FT ' REQUIRED P.S.1. PT 57.38 HYD. REF PT 0 ELEV. MOTES @...� s ...... 0 FTG. 860 015(0 PF t1►58 Q Z78o T= 39 TOT 7.4 Z PE Q S". 8 • DEr. CV . LGTH. 4 SPT (D8.9(.0 @ cokm To ZDV = a FTG. 8 1 Pr , 55 Pir 02780 o TOT. 1Z )-GTH. 0 P PT X9.51 • FTG. Pr 2.00 ,Q Z780 TOT.. PE Q le , 113. Tr -3o LGTH. 100 .0156, PT 71.51 @ to` t.EAb-it4 CoM►.t. To PCT IGet= 5 FTG. 35 PE 2.11 02780 (COT. t35 PE ouTs�t�E. o 7S0 LGTH. P7 73 ADZ. e CUT-iu TO FTG. PF t2" ExISTIMG. 75-80 Psi. 1465E Q 3530 o TOT. LGTH. PE PT , .FTG• - PEAN/MO(61 Q TOT. PE Q LGTH. PT - - EEG- TOT. P1` Q PE Q LGTH. PT FTG. PF Q TOT. PE o LGTH... PT FTG. PE Q TOT. PE o ,LGTH. Pr - FTG. PF Q TOT PE Q LGTH. Pr FTG; PF Q 'TOT PE o LGTH. PT - FTG- PF 0 TOT. PE Q LGTH.• FTG. � PT -_ PF Q 'TOT. PE Q LGTH FTG.PF TOT. PT -: 0 PE o ,FTG• - P Q TOT. PE o LGTH. FTG. PT PF 0 o TOT. LGTH. PE PT FTG• PF O TOT. PE o LGTH. Pr • FTG. PF Q TOT. PE -r JOB ICS! H, Z,WIL HOSE DEM.AT F+S ELEVATION SEGALE7 120.0 0 GPM _ 33.5 F.r sHE%T 12 oT. 21 SHEET OF SPRINKLER SYSTEM HYDRAULIC FLOW CALCULATIONS (FOR PIPES IN PERIMETER) PIPE FLOW- DIA FITTING E0 LEN FR LOSS NO (GPM) (INCH) AND DEV (FT) (PSI/FT) COUNTERCLOCKWISE . 6 85.2 _ 331.8 5 417.0 33Z. 1 4 749.1 3 1360.3 2225.2 PRES. HYD (PSI) REF MOTES 6.25 6.25 . 6.25 6.25 8,25 8.25 10,0 .00032 10,0 .00603 32.5 .01781 45.0 .05371 20.0 .03454 15.5 .03454 34.91 . 6 SPLIT POINT __$L,3 .00 .4.91 5 BL._1f .06 34,97 4_-- BL .d .58 35.55 3 TREE SYS 411 2.42 37.97 2 TEE TM_ ... .69 38.66 1 .54 39.20 0 BULK JCT 5 \EFT l3 aF Z 1 ZA4 z. Loot' sulk 4 RISEN SHEET OF PIPE FLOW IIIA FITTING ECS LEN FR LOSS PRES. HYD NO (UPM) (INCH) AND DEV (FT) (PSI/FT) (PSI) REF NOTES CLOCKWISE 7 -253.7 6.25 %So. q - 8 -404.6 6.25 95.0 9 -479.6 6.25 1.0 -479.6 6.25 11 -479.6 6.25 12 -479.6 6.25 13 -479.6 6.25 __ 14 -554.6 6.25 15 -554.6 6.25 16 -554.6 6,25 - 17 -554.6 6.25 18 -554.6 6.25 19 -554.6 6.25 20 -554.6 6.25 AVERAGE PSI AT JUNCTION IS 21 2779.9 8.25 2779.9 7,98 34.91 10.0 .00241 .02 34.93 3.5 .00570 .02 34.95 66.5 .00781 .52 35.47 10.0 .00781 .08 35.55 10.0 .00781 .08 35.63 11 10.0 .00781 .08 35.71 12 ..3.5 .00781 .03 3573 13 _NOSE. RAck 6.5 .01022 .07 35.80 14 10.0 .01022 .10 35.90 15 10.0 .01022 .10 36.01 16 10,0 .01022 .10 36.11 17 13.5 .01022 .14 36.25 18 92.0 .01022 .94 37.7.9 19 204.5 .01022 2.09 39.27 6 SPLIT POINT_ %L 13_ _ 4 Nes F1autt4L. 10 ". . . . .... .. 39.24 42.5 .05212 2.1' 1-a----- LbS THROUGH eglLk 41,45 __. _ Met _Tb TONS of MY. 23.0. .06129 1.417.74'7-7 LOSS THRnt1GH VALVES A 42.86 _ _8" 5L4140 P\ t'Fci 20 BULK JCT r 'E=. 1 _ jOyirD IN PSI' IS ♦ 4 • 14452. • PST Fir._ UIREIJ AT FLANGE: Atm SPIGOT PIECE. e 57.38 (WITH '2779; 9 GPM FL.OWI-Nt. NLA 1 TS NO Ab.hI T1oi4 AL DE.1•Ms4.1n 33.5 FT TOTAL ELEV. PR.nA 14%.t}EST BL.. TO FNNI5HE1 FLR. 4S /BEd AT .THE F S '0114kgfirlik16/11141)LlialikAlke CUSTOM ER ORDER OR CONT. No JOB NAME SHEET 14 of. 21 DRAWN BY DATF REVISED BY DATE 61.17 • t. . BO 8 st.J 1 TREE SYSTEN\ 2 FOR MATERIALS AND OPERATIONS SEE SKETCH No. REV PIPE REF. DRW'G. Nos. MARK No. SKETCH No. REV. CONTRACT NO. NAME LOCATION V t-1 11151 tl d:. i... 4.. SHEET A4O..15..OF.2. sEG.ALE. Pk'o r 771 5"s 7 DATE PSP 4 Z TREE 5Ys 1 xN r m GALLS NOZZLE TYPE & LOCATION k=az. 26 FLOW IN G.P.M. 0 PIPE SIZE s{ 1W FITTING & DEVICES PIPE EQUIV. LENGTH . Lull FTG. FRICTION! LOSS P.S.L/FT .0099 REQUIRED P.S.I. HYD. REF PT Q ELEV. NOTES PT 3►•� .. ( PF , 07 Q 182.5 TOT 9, z PE k=41.95 p Z3'.5 sl 1W LGTH. ,o4L5 .107 PT 32.05 F . FTG- PF .'47 Q 421.0 o Z39. Z TOT. 10 LGTH. PE 15-T 32.52. G i<=41.15 FTG. PF .30 Q[sss.Z TOT Z,8 PE Q _ 4 LGTH. .119 PT 32.82 N e 4" vtc FTG.: • PF -.33 Q6o57 2 SGthia .T. ..s PE OF Fla_ Q ZOO ti 5e.tt4o, T.:: Z° GTH. 2.Z .1945 Pr 33. t5 I. @ OFF la_ OUTLET @ cornu. Vo Lao P FTG. 20 PF A.3Z 0 859.2 Q TOT. zz.z tG f H. PE PT 39.4P 2 FTG. . PF Q TOT. PE 0 LGTH. PT k - 859.2 -too Stn FFG- TOT PF Q PE 37.47. Q LGTH. PT FTG. PF . Q TOT. PE o LGTH. Pr FTG. PF Q TOT PE Q LGTH. • 1:YT FTG. PF Q TOT PE p LGTH. Pr FTG; PF Q TOT. PE• 0 LGTH. PT FTG- PF Q . TOT. PE Q , LGTH. PT :._ .. -_ t FTG. PF Q TOT. PE o LGTH FTG. • Pr PF Q TOT. PE o LGTH. FTG- PT PF 0 TOT. PE• o LGTH. PT FTG. PF 0 TOT. PE 0 LGTH. PT FTG- PF 0 TOT. PE o LGTH. [FTG- PT PF 0 TOT. P 10/14/77 TOTAL PIPE EOIIV TOTAL REF GPM GF'M ID FT PF/L PSI PT NOTES siieEr 6 of z &RANCHUIttE CINNELL FIRE.• PROTECTION SYSTEMS -CCI. r INC. 18:22 PAGE NO H+W= 120 LINE 8.00 8.00. 8.00 LINE 8.00 8.O0 8.00 37.7 38.6 41.8 37.7 38.6 { 41 .8 LINE NO. 37.7 76.3 118.1 37.7 118.1 76.3 9.7 9.7 17.4 1.07 3.96 2.21 22.21C> 23.28 27.24 29.45 To? of RN! 1.38 1.38 2.07 LINE SUPPLY PIPE VARIATIONS 42.96 237.5 3.07 4:1.9; 237.5 2.47 40.33 237.5 ' 2.07 9.% 9.7 12.,E 1.07 3.96 1.56 16.3 1..11 13.3 2.-60 11.3 5.23 22.210 23.28 27.24 28.80 MP of tzi t: 30.56 t 32.05OFi© 34.68 PI -0W BAlANGE, o J Z9, tis / z3.80 C 118.1) -4-- 118.1 = Z37.5 = 237.5 /x/32.os = 4 195 BQANcS this GRNNELL FIRE PROTECTION SYSTEMS CO..INC, 10/14/77 18:32 TOTAL PIPE EQUIV K GPM GPM ID FT PF/L PSI FT NOTES stir %7 of 2\ PAGE NO TOTAL REF. ti+W= 120 LINE NO. LINE 8.00 8.00 8.00 32.5 32.5 33.6 '66.1 37.2 103.3 1'.38 12.8 1.38, 12.7 1.61 • 10.4 1.08 3.97 3.51 16.54 17.62 21.59 25.10 Tb? of Rt4 LINE 17.84® 8.00 • 33.8 33.8 : 1.05 13.5 4.62 22.46 8.00 37.9 71.7 1.38 16.7 6.07 28.53 TUP Rt t LINE SUPPLY PIPE VARIATIONS 32.28 181.8 2.07 29.71 181.8 1.6.1 11.3 3.19 31.72 9.3 8.92 37.45 Flaw . SAL/NOCE_ /28.53/7.5.10 to33) - - 71.7 = K = 18t.S/ 3t.92 3z •z8 Vi1kIIV1 J -.1..L_ CONTRACT N0. NAME SEG ALE. P1;O3ecr 771 5YS' 7 LOCATION RA' 2 T. tila.. 51'5 44z SHEET 140!8 OF21 DATE XMA1 is cALCS NOZZLE TYPE a LOCATION FLOW IN G.P.M. PIPE SIZE FITTING & DEVICES PIPE EQUIV. LENGTH FRICTION LOSS P.S.I./FT REQUIRED P.S.I. HYD. REF P7 0 ELEV. NOTES k= Z3.t�3 3 1 _,G H. 0174 ?r 31.83 c FTG. PF .13 A 133.3 TOT 72 PE k =4t .94 (3237.1 3 IW 4 IW LGTH. .1152 .038 PT 31,% F • t:FA.V IG. FTG• Pr . ct0 0370.4 , TOT. _Y•8, LGTH.PPT PE 32.8[0 !s . .FTG. PF !►0$ 0370.4 TOT. 2.z PE K. -=4I514 ctZ�IO.T 4 TW LGTH. 20.3 .0430 • PT 32.94 H n .1 K=t102.51 Iva FTG. 97 PF Z,(DO Qt 11.1 TOT. 28.0 PE PT 35,5 3 o 'LGTH. FTG. PF 0 ,LGTH. TOT. PE PT . 64 0 FTG. • PF TOT. Pc Q GTH. PT FT. TOT. PF 0 PE Q LGTH. PT FTG. PF Q .. TOT. PE o LGTH. PT FTG• . PF Q "TOT PE Q - 'LGTH. PT • Pr • Q .FTG. TOT. PE o ,LGTH. PT FTG; PF Q TOT. PE o LGTH. PT FTG. PF 4 TOT. P1~ LGTH. PT FTG. PF 0 TOT. PE. Q LGTH FTG. TOT. PT • PF 0 PE Q LGTH• FTG• f_'T ► - PF Q TOT. PE 0 ,LGTH. FTG. PT . PF Q TOT LGTH. PE PT 0 FTG- PF O TOT PE o LGTH. PT FTG- PF TOT. PE _ PRA1 &Q\ L11.1E SHEET fl car- Z rG :moi:?N LL -FIRE PROTECT IOM SYSTEMS co.. INC. 10!17/77 11:20 TOTAL PIPE EOUIV F;: GPM GPM ID FT PF/L PSI PT NOTES PAGE NO TOTAL REF H+W= 120 LINE NO. LINE 22+21g :8,00 37.7 37,7 1.38 9.7 1.07 123.28 8,00 38.6 76.3 . 1.38 9.7 3.96 27.24 8.00 41.8 118.1 2.07 • 16.6 2.11 . • 29.35' TSP of Rei LINE 22.21® 8.00 37.7 37+7 1.38 9.7 1.07 23,28 8.00 38.6 /6.3 1.38 9.7 3.96 27.24 8+00 41.8 118.1 2.07 13.1. 1.66 28.90' TO? of til LINE SUPPLY PIPE VARIATIONS -41,94 237.1 2.47 13.4 2.61 . 31.96®O F ow 811. ANCE aJ Z9.35 /Z8.90 1C= Z39,1/31`TCD ._41:74 118.1) -- II8.1 - 237.1 IIKANCALWE. S •GRINNELL FIRE PROTECTION SYSTEMS CO. rINC. 10/17/77 11:22 • SHEET 20 OF Z1 PAGE NO TOTAL PIPE EQUIV TOTAL REF K GPM GPM ID FT t'F/L PSI PT NOTES 44#141= 120 LINE NO. LINE 14.09® 8.00 30.0 30.0 1.05 12.0 3.29 17.38. 8.00 33.4 63.4 1.38 14.3 4.14 21.52 TOP OF RNI LINT 15.29® 8.00 31.3 31.3 1.05 .12.5 3.71. 19.00 8.00 34.9 66.2 1.38 10.0 3.14 22.14 TDP OF RN LINE SUPPLY PIPE VARIATIONS 26.69 '75.05" 23.43 130.5 2.07 130.5 1.61 130.5 :1.38 11.6 9.6 7.6 1.77 4.99 8.37 23.91 27.13 30.51 Flow BALANcE ✓ 22.1471.52 ...(3..1i) . + Co&.2 %So -5 1� = 130.5/ 30.51 Z3.Co3. ALV " �P. BAL-ACCP - BL BV CON CPLG (S) CM CR, DEL.V_ DET DIA (IN) Dpi DO 0PV DRWG. EE ELEV EQ LEN & S ?IT & :'P. LOSS ,_P.1.•I_ 3V INGR FOSE X1:7 HYD REF PT - ID I or JCT DEV - LTE PCM PE' PF PIPE NO - PL - PRES (PSI) - PT c aafl.,.%.uV y.s.J-.w�..• 16, Alarm Valve Above Finish Floor Balance Accuracy at Branch Line to Cross Main Junction Bottom of Beam Branch Line Butterfly Valve Center to Center Concrete Coupling (s) Cross Main Cross Swing Check Valve Deluge Valve Density Pipe Diameter Down Ditto Dry -Pipe Valve Drawing 90 Degree Elbow 45 Degree Elbow Elevation of Highest Head Above Flange & Spigot Piece Equivalent Length of Pipe (actual pipe length plus the equivalent feet of pipe for any fittings in that pipe) Flange & Spigot Piece Fittings and Devices Flange Friction Loss Gallons Per Minute Gate Valve Hanger. Hose Demand Required at F&S Hazen Williams Coefficient in. Inches Hydraulic Reference Point Inside Diameter Junction Where Bulk Pipe is Connected to the PCM Large Orifice Sprinkler Long Turn Elbow Primary Cross Main (front cross main of a gridded system) Pressure Loss Due to Elevation Pressure Loss Due to Friction. Pipe Number Primary Loop Number Pressure at Hydraulic Reference Point Pounds Per Square inch Total Pressure in PSI Flow (gpm) Remote Area Reducer SCi[40 SCM SCR SL STL SP sHEET 71 c:1 21 Schedule 40 Pipe Secondary Cross Main Screw Secondary Loop Number Steel Split Point (signifies a discharge point where flow is added or joined from the clockwise direction and the counter clockwise direction) SP .0fQ discharge SPKR(S) - Sprinkler(s) T -- Tee TOS Top of Steel TW -- Thin Wall Pipe TYP - Typical U.N. - Unless Noted VEL (FPS) -- Velocity of Water in a Pipe Given in the Units of Feet Per Second - Victaulic - Water Flow Switch - Unit Heater - Center Line vzc S H Pipe Numbers As Shown on a Sketch or Piping 'Plan •- Hydraulic Reference Point As Shown on a Sketch or Piping Plan - Denotes the location of a discharging - sprinkler head on a branch line as_•shown on a -sketch Flow direction in -a pipe - . Loop Number - Riser Location - Column line 071 11. , TIRE DEPAREa EN WASHINGTON SURVEYING & RATING BUREAU UKP r Park _poet s Tt0"NT�. ‘1416v1".-■ = ULIC CALCULATIONS For '' C 241. 2 70 re...4v.Se. Sheet By Date Job No. 1 1C9 -to7 Nozzle (dent. & Location Flow In G. P. M. Pipe S1Ze Pipe Fittings & Device Equiv. Pipe Length g Friction Loss psa. foot / Pressure Summary Normal Pressure NOTES q •1 Lgth . cs o 3 Pt 3 1. G $ Pt/ 61 k 4i' 1, 90 7 D` / Fit Pe Pv 1 0 1 11 .• .S Tot 4 Pf PI Pn� VS H L o -15 5 Lgth do(. Pt 3 1.4 g Pt 6 7 /1) Fit Pc Pv • 02.46.& Tot C Pf .v3 pn '- q 24/. b � Lgth .011 "i Pt 3 1. 7 Z- pal 1) 4 Z. t Fit Pe Pv Q 4-1. J Tot 1 :r Pf s 2 t) Pn 1- q y/•. � Lgth . c, Y Z. Pt .31. 2 rr pi(I6) 4.1.7 et : , Fit Pe Pv Q 7 /C1.3 Tot /...s pf . g Z pn 1 q 2')' .. S Lgth , V? 1 7 Pt 3 Z Z. 3 "' NO s) Fit Pe Pv Q q 73. 3 Tot /0 Pf .71- Pn , i i q 2'6.7 Lgth 2,0 0/ u. ; Pt 3?. o 4, Pt(l '19 ¢ 7. 1 u 7 5>c C Vac Fit S,/ / Pe Pv 01220,0 Tot 7. / Pf .77 Pn 9 L. Lgth 6.r: o .4.7'i 3 ?`/ Pt `> > , Pt0 3 ) L -re' Fit / 2 . G Pe Pv Q 1 2, Z0,0 Tot 77.6 Pf .3.'f / pn q &, Lgth 5'4. . 0 2 < (. Pt 37. Z y Pi 1 Z i 5 )t G Fit 33.7 Pe Pv SPC. • r /7_..... Q 5 c.. , 7- Tot / .71. 7 • pf .2,`. .2, 9 Pn 9 Lgth 7 4 ,O 1 o Y Pt • f o. C. Z Pt 1 Fit 3 S Pe Pv Q ' '. „ Tot / / / pf / . 1 5. pn 9 r`"-" Lgth PtT/.77S5 Fit Pe Pv Q^ -...---"s- --lam __„---T `""".lin -`'_. 9 w Lgth 4 5 ,elf/yr/ Pt "1.7. 'i Pt/ Z) Fit /2. G Pe Pv Q 4 6 0 Tot 77. G pf /,. 01 pn 9 s Lgth / F' .4 310 Pt 3 g •3 3 Pt .! v (_ Fit .5 . ' Pe Pv Q L'•• ° Tot /v .7. / Pf 3.4 O Pn q G Lgth Y...s ." .. a/Y/ • Pt -21 / '4/ 3 Pt C X •9 Fit 7 Pe Pv Q ., ( o Tot/03." Pf / .Y pn 9 Lgth 2 0 p 361 Pt ¢3, 3 Pt 7" Fit .3 `7 Pe Pv / / Q es {1Tot �3 .5-!' y Pf :2-2- Pn S WASHINGTON SURVEYING & RATING BUREAU HYDRAULIC CALCULATIONS For J • '.— • -. A E 1 c t Sheet 2 of 3 By Date iV -Lc' Job No. Nozzle !dent. at Location FlowPipe In G. P. M. Pipe Fittings & Device Equiv. Pipe Length Friction Los. p.s.i./foot Pressure . Summary Normal Preasure NOTES Se... .. -c- q 1 Lgth Pt; 1 .. (.`Y Pt l8 1� , - `/Z. . Fit Pe Pv 1 O 1 Tot / '' Pf — Pn ' / a 2 Y 1. i Sr Lgth . avert Pt y , . G s Pt t C " •t 2 ci .. . Fit Pe Pv Q 3 11. S . Tot / v . Pf •'3`1 Pn P L- I q .Ly � . S! S gth . v 2 ; ar . 7 Pt 2 ..-•47- . ei a 1 it F PePt Pv Q .55 3. 3 Tot / P Pf .2 \ Pn 6 t. I q .Z 4f 2... J Lgth , 'Y1y Pt 32.. - Pt Z i `l 1 . Fit Pe Pv Q 7 T4 . / Tot /o Pf .?'t Pn �t 2. q •zY4,O 3 Lgth . 4151 Pt 32..C/ Pt Z2_ 4 2 .7 Fit Pe Pv Q/aLAI . i Tot / 0 I Pf . X/ Pn r Lgth 7 D./ 04 Pt 3 3 .3 2- PtX3 .i )e L Fit ,S . g Pe Pv Q/ 20.S. O Tot i 2. f pf /, 7 y pn q 6 Lgth • d y3 Pt .3'1 G 1 Pt 2. 3 A Fit Pe Pv Q 1 2.43. Tot 1 1 Pf ,Ya Pn q 7 s 4 Lgth .°`'8 Pt 3.. 4/3. Pt 2 3 xci • • Fit Pe Pv Q.17 laJ Tot S t Pf 2. 'i Pn q / l Lgth S Y j Pt.- .?1? Pt Z N . /-% �S• Y Fit . Pe Pv Q /2J,) 4-,4 .'4 Tot G3.Y 'oyf Pf .3..'4 Pa q 8 Lgth / 0 ' /+ / Z pt err , .' G Pt Z's" 1 . Fit Pe Pv Z. Q t gO Tot / 0 Pf , / 2. Pn q 3- G o ' Lgth 2 C . 6Ly3 A4 i,le .) Pt Z T Fit 3 / Pe `11. 7 7 Pv Q1h1-/0 Tot G r" Pf /,se Pn P. L G b q Lgth Pt `f 3 .1 a Pt(i: ) Fit Pe Pv Q 2SGu Tot Pf Pn q Lgth Pt 1 3, J 0 Pt A u- / > Gr C Fit Pe Pv 0 • Tot Pf Pn q Lgth Pt Pt Fit Pe Pv 0 Tot Pf Pn Form 139 For WASHINGTON SURVEYING & RATING BUREAU HYDRAULIC CALCULATIONS e `1 S -r . N 0 1L,- v•St.). Skeet By Date -i1 job No. Form 139 Nozzle !dent. & Location Flow !n G. P. M. Pipe S1e Pipe . Fittings 8c Device Equiv. Pipe Length Friction Loss ps.i./foot Pressure Summary Normal Psessnre NOTES Lgth Pt 43.50 Pt(3S) 33, S I .t -AV FitPe / �. 1 ? Pv Q 2$ �► Tot �- 7 v 4' Z 3 Pf 1. f ti po a. �6 Lgth 2 Pt S `f . / Pt GI/'�' Fit 1 t1 Pc• Q ZSva Tot Z1 ° `�i1 PF 1. 0y Pn A 1< -- q 2 a f J JAZ Gr' 4 ' c L' ✓ Q "7 �' 0 Tot I Z - b ( PF . 7 Yi `---^— Pa R t' u Lgth —3 D �' / . �� Pt 3. fo Pt twar4r.4t �. Fit S pe 2. V 0 po/d r' ciy, Q 2.7 0 Tot ! C,. Pf h • J` Pn fi •DL/t° m Pc Pv Q34Sto Tot d "i �_ PF 7: 'l Pn q Lgth Pt �U.rJ0 Pt 147" �.I.•o"0- rO A / H FitPe Py/ L r' /`7 QFitTot PF Pn 4 Lgth Pt Pc Pe Pv QFitTot Pf Pn 9 Lgth Pt Pt Pe Pv • QFit Tot Pf Pn 9 Lgth Pt Pt Pe Pv QFitTot Pf Pn 9 Lgth Pt Pt Pe Pv Q Tot Pf Pn q th Pt Pt Fit Pe Pv Q Tot PF Pn • L ch Pe Pt Fit Pe Pv •Fit Q Tot Pf Pn 9 Lgth Pt Pt Pe Pv QFitTot PF Pn q L th Pt Pt Pe Pv Q Tot Pf Pn Form 139 For ' WASHINGTON SURVEYING & RATING. BUREAU HYDRAULIC CALCULAT • NS 1_,r. ' 1 N 0• 2.41. (1Z. C.. b Sheet By Data job No. Nozzle Mont. be Location FlowPipe In G. P. M. P' pe Size Fittings & Device Equiv. Pipe . .. Length . Friction Loss p.s.L/foot Pressure Summary Norma! Pressure NOTES q S Lgth ?' w _04/ / Pt Of. ` Cr Pt1 c ) Fit Pe Pv . • C3) Q 1.1 2 .. Tot /0 . PE .0 / Pn - I (G4 0 241 . S S Lgth . (/// Pt _3/ r C f Pt(1 b) Fit Pc Pv (q) Q 3C1•0 Tot / G PE .// Pn q 2'!/. 5 Lgth • ; 6Z1 Pt 31. 3 0 Pt 61 J Fit Pe Pv (is) Q 5? . 3 Tot /G Pi .2y Pnff 1 2. q 2 y2 .'t% Lgth . &5-1/ Pt -?2 .0 q No (0.) . Fit Pe Pv l (2 f! Q237, 7 Tot /0 Pf .5Y• Pn L/ q z' 5. I S Lgth .. . ° 873 Pt 3 2. 6 3 Pt I S . Fit Pe Pv r `7, Q/O'Z. F Tot /0 Pf . 7 Pn f q 2-ey. y. S- Lgth Z . / Z g. Pt 3 3, S Pt 1 q. s x G 4c.. Fit .•1-. / Pe Pv (3 3) Q / 3 31.2. Tot 7. / . Pf • Sr / Pn c ( Lgth Co c . °S 17 Pt 34.41 Pt 13 V,� ffL Fit 12. 1. Pc Pv Q 1331,2- • Tot 1/. la. Pf 4.0 I Pn $O1 q•s, 5 Lgth 1 3 3 02- 3 3 Pt 3' .92... Pt 1 L v,.- Fit 3 3.1 Pe P: ;td' Q..•3o. 1, 7- Tot 1 L1 .7 Pf 3. fe$ Pn q 6 Lgth H / • ,461 9 Pt I- -Z. .3 d Pt • Fit 31 Pe Pv Q 5 3 D.-- Tot 7e Pf .77. Pn • • q •- Lgth . - Pt 13„02 Pt2S" Fit Pe Pv Q Tot ..• • Pf Pn `I ` • Lgth Co . 6 t d Ile Pt 3 2.4'1'2 1411-L) • G .-4- Fit / 2. 6 Pe Pv > Q $u 1 Tot i 7. 6 Pf 1. L . Pn q 6 Lgth / 37. o °v/9( Pt3 % • 9 R' Pt S/0 4 Fit �', / Pe Pv Q g 0 • Tot / 3f'. / Pf (a. t1 v Pn q Lgth g p .02-4". Pt 16.. 2 g Pt 7 4 r e Fit 47. (••• Pe Pv Q 6,- / ' Tot 11-1. <- Pf 2 . a 7 Pn q . Lgth Pt / /`. 4 5- P(3 r) —r. P a dc R ♦ C e-.�. Fit • Pe Pv Q Tot Pf Pn S c r 3 For WASHINGTON SURVEYING & RATING BUREAU HYDRAULIC CALCULATIONS So: cn C 7' Na 6 Sheat 87 n#\ ov Dat. Job No Nozzle Ident. & Location FlowPipe In G. P. M. Pipe Size Fittings & Device Equiv. Pipe Length Friction Loss p.s.i./foot Pressure Summary Y Normal Pressure NOTES q Fit • •D u/ 2 Pe Pv r31 0 /29 Tot 4 Pf .vI Pn H.G . c 7S Lgth r . G 0 Y Pt ji. {.4 PtllA Fit Pe Pv , Q 2-0.Y Tot ¢ Pf °Z. Pn 1-- 2'{ Lgth Pt 3 I . Z / Pt ?_ o q /.:v • Fit .0/(,G Pe Pv d k:'4'2.�101 (R) Q tiYS.G Tot /O Pf .r1 Pn t.:./ q 2Y2.3 S Lgth . •6376. Pt 3?..$l Pt 21 47...c1 °I Fit Pe Pv. GS) (2 6 27 9 Tot / 0 pf . .3% pr. . 2. q L'1 3. O ,� Lgth .04/a Pt 3 2.2 � Pt 2.2 41. 1el Z Fit Pe Pv V) Q1301 Tot /0 Pf -66 Pn 2 YA(ZYS.� q /43 •1 '� Lgth • 0 g T3 Pc 32.9 Z Pt Z3 4 2,19 G Fit Pe Pv • 6) 0/094.( Tot /0 pi z.32 pi, H L q 7S S Lgth /S.O /no6. Pc 347. 2...? PtZ3A S is Fit S . I Pe Pv Q1ICA.0 Tot 2O.( Pf .•O2 Pn q •Fit 6 Lgth .¢ o 0 Y 0 7 Pt 37.2 4 Pt Z. 3 /3 Pe P. - Q •// G'. C Tot 4 O Pf /, e 3 Pn q 4. Lgth C t • - •V �°i 1 pt 3t, S!' S Pt Z.Y Z --,r- Fit / Z .4 pe Pv Q i/69. 4 l Tot . 72 t Pf ..�, o Pn q .5-30.2.Lgth C Z. C. . •o&/Z Ft 't a•01,.) P42 S) I 7•• At 3 a' Pe 9Z. ,.9 Pv Q/417.1 Tot 6'/ P1 9k .9:f Pn • q Lgth Pt 17. }t Y PC3 &) TOP p hc R1.5 C 2 Fie Pe Pv Q Tot Pf Pn q Lgth • Pt Pt Fit Pe Pv Q Tot Pf Pn q Lgth . Pt Pt s Fit Pe Pv Q Tot Pf Pn q Lgth Pt • Pt Fit Pe Pv • 0 Tot Pf Pn Form 139 �a$tr r3 9 For WASHINGTON SURVEYING & RATING BUREAU HYDRAULIC CALCULATIONS Sy S T CrY N 0 4 Nozzle !dent. & Location Flow ' In G. P. M. Pipe Size. Pipe Fittings & Device Equiv. Pipe Length Friction Loss p.s.i./foot Pressure Summary Normal P((''ressure NOTES . 9— 9 '2t .t en. Lgth L1 • , 0 `11-3 Pt -48. V 0 PA 111X'7t.9.4t.� �'•� 33.S 42.G74 AV G u Fit 21. 1 Pe / ¢. S'Sr- Pv Q 2 -SO 1 Tot 4 g . I. Pf 7_ 0 C Pn K .4G 1�S R a x,o o ii O Lgth 4.O r./V4..) • G . 0/ 35 Pt a S.../ 3 A7' Pt 6. S e 0 Its J I; L?E Fit �k Pe Pv Q 7.. 1 Tot 12 Pf i• -7S) Pi q 10 Lgth _S2 a .0/ 3? Pt 47. Z 1 Pt . 'i Cr, 4 s 04 • D. C. 2 T Z v Fit / a, 2. O o Imo---- / O Q 2.7°I Tot G 3 7 Pf .51,6'5 Pn . `/ J PG , q 7 r u Lgth Pt 7 Y O ( Pc /1-77 /2.'" Ger } 'r • Fit Pe Pv "•! "- A Q 54S-1 . Tot Pf Pn 4 Lgth Pt Pt Fit Pe Pv Q Tot Pf Pn r 9 Lgth Pc Pt Fit Pe Pv Q Tot Pf Pn • . q Lgth Pc Pt Fit Pe Pv . Q Tot Pf Pn q Lgth Pc Pt Fit Pe Pv • Q Tot Pf Pn q Lgth Pt Pc Fit Pe Pv Q• Tot Pf ' Pn • q • Lath • Pt Pt f, Fit Pe Pv Q Tot Pf Pn • q Lgth Pt Pc Fit Pe . Pv Q Tot Pf Pn . q Lgth Pt Pt Fit Pe PV Q. Q Tot Pf Pn `t Lgth Pt PP1 Fit Pe Pv Q Tot Pf Pn_ a Lgth Pt Pt Fit Pe Pv Q Tot Pf Pn • Form 139 For �. s E WASHINGTON SURVEYING & RATING BUREAU • • HYDRAULIC CALCULATIONS ' By Date Job No. Nozzle Ident. & Location Flow In G. P. M. pipe Size Pipe Fittings Device Equiv. Pipe Length Friction Loss p.s.i./foot' Pressure Summary Normal Pressure NOTES q I"4 Lgth . 11$ Pt 23. 7 7 Pt A . . Fit Pe Pv o 39 Tot /v pf 1. 1 c Pn q 4 e aFit Lgth - . 2- °I.. Pt Z . i 5' Pt Pe Pv Q l 5 Tot / 0 Pf 2-0 ) Pn 4 z . q 2. Lgth 4. S- . 13"1. Pt . 7. Pe -7 - T Fit / Pe Pv (3) 9 120. � . Tot /Q • S Pf I. 9 1 Pn q• Lgth Pt 2 k• 9/ Pt C .. /C 2.2'.93 Fit Pe Pv Q Tot Pf Pn . q i 2_- Lgth 5 , S . 1 -31- Pt 21. oQ Ptd T Fit 1 O Pe Pv U PSP. (31 Q 1 2,.0. L . Tot I i . S Pf ... t, C Pn q 1Zu. c i 2.2.. R At Lgth / '2- °2-2- Pt R' . oS Pt C•• T Fit / 2. Pe Pv C!') Q,Z'/,� Tot / 3 Pf 22,63 Pn q Lgth Pt 3 /. G 8 ' Pt f< 7-.1/2. = f'2,707 Fit Pe I pv ,L q s / Lgth .//8 Pt 23.17 Pt Fit Pe Pv . 1Gar Q. 3y Tot /v Pf B.i& Pn )S q v • /z., Lgth ' , 2 v Pt Z V. 4 .S Pt Fit Pe Pv Q 1 / Tot • 7. pi /. Fil' pn ry d tar q 40. 2. Lgth 4,..), 3 ' Pt A C. 80 Pt . • • -r Fit / v1 Pe Pv Q f lcf.5 Tot /Y.$ Pf l•a/v Pn q Lgth ' Pt .. • 70 Pt Fit Pe Pv • Q / )•J. 2 Tot Pf Pn • U(�P. q 1ZO.L 2 =c. Lgth i • z O 1 7.. Pt 2.1.0S' Pt —j`" Fit / Z Pe Pv Q 2 `Nk's Tot / 3 Pi g, 2- Pn q . Lgth Pt 3 / • (,,► 7 Pt /< . 4/ 2. 7 y 2. Fit Pe Pv Q Tot Pf Pn q Lgth Pt Pt • Fit Pe Pv Q Tot Pf Pn Form 139 WASHINGTON SURVEYING & RATING BUREAU HYDRAULIC CALCULATIONS For G Sheet of y By Date Job No. Nozzle Iclent. & Location Flow In G. P. M. PiSizpee Pipe Fittings & Device Equiv. Pipe Length Friction Loss p.s.i./foot Pressure Summary , Normal Pressure NOTES er if• I 3.- Lgth . a S "I t. Pt 2-.3.1 ../ Pt Fit Pe Pv 0 3 5 Tot I a Pf .54 Pn 3`f. s 2 - Lgth .. 64 O Pt 2.'/.3 3 Pt • Fit Pe Pv ' Q ie.. Tot cj Pf ,s?r Pn .Tvli t) n q 3y, 2. Lgth ,, 1 Z.'7 Pt Z r'. 87 Pt Fit Pc Pv ' Q :i 1 7 . < Tot q Pf 1•1'7* Pn `1 -' • Y % Lgth 3. 3 • ....! ! 9 8 Pt 2 4 .. O t Pt '` Fit I U Pe Pv Q 6-g•3 Tot . 13. 3 Pf 2 .9 2 Pn q Lgth Pt 2 k.13 Pt - Fit Pe Pv Q Tot / Pf Pn q Lgth Pt • Pt • Fit , Pc r Pv • Q Tot . • Pf Pn ' q 2. Lgth G ? • , 1 32 Pt 2 7 • o 0 Pt . Fit /a. Pe Pv 0 re 3 Q 120.( Tot 'G.7 pf 2...Ze7 Pn q t rq . b 2 z Lgth 1 ,'Z. 6 6 Pt • .2. I. 2 v Pt f Fit i 7.Pe Pv Q .t 7 9.` Tot 1 3 Pf 3. 4744 Pn _�k Lgth Pt 3 2 .6 G Pt o. 9Z 6 Pe • Pv Tot n q. 2 Lgth / /. 3 2. Pt 2. 7-0 0 Pt • Fit /o Pe Pv Q /lei, b Tot / / Pf I . Pn • q Lgth • Pt 2 e. v.. _r Pt Fit Pe Pv Q Tot " Pf Pn q 't— Lgth 7 . / 7 1-•. Pt Z 7. o 4 Pt ' Fit / ci Pe Pv • Q f L o . (,, j Tot / / Pf 2 , 6-1 Pn / 2 2 $ Z - Lgth / s 2 OL Pt 2 . '1. 1 Pt Fit / 2 -Pe Pv Q2`/3.V Tot / 3 Pf 2.4 e Pn q Lgth Pt 3 2- . / 5 Pt /< •- .4 21 %c7 L • Fit 1 Pe Pv Q Tot . P1 Pn Form 139 For L a •t WASHINGTON SURVEYING & RATING•BUREAU HYDRAULIC CALCULATIONS '3%1 #4U ' Sheet By Date • Job No. • . Nozzle !dent. & Location Flow !n G. P. M. Pipe -"ze Pipe Fittings & Device Equiv. Pipe Length Friction Loaf p.s.i./foot• Pressure Summary Norma! Pzeasure NOTES v g v P Lgth / ° al , 21•`7.3 pc . - • Pc / • yS o Oris Cr. Fit �--' Pc Pv 43 RJ O Pf 2' '11_.•1' Pn •.7G Pt/kt 5,5 Pt23:Se Fit Pc ' Pv Q3Sa3 ® Tot Pf • Pn rc,4 Z q 3/ 0 i 1/ , �, 6 Y Pt 23.17 Pt •. Fit Pc Pv 'pcil (zJ Q 7Y.3 Pf •I • �Y Pn q 4U . S Z ® •. .'!2"t- Pt „7....,_ G 1 Pt ' T Fit / o Pe • Pv Q/14.. ' H 2.3u Pn.i q Lgth .• Pt Z7. 91 Pt• ' Fit Pe Pv Q q ® h Pt Pt Fit Pe Pv Q Pf Pri .7PP •' ' , q , ! -i- � . o l..(G Pt z. 3 .17 Pt Fit Pe Pv ..._ Q 3i. O Tot 9 Pf • So Pn fur u0 q 3 fe. g. 'Z. • ® Lgth .D S g .f Pt Z '1.27 Pt • Fit Pe Pv 011.5. Tot ti Pf ' r;3 Pn q `l y ` g Lgth • Pt 7.-4/* 8v . Pt '. Fit Pe Pv Q I t7••3 2•® . .,"I 2 G Pf 1. z.% Pm • Pt a4.04, Pt• q 40ag 2 Fit . 01 , .2. I 1 Pe Pv L Q I S8. 1 • Tot /O . c Pf 2 .3° Pn ' q 11g.0 Z— Lath . 2J Pt 2. g.34 Pt Fit / 2 Pe Pv Q.Z.7fl Pf .3,31 Pn q . Pt 3 /, 6 7 Pt Fit Pe Pv Q Pt PnLgth ®Tot Pt Pt q Fit Pe Pv 0 Pt Pn q • Pt Pc Fit Pe Pv Q Tot Pf Pn Form 139 .4'• + ' • For WASHINGTON SURVEYING & RATING BUREAU HYDRAULIC CALCULATIONS 'tier: -tom By Date Job No. , Nozzle !dent. & Flow In G. P. M. Pipe S12e Pipe Fittings & Device Equiv.. Pipe Length Friction Loss p.s.i./foot Pressure Summary Normal Pressure NOTESLocation 1 �..= q t 1/.). t �iZ 1 • Lgth G . , 1 ,) 31_ Pt 2 '] . 0 " Pt -t— Fit d o Pe Pv - 1 (3 Q IZ,'..(o • Tot. /6. pf 2.Z3 Pn a Lgth • Pt 2-9•L3 Pt Fit Pe Pv Q Tot Pf • Pn q 1 - Lgth • c2S G Pt 2.3.1 7 Pt Fit Pe Pv • • (1) 0 3? . Tot 1 0 P1 ...5 ‘ Pn q 3 ct• 1.. Lgth • D Pt 2 33 Pt Fit Pe Pv (Z 1 Q 7 I. j • Tot I Pf 16° Pn q 3 `l ,1 Z • Lgth ' . I Z.1 Pc 2 1.7 3 Pt • Fit Pe Pv . (31 Q I 1 Y. L( Tot j u Pf 1. Z1 Pn . q 40 !Lgth .1' 3. 1 . Z t 'Z Pt 2 C . 1 ca Pc . 7— Fit I •+ Pe . Pv i °r' Q j S1'. 3 Tot 1. r( Pf 2.9 Pn q Lgth Pt ..Z.1./0 Pt Fit Pe Pv Q i s . 6 Tot Pf Pn q 120 . te Zs -"L Lgth 1 Pt Li', Z. 3 .Pt Fit � 12,, Pe Pv CO Q2to. / ot T/ • • 3 • � � G Pf 3.'1L Pn q - Lgth Pt 3 2. 6.9 Pt JA Y cj ea `j -- Fit • Pe Pv Q Tot Pf Pn . q Lgth • Pt Pt Fit Pe Pv Q • Tot Pf • Pn q •Fit Lgth Pt Pt . Pe Pv Q Tot Pf . Pn . q •Fit Lgth Pc Pt Pe Pv Q Tot Pf Pn qFit Lgth . Pe Pt • Pe Pv ' Tot Pf Pn 1° q Lgth Pc Pc • Fit Pc Pv Q Tot Pf Pn Form 139 .;ONTRACT NO. NAME LOCATION 5ECLAL.E_ PRor ERANCFI LIMES 19 Zo SHEET NO.L�QF. -DATE .35 ?+l.Sx i2.S -31.7 NOZZLE TYPE a LOCATION FLOW PIPE IN G.P.M. SIZE FITTING & DEVICES PIPE EQUIV. LENGTH FRICTION LOSS P.S.I./FT REQUIRED P.S.I. --WfD..-- REF.PT 0 --..:_... • -.. ELEV. . .---,--- NOTES PT 9 is, 0 31.i 1 FTG. PF .78 i. O rr- }c -g Q 3 1:4 TOT 12.5 .o I<0 PE LGTH. PT 10. Z7 / G • 7 k =r3 Q 32 t TG. . ltd Pr 344 3.1 O Gy 3 � ..�.-. ' QT. t2.5 . 7- 1 7 PE 34. , T .8 GTH. .. PT I9.9I 2o.Ya k - 8 0 35.7 , TG. :.O .4I --3-e PF 3.70 3 .1s auy asict45 12 QT. LI .8 .3114 PE • PT 2'3�o I TSP of R1.1 QGTH. FTG. PF - Q . MINIM PE GTH. PT'i4.4 - • Q + TG. .. 0`743 F. . 9 N a r .f4 •c: -i •7 14 -4sr,, OJAI.- q OT. tz,z P -r GTH. PT , 1 IS = 8 Q>src t FTG. . 2751 PF - 065•r 14 OT. 12.5 PE T= 8 : GTH. 8.8 - PT +gr: `75 k• -'s . 0 t T • :-2451 P F -u44ii /po, A Q.3 { z .: OT. 1(0.8 .3 + 1 (3 PE GTH. PT Z :Z" - 'To? o,F Ru o TG. PF S• Q OT. PE 0, 1'_oy, T= 2 GTH. 1.2* PTS -3r; ciz Tot" of ev. ./ . o FTG. -S / D . .3,51-- .kt ` PF•.1A - .2s.7y cr s"F-1) Q _ .b I t. -z. TOT. 9.z. .3. z.-0, r-+.0wS LGTH. PT33: S•1t B t95.S_ Q Pr 11 k= 33... FTG. - Q TOT PE k/33.84 - LGTH. PT a FTG= PF 1 • I - Q TOT. PE TH. PT o FTG. PF Q TOT. P LGTH. • - PT o FTG. PF Q TOT. PE LTH PT 0• FT PF 0 . TOT. PE L. TH. P 0 FTG- PF Q TOT. PE GTH. PT . Q FTG• PF q TOT PE • LGTH. Pr o FTG- PF 0 • TOT. PE LGTH. PT • o FTG- PF O TOT. • PE PT .3 03 •1\9.h\E. 11/29/77 (AR%taw= I FIRE ?Wm:2=Kn.1 , • 771 nis ±REE.T ZZ 24 II N LRo5sMA%14 E GRINNELL FIRE PROTECTION SYSTEMS CO 'INC. K GPM H+L4 120 LINE 33.50 20074 181 2.138:8 28,4 iz 14.50 TOTAL PIPE GPM ID LINE NO. 200-.4 4.12 446:614024.12 7-761 .6 4.12 710.1. . 7751.0 4o .71 EOUIV FT 8.2 10.0 29.2 - 121.56 TOTAL PF/L'. PSI PAGE NO REF PT NOTES LINE 8.00 8.00 8.00 8.00 LINE 8.00 8.00 8.00 4 • -: //Ft% 1RF_ • F i t0M 5 EL.ALE. 771 SYS 1� 'GRINNELL FIRE PROTECTION SYSTEMS CO.,INC. 14:34 TOTAL PIPE EQ�TPF/L RSI PT� TOTAL REF GPM � GPM Iii LINE NO. 39.0 39.0- 40.0 79.0 44-r& .420-r6 2Or6 4477 + 1' x.1 1.38 1- 2.07 2.07 10.0 10.0 10.0 11.0 .zz � 1.18 2.05 4.49 T1.99 - 2.3.77. 0 24 95 . . .G. TOP OF RN -- 23.77 0 .56 24.33 39.0 39.0 1.61. 10.0 2.03 24.3b. 39.5 78.5 1.61 10.0 nP OF RM -1- s 3 -3 -T -88\_ I T1.Y • -t 41.1 119.6 2-41izo• � 2• 1 `t•0 �s^• LINE SUPPLY PIPE VARIATIONS 07 47.82 16.4 1.56 pi 11 .3-0 30. • BRA.14614 Li 4Es w 17 IB GRINNELL FIRE PROTECTION SYSTEMS CO.,INC. 11/04/77 17117 TOTAL PIPE EOUIV K GPM GPM LINE NO. H+W= 120 LINE 8.00 8.00 8.00 LINE 8.00 8.00 8.00 30.3 31.3 34.6 31.3 32,3 35.7 -10 .3 LINE SUPPLY 38:72 37.37 33.50 30.3 61.6 10 0.4 31.3 63.6 X99:3" too.y ID FT 1.38 1.38 1.61 . 1.38 1.'38 PIPE VARIATIONS --200 2:47'7---13--5 20074 2.07 11.5 3T09 4.u." 28--75 208:4 14,64 SfEEr 24 c:P Zit PAGE TOTAL REF PF/L. PSI • PT 14.39 12.2 .90 15.29 12.5 3.43 183-.72"""-' 12.8 2.275.60._To? OF- Rlei .311c. f."4- NO NOTES i .1. 16 .12.5 12.5 i5,8l .31:74 • .98 3.6.4 15.29 16.27 197-9t 7-J'- Fl.Ow $ALA NGE &a/ Z 2.50 2 0"..4 71113 = 33 . SC) MggEniql-1 CEC 121977 GRINNELL F.P. ENG. RENTON WASHINGTON SURVEYING AND RATING BUREAU Alaska Building P. 0. Box 1168 Seattle, Washington 98111 2 SHEET 7 OF D - . 19 ,7 SUBJECT S" /4 4— E Pe'' ~7 -7 ' / VI{ Wu A LAJA3 The attached plans have been approved as meeting requirements for classifica- tion as a sprinklered risk. The following revisions or additions to the design as shown would qualify the protection for improved rates based upon information shown on these plans: /. 43/ ?' l:..r ,.SAr/ C) w .v ,4 • Act_ if=._,r-a 7' /1 4_, d'. "r "17. ,/_r .4'T" JAL /-: id4.A NT"J C4J/L L- / r ,, /N�e',ozwQE'N 7 Of -r/-/ /0 / cN /11,NS AS Ga >*t a.o ft-. '7-14 > . L. a T T— E n.. o r S %.. Gs A k- C.' V S 1 l+: r'* S S r•-• t[,s . fra - 2• Pio a V/ o c' /1 v O ;=" 0/?,4 r r "-- G v /4 / r/ s S O'4 c E a, ..i, �rOde-/z /0O ) / �•c) 0, r". 3, .---.1x --L s.. c ...5—e'‹ ' r.. K /. E. rt, /4.R o T— efl!' e- 7' . , r.. 7".0 ' E -X 7 ' f o d AN 0/" / Er 5- h." -7— '. Me £/A E LE A, 4- 2.. .S vC AA-- / S r V, rt /1 G a 44 -1‹ f.c Bea ,44 A, c X. t r.s - /4 5 iv a sr—e- o aN J.,, 7"4— 2� 6 `J •'/ /..#4.0 4 -et. E?(T42fo4.' S),c.c,-r1, OVER N .r1a so4...t 4- . Pa J d/ 0 4 SY s r 4 /`T 0 L //v,,f' /Q c- //os 4 "A iv 0 /4 Ex's GS'N a 4r •••• 7 -z -.y ' .-.7- -3 rew.•vK - E -z.. S Y .S' r4 - ,rs- , APPROVED BY WASNNIUON MESE & RAUIIA IIMEAV SEATTLE WASH. DEC1l1S77 As meeting rom rements of this 8rueau for—dassific2tinn at Cf rinklered: however, system changes or additions as recommended on the attached .hepro) wdt result in improved rajas. ACcentepce IRIS'S to plans as submitted and for construction and occupancy show tnereon. Finished installation subject to inspection for final acceptance. Al comments, approvals and .. f relate eludeeively to relative affect of various conditions enn. a instuaece rates They are not 0 be construed as besting in any way upon the question of whether "doe care" has been exercised with respect to possible liabitity for persomt rnpiry or aamage to property. 'tit recogmcea TIM Ramos wn1Nt mp result in loss stilt e 5n'. For S G A WASHINGTON SURVEYING & RATING BUREAU HYDRAULIC CALCULATIONS Sheet I A of By Date I z - L.- 't 7 Job No. 1. Nozzle (dent. .& Location Flow In G. P. M. Pipe Size Pipe Fittings & Device Equiv. Pipe Length Friction Loas p.a.i./foot Pressure Surnmary , _ Normal Pre sure NOTES /'4..e• 44 .e ?_._ y q 5 Lgth v o 1 t.. Pt 3a,4/t. PtIl. l:.-4?.i4. Fit Pe Pv O i Z-1. 1 Tot 10 Pf , o L Pn 3 ..,.. .?...i.:. C. o ' Lgth . '1 14`t 'i ' '' " r pt"/3_) Fit ..Pt Pe Pv Q 36 1. 7 Tot ,1 ca Pf 1 I pn yY j. .S Lgth. u g° ? Pt •'''1•6'..' Pt'i v 1 Fit Pe Pv Q ',/::: . 7 Tot / Pf • 3 / Pn q 2 y .., 3 6 Lgth , 0 SS Pt 3 u• Z/ c Pt % 1 Fit Pe Pv Q Y 5 7. Q Tot / .-.' Pf . `S Pn q Z+Z. �' Lgth 1 "l. t Pt F t. `19 Pt <a A. . , Fit Pe Pv Ql 1 t 7 .1? Tot / ,i0 Pf . t ' Pn V7 q J.Lgch .°S • • it °f ' Pt ? • A"1- Pt 7 ' /< . . Fit Pe Pv Q12.'•1.1 Tot 93.x Pf 1. i'3 Pn L-' 1 q 7 5 Lgth / .q....1- • 7zYZS` Pt 3 7.- C Pt t f S k G Fit J". / Pe Pv Q /3o?, I Tot 7. 3. G P1 2.1 3 Pn qz.-re- �' Lgth 77. < 6 j0 Pt -1$. / P Pt'r) Fit /a•Y Pe Pv 01 o1 Tot 7. Pf 4. 4.0 Pn 5�� o q 4 Lgth Z.0 .n `t:7 ' Pt 4 '.S5 Pt 2-....-) 4. .ri. Fit f • v pe Pv Q 1 8Ccj, 1 (...eo Tot 70..f Pf 1. 1 /1 Pn q IC Lgth •OZ'r4� Pt YS. 5 f Pc (,t. t) Fit Pe Pv 011061.1 Tot .53..6 Pf I.. .V P q 6 ,r'. 4. , 9' Lgth 4 e. . p i ? -r.. PO I- .7 3 ) PC2 S7 /t•4 '- •'t Fit I- f. -> Pe I1 6 . 'UP Pv /a ✓ .t. Q 2.5. 1 o Tot 3 . ;k Pf 2 • `i 1 Pn q 9 Lgth 3Pt . o .° ✓ ' %. • '7 Pt 3= .S G • r: A 4 64/ / Fit 1 cf Pe /y.S v Pv Q?( 1 u Tot Z .1 Pf 1, G 4 Pn IZ n C. V. q 2 0 o 10 Y.a I- vs t I r n Lgth / Cl 0t4-/0 Pt 6'5 - . 51 Pt 4 •r ' 'c. ..t ...... .Q.. ' t;"i.c ✓ LTE Z T Fit /4 Pe I. 1 Pv Q 21.0 2.6v Tot 3S4 P1 _4 ' u Pn q 8 Lgth 4 G=. z..c, .04 y Pt —I Z.. 3 t Pt . C. 2 C.v Fit X Pe 2.5'o N. 8 " L Q Z -HU Tot . 1 7 Pf . 5 ac3 Pn Form 139 75. 3`I Co -I fit 1 S. 3? 3 7/.7-q Is 31 For WASHINGTON SURVEYING & RATING BUREAU HYDRAULIC CALCULATIONS `• 1 5 -r .r 1..1 S) eet I f; By Date Job No. Form 139 Nozzle Ident. & Location Flow In G. P. M. Pipe a Pipe Fittings & Device Equiv. Pipe Length Friction Loss p.s.i./foot Pressure Summary Normal Pressure NOTES q 5' Lgth , a o' 1 Pt 3 .. • Y C. Pt6 73 • Fit Pe Pv O I I J. ,'1 Tot 3 . < Pf --- Pn l-1 c. a 1. S Lgth v^'A"' Pt F'• • Y C. Pr' Fit Pe Pv 0iela-1 Tot G•<' Pf •.17. Pn .5 Lgth c /7 Pc ., • ' Pt i Q i 4' C Fit Pe Pv O 9.4 z.1 Tot / '." Pf ..17 Pn q .Z5�j.3 s Lgth 0 3.77 Pt 30.6 S Pt 7` -ea . 8 3 Fit Pe Pv Q 7G , . L Tot / Pf . "7-1' Pn q 2...N.1 J Lgth ' •lf i. Pt...3 /, 0 ..i- Pc ,r , it ? . y '. Fit Pe Pv Q 95-3.b Tot /J P1 •'°.4 Pn 9 .Z7?/ i�► Z. Lgth i y . C • 1 as t. Pt 3 / . 7Y Pt 7 9 7 - ,- L ... 1-4 Fit 5 . Pe Pv 012°0, 6 Tot ' 6"►. ') Pf . 7.17 Pn ) I T' F...., w qq 65G0.0.\ t .� Lgth 2. o' .0 3 "?''0" Pt 3 i? • 11 Pts) Fit / `1. 2. Pe Pv Q (r:Yo.G ,c. 1•... V /.. Tot 7.7 i .") Pf . 31 Pn q ‘ Lgth 2 1 _ o / 3 3'7 Pt ' G • 7. Z Ptli) .7` Fit 3 s Pe Pv O -4 v,) • C Tot ..) C Pf •7 5 pnf q Lgth Pt `f7. 3 PI2-k) Fit Pe Pv _ Tot Pf Pn, , �...�' q `�`. J Lgth / r y . o L a 6. f. Pt = E °1 1 Pt(5) T Fit 33.. G Pe Pv Q .S6 b s")• G /40 Tot 1' it 7, G Pf 4-, 4'1 Pn q G Lgth -L / . G lot" Pt 4 3 ..'7 I.- Pt' Z.9 T Fit 3 < Pe Pv Q .8.--"60 Tot 5 G Pf . 52 Pa Lgth ..-...1 Pt I 1 .3O' I425) - Fit--. Pe Pv .t _ - _ .� Q .. _.. - Tot Pf ` __. - Pn q Lgth • Pt Pt - Fit . 1. Pe Pv Q Tot . • Pf Pn q Lgth. Pc Pt Fit Pe Pv Q Tot Pf Pn Form 139 (LR1Nqa1L FIRE iol'ELTtoK1 SHEET 7 OF Z/t 3oB •t AL = sELNLE 771 SYS 3 BIZMICANAmES GRINNELL FIRE PROTECTION SYSTEMS CO..INC. 11/28/77 16:35 PAGE NO TOTAL PIPE EOUIV TOTAL REF K GPM GPM ID FT PF/L PSI PT NOTES H+W= 120 LINE NO. LINE 15.21 8.00 31.2 31.2 1.38 8.0 .62 15.83 8.00 31.8 63.0 1.38 8.0 2.29 18.12 8.00 34.1 97.1 1.61 8.0 2.41 20.53 7.85 35.6 132.7 1.61 12.3 6.59 27.12 LINE 23.77 8.00 39.0 39.0 1.38 10.0 1.18 24.95 8.00 40.0 79.0 1.61 10.0 2.05 27.00 8.00 41.6 120.6 2.07 14.8 1.95 . 28.95 LINE SUPPLY PIPE VARIATIONS 46.86 257.7 3.07 16.4 1.29 30.24 45.56 257.7 2.47 13.4 3.05 32.00 (�1Z\1��tELL FIRE 1 R°TELT 1oN 3oB NIAtt'E_ = 5FLk LE . 771 5Y5 43 Bg.A4C.4lL11SES . 4341i GRINNELL FIRE PROTECTION SYSTEMS CO..INC. 11/28/77 16:42 5HEET 8 OF Z21 PAGE NO TOTAL PIPE EQUIV TOTAL REF K GPM GPM ID FT PF/L PSI PT NOTES H+W= 120 LINE NO. LINE 23.77 8.00 39,0 39.0 1.38 10.0 1.18 24.95 8.00 40.0 79.0 1.61 10.0 2.05 27.00 8.00 41.6 120.6 2.07 17.3 2.28 29.28 LINE 23.77 8.00 39.0 39.0 1.38 10.0 1.18 24.95 8.00 40.0 79.0 1.61 10.0 2.05 27.00 8.00 41.6 120.6 2.07 12.7 1.68 28.68 LINE SUPPLY PIPE VARIATIONS 43.95 242,5 3.07 16.4 1.16 30.44 42.86 242.5 2.47 13.4 2.73 32.01 SOB ,NAN\ C 1K1 Ntitaa FIRE ?RcTEC_ ioN _SELALE 771 SYS 2e3 GRINNELL FIRE PROTECTION SYSTEMS CO.,INC. 11/28/77 16:46 StUEE.T 9 aF Z4 PAGE NO TOTAL PIPE EQUIV TOTAL REF K GPM GPM ID FT PF/L PSI PT NOTES H+W= 120 LINE NO. LINE 23.77 8.00 39.0 39.0 1.38 10.0 1.18 24.95 8.00 40.0 79.0 1.61 10.0 2.05 27.00 8.00 41.6 120.6 2.07 16.7 2.21 29.21 LINE 23.77 8.00 39.0 39.0 1.38 9.0 1.06 24.83 7.83 39.0 78.0 1.61 9.0 1.80 26.63 8.00 41.3 119.3 2.07 13.3 1.72 28.35 - LINE SUPPLY PIPE VARIATIONS 43.88 241.7 3.07 16.1 1.13 30.34 42.82 241.7 2.47 13.1 2.65 31.86 (s.R‘Kt E i FIRE kRoTPL.� tol l 3oS t�lAritE. = SELA1E..MoSEC 771 SYS 3 5itEET 10 OF 2A GRINNELL FIRE PROTECTION SYSTEMS CO.,INC. 11/28/77 16550 PAGE NO TOTAL PIPE EQUIV TOTAL REF K GPM GPM ID FT PF/L PSI PT NOTES N+W= 120 LINE NO. LINE 23.77 A 8.00 39.0 39.0 1.38 10.0 1.18 24.95 8.00 40.0 79.0 1.61 10.0 2.05 27.00 8.00 41.6 120.6 2.07 16.6 2.19 29.19----B LINE 23.77 8.00 39.0 39.0 1.38 10.0 1.18 24.95 8.00 40.0 79.0 1.61 10.0 2.05 27.00 8.00 41.6 120.6 2,07 13.4 1.77 28.77 LINE SUPPLY PIPE VARIATIONS 43.97 242.1 3.07 16.1 1.13 30.32 42.90 242.1 2.47 13.1 2.66 31,85 b SOB = 5ELALE. 771 SYS 43 11/28/77 K K+W* 120 LINE 8.00 8.00 8.00 8.00 AALC.NL ALES d q J GRINNELL FIRE PROTECTION SYSTEMS CO.,INC. 17:01 TOTAL PIPE EQUIV GPM GPM ID FT LINE NO. PAGE NO TOTAL- REF PF/L PSI PT NOTES 19.25 P' 35.1 35.11.38 9.0 .87 20.12 35.9'' 71.0 ✓ 1.61 9.0 4.7.521.S) 22-.-64. 2-t•63, 37.2 108.2 `'1461 8.0 2.94 24.58 2.V.6. 39.7✓ 147.9 4-0:6 -6-7-9-4 y y 311-52 F' z'-1.0 1 10/ 2 1i.., (. .0t. LINE ._7.83 31.2 • 8.00 32.5 8.00 34.5 31.2 1.38 7.7 .60 63.7 ✓ 1.38 7.3 ' 2.13°" 98.2' 1.38 10.8 71-03 oz 160.5 .GS`yL LINE SUPPLY PIPE VARIATIONS 43.73 2 2.47 13.1 .2-r9 9 D 15.86 -mac 16.46 18.59 '✓ , 3 2.q . So3 AIPJ E 11/28/77 6.R\ t1UClL FIRE k)RoTEG.c: tom SELIALE . 771 SYS 43 BRANGNLIt�Eg ` 11 i 1z GRINNELL-FIRE PROTECTION SYSTEMS CO.,INC. K GPM 14-144= 120 LINE 8.00 39.0 8.00 40.0 8.0040;1,¢1-;6 8 0041,x4 -a r. LINE 8.00 8.00 17211 TOTAL. PIPE' EQUIV GPM ID .FT PF/L* LINE NO. 39.0 1.38 10.0 79.0 X12.0 10.0 119.Lt2.07 10.0 1-6.3T2 2.07 . 11.1 tb�•9 39.0 39.0 1.38 10.0 40.0 * 79.0 ..1., 3' 16. i LINE SUPPLY PIPE VARIATIONS 42.68. 2 yj•'2- 243:3. 3.07 16.1 41.70 2 y, .-t_.2.4aT6 2.47 13.1 & E.ET 12. OF 221 PAGE NO TOTAL REF PSI PT, NOTES 23.77 1.18 24.95 2-.45.G1 27--: oty L 5.5- 1.3V S1.32' 2 2- z G• S 3�s Z3611t,gz.31 � • 23.77 ;G Z14::35. 2.g, 113 4-,4 32 -r58 - 244r9 34-V 2 2 6`/ 9 .S1 b 32.0! CUSTOMER ORDER OR CONT. No JOB NAME DRAWN BY SHEET' 18 QF Z1I REVISED BY DATE, DATE x 13t# 194 20 X a. IS ' uo . st MAIM % X X X X al t5 ka FOR MATERIALS AND OPERATIONS SEE SKETCH No. REV PIPE REF. DRW'G. Nos. MARK NO. SKETCH NO. REV PIINTLDIN Y.S.A. STEEL. ./NTRACT NO. NAME GRJNN ELL . sEGAIE. PP.c3ECT 771 LOCATION u .• XMAIN. ' CA ILS SHEET NOt. 9 .OF. 4 DATE NOZZLE TYPE 8 LOCATION FLOW IN G.P.M. PIPE SIZE FITTING 8 DEVICES PIPE EQUIV. LENGTH FRICTION LOSS P.S:I./FT REQUIRED P.S.I. HYD. REF.PT 0 ELEV. NOTES o TW PT.76 PF .31 .o38Z k= 33.L./. Q20-4.1 3 TOT S:2 Pt= k= .5-4,3„, X331. p Tut LGTH. PT 37,07 TG• . ZZ75 Q535,1 3 PF 1.37 QT Co . o • PE 0. TN GT 'T 33.44 REA. YIG.. FTG. Pr ' 29 Q535.1 �. — T. -4.o .027 . PE . k- 5 .3/� R3 8, INN T 22.5 LGTH. Co.7. PT ■ 22.5 , 1200. Q 83.4 4FTG. PF 5-Z6 !i PE 0 - GTH. PT -43.9 27 TG. 0 PF k _ 873.-4 —131 x.43.99 OT. PE .7 . • c,-. is -ie 0 7-w GTH. g P T ,2 R • 9'j . E 3X' 4 /Leo FTG. 8 2.I 2. ( (� q- f.. e. 3 PF . . OT. /6 , o3- PE _ ..... 321, R Q 4 TTI . • . 07 Z 6 ,/ r • Q s3v.( PF32 8 OT. v PE .71 0 3 is. .r GTH. G . 7 .11'1 PT 7.c.) H QS/v�.o -r TG. Zt.S PF s.09 OT 2'7.1 PE - 0 • . GTH. PT37.9 8 2.1 FTG• Q • PF TOT. PE 0 LGTH. •T FTG. Q - PF TOT PE 0 LGTH. PT FTG; 0 PF TOT PE . o LTH. PT FTG• 0 PF TOT. Rd-v.S4 • 0 LGTH• PT Ai" /iv E 0 FTG. PF TOT. PE .�4. o LGTH PT . FT . • 0 PF TOT. PE o LST.8. FTG• Pi 0 PF TOT. PE o LGTH. PT FTG. Q Pr TOT. PE o LGTH. . PT FTG. 0 Pr LGTH. TOT. PE PT - o .. FTG. P. f/ • 305 • 1\1:\?.\F 11/29/77 E EGALE (N. RI N!.:E.a _ FIRE `)R. oTEC T 10 tit 5'/5 3 SD,MC.AL ES # 15k 16, GRINNELL FIRE PROTECTION SYSTEMS CO.,INC. K GPM H+W= 120 LINE 8.00 39.0 8.00 - 40.0 8.004t;6' 8'.00 4 ..t4-449 LINE - 8.00 39.0 8.00 40.0 8.00 41.6 8.00 4.4-;9- 13:29 • :LW& tori kt to +,,-.urii 5tic.ET Zo a Z4 PAGE NO TOTAL PIPE EQUIV TOTAL. REF GPM ID. FT PF/L PSI . PT . . NOTES LINE NO. 23.77 39.0 1.38 10.0 1.18 24.95 79.0 1..-64 'Z 10.0 2.05.6 t 27.:00 Z .5%54 46-201-6 I'1.' -1-vM Z 10.0 .-42fo7 1.3l 31J T 7 . 16-575 2.07 15.0 Z. -Sir 35, -O5r To? oc R�.L Go,' 335 '30.24 :.. -. 23.77 `'0 ----- - 39.0 1.38 10.0 1.18 24.95 79.0 .M 2 10.0 2.05 2.7...-99 120.6 -1: i 12 10.0 -4--49 -31 xf9 G g 7 .5 2.07 15.0 -3 3.5.705- TOP f- R1 t 40..73 ?54 J d 3 •'t-�t r LINE SUPPLY PIPE VARIATIONS -54.36 zargr 3.07 16.1 37.107 ®E 3 Z ice t1 4 fla t i 1 $ t. 2 3 4 4 6 6 7 wk+ "i'w"rr6Y+a f f it rwr 't"T4 "P"' -� 9 orlroriec.ly,rwl ! t 1 IC,1,44,401rs'Ir .1e, trph 110 11 12 APPROVE �a�AF AS NOTED it The drawings affixed hereo have been reviewed and accepfedtas, meeting Or exdeeding minimum requirements of the City ofvTukWila Fire Dept , E3ureau of Fire P ventiorl Additions or revi loris to these drawings after this date shall not be construed as being approved Or view ..1 -197Z .... CITY OF TU �LA ... BUREAU OF FIRE REVENTION k� axri yri R 14; W14 tt A 1 WELtE.0 bort LET TO 3PKR LINE Pit .SEF=M, autic 1J�'T ATL7 �trt2N d 4i r" 4t i 1 � RRE DEPARTMENT TO EE CONTACTED TO t31Tt ESS THE FOUND TESTS 1 tlnrargrtl+ld Visual laspaction �� �; 2 Lr !lard Lir static j1 4 x 3 tiall c raLr1 11141110 .k ','1 4i 1 4 ,1'tiverli A Dir I talct a ct', '0 r „ TOKWILA FIRE UEPARTM JEUT ks 4 575 4404 -Nr-A it 1 (t r� 1, k 1 � T' k a i ?£1,g t 7 '''!1 ro iA• 4 / 1,t 1t-arlt+� 4. , ,r IN 51,61' " , t FROri 71 1 1,7 4 1 1 TOP 6P' tEPM qx 11 f IJNLrt 1,5 to In Tb I' 4. 4 0 13EI;M (r ,. -a-- + ... �� t tib 4D6 4 } ) ,r l i } ��1 .�LTAL Qty CAt.E intoes 1 S ""(7-1"c. 1 It) 1 � .. i . 1, • .7 ' rW S 4 A \ ,1 114 .4•rmk „vim H' 4 LATEST REV 4 1 IMPORTANT LOCALIT ES' SUBJECT TO FREER NG CONDITIONS IT 9 THE OWNER $ RES ONS 8 L TY TO PROP OE HEAT THROW OUT WET PIPE SPR ',ACLU(' SYSTEM AREAS A b IN ENCLOSURES FOR DRY WIPE, DELUGE ANO OTHER TYPES OF VALVES OONTROLLtNG WATER SUP LIES TO S FUNKIER SYSTEMS DATE i 11111111111111111 1111111111111111111111 •0111.111_ 1111.11111111111111111111111111111111111111111111111111111 IIIIIIIIIIIIIII1111111111111111111111111111111111111111111111111111.11111111111111111111111111111111111111111111111=1111111111111111111111111111111.1111111 1110111111111111111 10111111111111111111111111111111111111111111111111111111111 1111.11.1111011111.10111113110.111111 -NIIIIIIIIII -11111111111111_ d REV SIONS MUL.SIfYRE PROJECTORS ACTUATING DEVICES QUANT QUANT SYMBOL CONTRACT WITH These Plans Prepared At KIR. 0 0 go PROJECT f3 FILE No 44-u' TOTAL TOTAL, TOTAL 4. At 5 4.4 .2 a.0 { 6 1� , F 4A t r # 10 12 WASHINGTON SURVEYING AND RATING BUREAU Alaska Building P. O. Box 1168 Seattle, Washington 98111 SHEET OF SUBJECT *-4)-4:‘..:v : 6 I t - �1 P, v T c 7 '7 ( aw 19 ,? '7- V'< W ` q J A a (-{ The attached plans have been approved as meeting requirements for classifica- tion as a sprinldered risk. The following revisions or additions to the design as shown would qualify the protection for improved rates based upon information shown on these plans: Classificacion as .sprinklered is subject to provision of adequate heat in all areas containing wet pipe sprinkler equipment. " ! ,, , AJy 0 , Gt/ /4.. c- 6'4-5.- 7 -A, AG. " . /C)f,v04W ;F.- 7.71 71 / r-� , c;,,_, rt 5 E /t: 0 r 10 2. /., 0V /e,c 7- ' mac' 9'' //'s ov4-re / 6' Y / v 0 0 SP'A c O -a, . /`• .. / " 0 7T• r 7 / . f 7-0 • --->c—a-2 o, C.....4 '.i 0 /4" / Er s /... i E /C M C a , .� -r e L. it' ✓ E I- S v .=` /4 .,-- -5" - -7-u / A G /E' .9 c Ks 8a -A /H PO C/ . e- TS- /4 S. n/ a 7-e o v /••...5.4-1 . r-2 ) 6 c...,j 4"z E?T-'4./04. Sim m,T.( 1-. 71)/ 4 •53".5-7 4 /17 a A— n./ /6 "SvP/[ /a /.it7 .e,'°Gr—" Q' "7 L..Y -5/ ", /N/•< L 4-02 J Y ,S % e /Y -, /N.f /Q G /4/0„..5 O F" ' k".4 /-r .4'A O APPROV BY WASINTON SUNNIo MIN N nv 1 71977 As meeting requirements of thisBMWfor classification the klered; huwnva, .7'stsm changes r avow: on to mans d sheat(s) will result In improved rates. A thereon.asFinished submitted arri fnr cerrstructitxi and ocdupansy shovm Installation subject to Inspection for Tinel accepramar. All comments, approvals kill w Ceptanca /elate exclusively tC �_v .....:..� rnneulatis upon fire insurance rates. They are nott WASHINGTON SURVEYING & RATING BUREAU HYDRAULIC CALCULATIONS < Fos< -•r1 S -r -E . No �. (tZ. V ' se - 1/.7 e 3/ 7 Z Sheet 'JECE1VV€p NOv 16 1977 1 A of By Date /1/ 1 -/7 Job No Nozzle (dent. & Location Flow In G. P. M. Pi Size Pipe Fittings & Device Equiv. Pipe Length Friction• Lou p.s.i./foot Pressure Summary Normal Pressure NOTES q ' Lgth G !, ..GYIi'G Pt 3/. 9 S ptJ ¢ •z %-f Fit /o , sr Pe Pv 0/2.4o Tot 7G. de Pf 3 SC Pn Q 9 k � 6 Lgth 2 =. v .0/ y. z Pt 3. ..S / • Pt l e 6 i. G � 1.re Fit 2141- Pe Pv O -78 6 ! Tot 28 3.1 PE S. Lt 4.. Pn . 9 g Lgth ' `/ , O o y 1p Pt Ie • 9' l Pt 7`" Fit 3S Pe Pv O 7 g° Tot '.S V Pf . 2' Pn 9 Lgth Pt 4/.2. 3 .. Pt() 1 Fit Pe Pv Qy ' Tot -- q --- Lgth i - t •0`'_-)`' Pt,...?S . S f Pt/e 2 -r Fit 7.,Pe Pv Q 4 2' Tot 34c Pf 7.7.1. Pn q --1 Lgth _ _ ...._.—...P1 Pt..3`e • Z .1 Pt / > ' Fit Pe Pv 9 Tot _------.— Pn 9 _ G Lgth - .6 MS Pt.:'/. 7-..i- Pti¢ ► ., Fit Pe Pv Q//-410 Tot itG Pf i•78' Pn p Q 4 S' G 3/J _s , Lgth 9 2 .o`#3 4 Pt 3 3. 7 3 P(3) �-T/_; C'+ce Fit / t- 1 Pe Pv Q/2.i Tot /um.S' Pf 4 Pn q 'Fit qq P Lgth / v . (I// Pt 3R. 13 Pt Pe Pv Q I3•I< Tot /45 Pf . 11 Pn q 4k.) . Q Lgth 4, • .01' !y Pt 3.g. 2. y Pt/// -7- Fit ,3'f Pe IN; QIG 9 $ Tot S Pf .2.O 1. Pn q 7 k 4Lgth Pt-yo.3 6 Pt (=") Fit Pe Pv Q 247 l Tot Pf Pn q Lgth 2v , ov -r i Pt ifu.gO Pt Ar/e • •J�4- c, .7 Got Fit 7y Pe / Y.S•/ Pv Q 2.4 1j p; ✓ Tot 1 v 3 Pf 4 3•1 Pn Zo.. 9 10 Lgth S'is' or36. <Pf Pt S 7. 67 Pt is: ` .C- ZT ef,-,/ Fit / r y Pe 1 • 7 Y Pv Q 267., f - Tot G?y, `1.3ti Pn q A Lgth Y c: r •r . `" Pt 7 u• .7C.. Pt 3 •C. Fit 9 Pe Z.j2 Pv Y" Q 2 61 Tot ' / Pf • G ' Pn Form 139 750 3y7s / v / 73 0 2.r T 3.90 3 &3 A r i"7 WASHINGTON SURVEYING & RATING BUREAU HYDRAULIC CALCULATIONS For H Sheet By Date 11 f / 1 Job No 7 Nozzle ldent. & ' Location Flow In G. P. M. Pipe Size. Pipe Fittings & Device Equiv. Pipe Length Friction Loss p.s.i./foot Pressure Summary Normal Pressure NOTES / q Lgth o0 -2_ Pt 3 /.1.4-, Pt 7- gm* 21/2. I� "rZ •9G7 Fit Pe Pv .'- r... O 7,6.s-4 Tot /v pf• o' Pn G Lgth • u., 6 s Pt 3 ' . z , Pt 7 4- i •141 Fit Pe Pv Q 1zn-../ Tot / u pf 01 Pn s: ,.. ,. Yo • 3 qFit e Lgth .0/ N Pt 3 ' . '. 'i Pt G 9.t.14' Pe Pv O 69v.I Tot /V pf .F Pn q 7S9.q .6 Lgth .02'/<. Pt 21 "' Pt S 13.e ,y• Fit Pe Pv Q 671'7.1 Tot /t) Pf 2i Pn �zyy ) q II u.G Lgth .033`1 Pt 3,.77_ Pt 4 Z'i, • 9�. S/r Fit Pe Pv Q/0.5-8•4/6 Tot 4-4 Pf /.54, Pn /a' q -71'37 G -"el Lgth /%, �: . °38 3 Pt 33;.2 Pt 3 ... -r t Fit / o .`' Pe Pv Q / / 37 .''f Tot 7 ' s.. ' Pf 4.3/ Pn q o , u ' Lgth e- • 070 3 Pt R-7, S ? Pt 1 T Fit 3 i Pe Pv Q /S 7j•4' Tot ' Pf G• & a Pn q 90 ►•y 1 Rise:., Lgth Lie . O512/ Pt 44•.27 Pt 7 o 33. S t' . { d El 7 41/ Fit 77 Pe i'"'• .S Pv Q L' 1 7Y,X A ✓ Tot I v 3 Pf 4. 33 Pn At -It t q Z o.. , u /e Lgth Se5 ,ue34.'m Pt 63. /Y Pt ¢ EC /£ 2T• Cy Fit /G 9 Pe , . 7r • Pv Q24-ij Tot 42( `-t Pf 9.3Y Pn i.1; q I Lgth '' C - 0t _.Pt . v. y ' 7't. Z 2 Pt C. Fit 18 .. -P-e 2 • S 0 —Pr— / " C Q'2..4? ' Tot 12• Pf .00J Pn q 7 s'-' . / v Lgth / e r' . az' i Pt 77. 3 o Pt .2 G / Fit 7 3 Pe Pv Q3 q 5 Tot 1 7 t Pf 3. '43 Pn q Lgth Pt ff , , i 3 Pt #° ' C LT / N ' St Pe Pv Q Tot Pf Pn q Lgth Pt Pt Fit Pe Pv 0 Tot Pf Pn q Lgth • Pt Pt Fit Pe • Pv Q Tot Pf Pn Form 139 WASHINGTON SURVEYING & RATING BUREAU HYDRAULIC CALCULATIONS For Shat By Date I (/ 1.-C/ 77 Nozzle Ident. & Location FlowPipe In G. P. M. Pipe Size Fittings & Device Equiv. Pipe Length g Friction Loss p.s.i./foot Pressure Summary Normal. Pressure NOTES �M z / q 4 _Len Lgth Pt 3'.z' pt 2 %Z K. - 9 Z. F*4 7 Fit Pe Pv . / — rL .. ,,. O 29.5 Tot /0 Pf -- Pn o ,? yo . c G Lgth ✓✓ 1 Pt 3/. 2 0 Pt.1 92 9G7 Fit Pe Pv Q26 1..5- Tot 4 Pf . el)/ Pn /ice q 7 4. C Lgth . dos. Pt 3 i . 2 ' Pt /v Fit Pe Pv A Q 31''./...( Tot 6 Pf . 03 Pn C Lgth • o Z Pt ,31. zy Pt. // trZ i' . As d N Fit Pe Pv Q 60o, S Tot / c, pf .12 Pn L.q .2 5 4 .5 C Lgth • v2 "'? Pt 3/, 3 C Pt 1 2- 7_'` k _ rr. F" Fit Pe Pv Q $S-7. V Tot / a Pf • 2? pa L,.•,, /q 2y i. { le Lgth . 036 Pt 3/. S 9 Pt 13 2 , L i, v.7 1 47 Fit Pe Pv 1 Q /69$• �" Tot /o Pf .3 4 Pn ,,r . q 7.•s2. i �. G S f / Lgth G4 0S t'/ Pt 1. 9 S Pt /' Z L /` - .�•FG� Z Te. Fit ''V Pe Pv Q /3'/f..a Tot 7t r Pf ..e .c. Pn ',et- ,� . 7,,,,-,., Lgth 2/ 3 a Pt 3S- . 7 s` Pt 16 ,-f _ gr,%t4" C z t. 7 r Fit SA' ..g •°Z' i Pe Pv Q 1'0/, Y Ayr _Tot 32X.8 Pf S5.i 5 Pn Lgth Pt 4- 1.2 o Pt 2 Fic Pe Pv Q �_ ,. Tot Pf Pn G N v � .4- q, t, ci Lgth Pt Pt Fit Pe Pv Q ...---•'''; Tot Pf Pn q Co Lgth / 7 s ,6a6e.G Pt 35 -/.5 Pt 16 2 T Fit 7 oPe Pv Q 1-40 Tot 2Yf Pf /.6 Pn q Lgth Pt 37, S2 Pt / Fit Pe Pv Q Tot Pf Pn 9 Lgth Pt Pt Fit Pe Pv Q Tot Pf Pn q Lgth Pt Pt Fit Pe Pv Q Tot Pf Pn Form 139 ° ^T".e—�nr4 =rr^V• A 13 « .L.,�.r. Cris . I WtX ';'t' URIC W l L . 1'i( 4...71 -.-„NA‘ W v.% J /•v Pow, s 1,001, ak " a d rJ , AS NQTED The drawings affixed hereto have been; reviewed and accepted as meeting or exceeding minimum requirements of the City of Tukwila Fire Dept, Bureau of Fire, Prevention. Additions or revisions to these drawings after this date shall not be construed as being approved or r� j :we SEP 2 1977 CITY OF TU K BUREAU OF FIRE P T ENTION FIRE DEPARTMENT TO BE CONTACTED TO WITNESS THE FOLLOWING TESTS: t 1. Underground Visual Inspection 2. Undergrcond Hydrostatic 3. Underground Flushing 4. Overhead Hyrdrostatic 5, Dry Valve Trip Test 575-4404 °39 C 1•��A .'sa AA, APPROVED A 3 BY A/QT-0 WASHINGTON SURVEYING & RATING BUREAU SEATTLE. WASH. SEP 1 51977 As meeting requirements of this Bureau for classification as sprinklered, however, system changes or additions es recommended on the attached sheet(s) will result in improved rates. Acceptance applies to plans as submitted and for construction and occupancy shown thereon. Finished installation subject to inspection for final acceptance. All comments, approvals and acceptances relate exclusively to reiativs effect of various conditions upon tire insurance rates They are not to be construe° as beefing in any way upon the question of whether "due care" has been exercised with respect to possible liability for personal injury or damage to property. It is recognized that hazards which mat result in loss still exist. /n , �CY/C(/✓ 0, 0' ' f/eAFD .,1—'£ /UN } NO DATE . BY REVISIONS PROTECTOSPRAY NOZ MULSIFYRE PROJECTORS SPECIAL PURPOSE SPINKLERS/NOZZLES ACTUATING DEVICES SPRINKLERS SYSTEM CONTRACT NAME TEMP ANG G ORIFICE OUANT SYMBOL OUANT SYMBOL ORIFICE QUANT SYMBOL OUANT SYMBOL OUANT IMPORTANT fN LOCALITIES SUBJECT TO FREEZING CONDITIONS: ITk IS THE OWNER S RESPONSIBILITY +TO PROVIDE HEAT THROUGHOUT' WET "PIPE SPRINKLER SYSTEM AREAS AND IN,ENCLOSURES FOR DRY PIPE." DELUGE AND OTHER TYPES OF VALVES CONTROLLING WATER SUPPLIES TO SPRINKLER SYSTEMS -' ,n t 4 *r WET.. I i DRY 11 DELUGE PREACTION $ELFCON FOAM PRIMAC . fl CHECKED 8Y, FILE NO TOTAL: TOTAL TOTAL TOTAL EXECUTIVE OFFICES PROviOENc R • Date r 7t4>Y sY is r� x t s i I_ rt ^T".e—�nr4 =rr^V• A 13 « .L.,�.r. Cris . I WtX ';'t' URIC W l L . 1'i( 4...71 -.-„NA‘ W v.% J /•v Pow, s 1,001, ak " a d rJ , AS NQTED The drawings affixed hereto have been; reviewed and accepted as meeting or exceeding minimum requirements of the City of Tukwila Fire Dept, Bureau of Fire, Prevention. Additions or revisions to these drawings after this date shall not be construed as being approved or r� j :we SEP 2 1977 CITY OF TU K BUREAU OF FIRE P T ENTION FIRE DEPARTMENT TO BE CONTACTED TO WITNESS THE FOLLOWING TESTS: t 1. Underground Visual Inspection 2. Undergrcond Hydrostatic 3. Underground Flushing 4. Overhead Hyrdrostatic 5, Dry Valve Trip Test 575-4404 °39 C 1•��A .'sa AA, APPROVED A 3 BY A/QT-0 WASHINGTON SURVEYING & RATING BUREAU SEATTLE. WASH. SEP 1 51977 As meeting requirements of this Bureau for classification as sprinklered, however, system changes or additions es recommended on the attached sheet(s) will result in improved rates. Acceptance applies to plans as submitted and for construction and occupancy shown thereon. Finished installation subject to inspection for final acceptance. All comments, approvals and acceptances relate exclusively to reiativs effect of various conditions upon tire insurance rates They are not to be construe° as beefing in any way upon the question of whether "due care" has been exercised with respect to possible liability for personal injury or damage to property. It is recognized that hazards which mat result in loss still exist. /n , �CY/C(/✓ 0, 0' ' f/eAFD .,1—'£ /UN } NO DATE . BY REVISIONS PROTECTOSPRAY NOZ MULSIFYRE PROJECTORS SPECIAL PURPOSE SPINKLERS/NOZZLES ACTUATING DEVICES SPRINKLERS SYSTEM CONTRACT NAME TEMP ANG G ORIFICE OUANT SYMBOL OUANT SYMBOL ORIFICE QUANT SYMBOL OUANT SYMBOL OUANT IMPORTANT fN LOCALITIES SUBJECT TO FREEZING CONDITIONS: ITk IS THE OWNER S RESPONSIBILITY +TO PROVIDE HEAT THROUGHOUT' WET "PIPE SPRINKLER SYSTEM AREAS AND IN,ENCLOSURES FOR DRY PIPE." DELUGE AND OTHER TYPES OF VALVES CONTROLLING WATER SUPPLIES TO SPRINKLER SYSTEMS -' ,n t 4 *r WET.. I i DRY 11 DELUGE PREACTION $ELFCON FOAM PRIMAC . fl CHECKED 8Y, FILE NO TOTAL: TOTAL TOTAL TOTAL EXECUTIVE OFFICES PROviOENc R • Date r 7t4>Y sY is r� v 014 10, „11,414 , 4.4 , 4:6 mrt ,, • pp • • • - 7 e • p 6 6 P -e!!' 4: 'e• 64, , 6,4A •••! P . - • . • , P 661: • ; , ,h rn 0,0 •.• 1 1 14,10 .r 411 0, .1, ,•01 • l• g 16 4 r r 4 ".", , "4 0 P , 4 h,„ r 444 ,1 • „, , 1!„ •„;.•••,, • • •.! , • , „ , 7••• ''„ „„, „," 140 • 4. ir '411404) , •,,,, 'I • ' „. e.,;• 6, !.•!' 0 1;>1P.. v)0.5,E. 01 ''",' ' " • 0 Ar 6 1\1‘,0-. OZ 00;,,C.114[1, • , th1 „h „ 8 enk, sNE.Lte NUT , • PIPE. ToL.ET tkE „ 1-ki)$F-• ..JL c$ F \AUBE F. P 1NL (N0 • 01 T • • thAP Avkltrre* xrer. .1r. n 0- 0- 0- 144111141.1 4. / , I " " " 44* 4 /1 r 44 "46 4 4 , ''• • 4 , , , ti/14: ELL' LET Akk_ ELTC• C.46 "W„Sol- Nc tP,,P•IVA „ . • 4,1 V • AL121\k Vit E. "*4/ ST Kt.it,K.S2t4 1N.L. 'WA T E.,;Z P6oToS LONG. 2': tTMN 11 1. srn 1 I ' P 110111111111„.. .4* e6„,, 44 • P 4 „ 4 „„ • ' 1,00.60.4 _ 04- 01 S4 W./. 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' , r I „ 4 ' / „ , „ , t , 6 , , • 6 6 , 1 , ' - 0 I, e " 4,1 • , • , ' ,••, ' 4,66 " 44 14 h • ' I , 1'4 4 ' ,• . • „ 6 r , • A, I ' h o P 0 t, " hh ho 4,/ gll 444, kl• 4 1" , • „„ ,,,,, , „„, , , „ , ,, 14 :„ 4:14' '7 , •6p S\ ' ' h'Ih• , 1,1,..h, ' ' „„ "..... . .000.• , 1, „r 1 ,, 1, " , 4, , . „, „ , , 4 ,1, '1.14 ' '' 1 ''" r 4 , ,' ' , , , '„, 46' : i ' ' ee: ..1 ' e ', 'q .I: 40 : I'' „ 6 ' '9'. „ ' 44, 4° ' ' 0 i ' 4 4 A ' '..A'' , „ p" ' , . • , , , P 1 ' 'no hA 14 1 r"T‘ ' , ''',' ' ' A • ' ,„/ 4 p '' 0 " '4, ' "P• p I ie', • ' ....-w.,..'....:6,--.-6,---1/-4.--- -....6, '....,, ' . -L., 'I . , • 4 , ( g I „ '110 h 0 • 1.1-1 IMPORTANT IN LOCALITIES SUBJECT TO FREEZING CONDITIONS IT IS THE OWNER'S RESPONSIBILITY TO , PROVIDE HEAT THROUGHOUT WET PIPE SPRINKLER SYSTEM AREAS AND IN ENCLOSURES FOR DRY PIPE, DELUGE AND OTHER TYPES OF VALVES CONTROLLING WATER SUPPLIES TO SPRINKLER SYSTEMS 4 9 NO 4r 4 15; „ 4 1. , ,„. 0 -- re - n- 0 -- - 61 • APPROVED AS NOTED The drawings affixed hereto have been reviewed and accepted as or or exceeding minimumrequirements of the City of Tukwila Fire Dept., Bureau of Fire Preventon. Additions or revisions to these drawings after this date shall no be 11es. or approved o 1. - ... OF TU .... --7;;;EAVOI F FIRE EVENTION • •, 6-.67/6, •••••••4441•••'..)64-17.6„-64/”...re44;•/09'4#40,,,;',„4*-7,3,4p, 4,„„ ,.„14•Ip',4,•44 " 1 FIRE DEPARTMENT 'TO OE -CONTACTED " TO- WITNESS THE FOLLOWING TESTS: k 4.4.4enterri-kIttrAmitrtretti 4•41•44444a411.41014sttt 41-4iat4.3g1I!14aka4ig 4. Overhead Hyrdrestatic TUKWILA FIRE1EPARTMEtit-7 0- 0- 0 DATE BY 575-4404 0, rr r '1I 4 44. ••••••••••••••06.011.100.14.11.1.6•4161,11114.111.1....1,141**14... 000 " :e•-•.•• " ° ""'" " : '" " 4 " .11,44 " 4.4"•$e.e.,-- " ' 444 „ L 30 ; 4/4 P.. ' P.P.," 40 " ..4 „p• 14 hter , ,,,h ,;/ " P ''' 1,„ ". ' ' ' , '0' ' ''" . 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P'q\'`,;..t.lt..t$'" " e.;'. ,fl‘.•1"114,(e.),„' 1 FV,k,t4ets. 1 , • 4.c. ‘0,t•••4 r.... 11.. ' , 4.9 • 041 04z 4.‘'"4-1‘z. 1-)". 17# 9 to 2. n-,!, 4111V... To t. PlIfL4 9 0 10 0" ot 0- 4 ?A1:?, 4 >. • 44,14, I 6661- / 441 12 s;• t440 '..„E.C.TVII•61 4-z .p S -4z. 8- Wt. #• -Q1 \%."; 9- io`z ••••••141,1•••••••••0141.... .40 o 66 6, ph th' . 44. " r1 4.4 ' rrr.„,.604' ",„et, ' L - "•••-•"- CC) ' 11 Col' Boa .00.0111 , ea_ I 44 • 1N1,1(.„F_R tN1C5U-L., or PROTECTOSPRAY NOZ. MULSIFYRE PROJECTORS SPECIAL PURPOSE SPINKLERS/NOZZLES -o 14,4*,110.01.4 , 7.-1 0-4 kt. 16iS 0 • 441 ro 6-1,r) -61i. -o I 2_ 9-1727-C)44 t\\1_ t.v.Nw.„ \\ \„, , \N CV\,6 F ; • „, ,•' 4 'A..1..0- !!' ! " 4,4 .1.41144.1.4.00.04.0.0•00000.00.0/0„ 2‘, tee,D " r ....0.16,400104 ,00 44.440,404944.9444,444,49.4490 41 ' I ' Ny' 1 s' 5 \.. ! ---(i"4•7") -,roL-- I . so -1'2. T N, to 4,4 45.11-11 4.51Z-1! ACTUATING DEVICES r'S*4.14.4 txD , , Alp / Or EL J'3 41) ,4 4,•• ••,• --•`- ---,Pi-- 0-'----.40 • loz. • 1)-4 ?.!.•C% °41 -2'1 p, ') ;2o •••,„„)i - J 4 .19 " • 7 it, I 1 IC CIT -'44L. 114 61_44 r. ir t--- ! gi ,, _..., :; TO 4 P1FF_ 1'9"' i 1.4 ? .,, • ".. -Pe 4°- N. 4. 'LJ •-•P -4 • ' I 1- 9 4240b ' -;0-0 rk,-- 0 ' ,,,,, ..„,..„7.........2. , ,. ., ,.., .,..;;,) .4,1 .4c..... ..... 1).......L- i.....Lbk. - (N.1....2.:, • , , ''› %,, C91.4 I 10Z Tr) ry ' 1x - 1 icf\P t,3-1*-9--S;e74 .4" 4 6.11,4011.11,441•11.• 666' SPRINKLERS • , I- 82, • • 4 - 4s 444.4 4.44 .....49.44449 P.. 44. 44.44414.001141, 4.10.0.: 6 44„, .4,44 .44.94.4,444.44044,494. „4 SYSTEM TYPE TEMP DEFL ANG ORIFICE (WANT, • TYPE SYMBOL OUANT TYPE SYMBOL TEMP, ORIFICE OUANT, TYPE SYMBOL TEMP STYLE OUANT. - TYPE .1 ' SYMBOL tuRA ss u-3 3Z. 0 .I•et,, • ?...R AIL TFig,M 16 1732 nni ,pFlt, (6) OUANT 315 ! 12 11 10- c._-trLANv;=,- F\•/)., TtIRtiNQ KN') R1N4 2 , 16 TOTAL „' TOTAL TOTAL TOTAL •• • , ,1 I 1 1 1. 1, ,41 6 ir „ TOTAL 32 7 WET„. ---4.-111111 DRY DELUGE- . fl PREACTION__E) SELFCON n FOAM ' „.43 PRP MAC .*** , ••••. • 10 • 7_1?,.. •-• . --b1 .-,1,----' 0-- 'td; '17*:- r .....4 .........* 4 " 4 444440 '. *4 .44.4 .0.444, ,'IA tr0?"7 C" 1C. h tirl../...e, . v).1, o• " 4. 1_41 \t,41,1.1▪ 1ovV /IL 0•00.06.00*••• tF0 444 01.0600.04 .0•140.•410, .100.40,0.0 Ea_ ,4•4• • "117iirl" 4", - Pr1";',...:441"4,44;44„,,,,...449,4444.4"1C•44,;.:44,9 44,.....44.4•11.14.1114414.- 11 4. 15/3 -I 44,144 4.4.4.44 FIRE PROECTION SYSTEMS EXECUTIVE OFFICES PROVIDENC, R 10 40,4 444.14 • !tNETNL_GRA41,1, ri4 These Plans Prepared At RE NTON Date Engineering Dept. r{. • 4 • bLLt 40.444,h1 1" 4.4„i•-p_c„.Tho9',..e TV7 0, flJ 1.4°4 41, op' • 10 1,6 „ 44; "At ;. el*,,,1Tfe 1", • , • 'fi-r• • " „," „I„ 44449 , 4 44 4-49,44, 44. 4444, 419 4 ...NA, 9 \ 4. 144.1444,4'. -4 41 • N 411, h • 4, 14'; '! 41 '1• ;" 4. , • 1, „, LATEST REV. CONTRACT NAME' f;••,‘E.4-(%••A,L S..."T 77 1 TUKVv1‘.. j CONTRACT WITH: '51NN4'If.1()N1 C,N7• 2 08 II 7, Kle.„ • U:.11-.E.Nt„ SCALE' sigVil A t). 0 c)i ,e1/4.44 cv By, GlIrtlittC194 VelICCILECT NO; 44,r Ft c•--aYniriiM. 7 4 VKA 14h VE 11 j PILE NO: DRAWING NO 2 o F ' CONTRACT NO.; " 112 Si -co C• 12 414 4 V4 1' 4 , .4. 4 r 3 , 4- .a zr F 4} 1/-1,#,... — /--44,- - s d 3 44 A w h s • 4 • t} t• • 3 s^sr 4 41 r. 4 ti t 4 4 A The dra cc Nmigs affixed Itcret® haw been reviewed and accepted as meeting or exceeding minimum requurmeats of the City of Tukwila Fie Dept , Bureau of Fire Prevention Addit,ans or revis.3ns to these drawings after this date shall not be construed as being approved or �, iev�e OCT 2 6 1977 CITY OF TU r A BUREAU OF FIRE ' VENTION h• -4 4x 4, 4 4 1' 77 4 k 4, x • -9 44 4' -4141 t ! 81 ti • • 4 44 } d# • • r 44 5. A .4r '4- r 4. 4) r P .5 A t4 4 4 * ar 'f I 141 It? l t 3 ! at 4, r °1 r s Y d4 x77«7 { y+Ynvyn,+�Mry.+7v.�+�41 34'414 ..#4,#.4.4,40,424•41.41•14 FIRE DEPARTMENT TO BE CONTACTED TO WITS ESS THE FOLLOWING TESTS: Ii� fll�frl� 4 Cmc:,1 qr '} 'hail$ EMM IL FIRE DEPAgTMUIT) 5 75-4404 —' f 11 • 0' Vt4 a 4 1.) t l—Cr. "34141 V ( - r AAtt ✓N'r�i�» b• v.) Q LL A 5 p 4 1 It r(.,ae.,v...)) r“ VJ< 1 • - V74.1.„34 - 11k!'ECr . g.4, -t IM PORTANT IN LOCALITIES SUBJECT TO FREEZING CONDITIONS IT IS TI4E OWNER S RESPONSISiLiTY ,TO PROVIDE HEAT THROUGHOUT WET PIPE SPRINKLER SYSTEM AREAS AND IN ENCLOSURES FOR DAY PIPE,' DELUGE AND OTHER TYPES OP VALVES CONTRoLLiNG WATER SUPPUES TO SPRINKLER SYSTEMS EY t�►�a4n1 J r 1 ¶ t LIS 1t M TL • 'f } • 4 44 4' 4 4 T 4 7, -- .. „p. 4 .>w • ,81 41 , T a"+"til - P'" �" e..' ..'1'41 PS i 4""0Y 44 47, 7' - n.P 1 • R +m w 7j 41 12• Pe • • Mieir • tlek 0 40 rsicEE.TE,„ • rrt IA vrr 1,71 • • 14, • • 4.1 A 14 If • • 114 444 le 7 •,9 PI 8. et -it -7 4.4 I -tk' "7 • itqer 4-- np, 3 41 rr • 73, • 2. 44. 34, 4 1.4 44, nimmiamonEvISIONS NO DATE gnu • MINIBIEMESSESICERIMEI 11111111111111111111110111111111111111111111111111111 1 24 • • 11 4444. TYPE AFGL ORIFICE • 1111111.111111111111111111111111 OUANT TYP .11 RED co 4.4.11 11 4.74 Ift#4 424, 4 144 TxP ___0_1‘7 I a • fix- 0 1 1— • \\1 • gra 7 -3;41 4034, zrite 11'7- -33 ti 2, let /14 tm 44 S" -A130 kto,Co4r 0 r 454 rYP 0 tkr- 445 '5- inseeinvor • 41, err 44/ • • 44, • 41,0 It 10 "1-4 ir 1110 1/4 0 • 0 to 331 isr UM 14 42-1 .4 0 464 • .41 MULSIFYRE PROJECTORS TYPE SYMBOL OUANT SPECIAL PURPOSE SPINKL ERS/NOZZL ES • SYMBOL ORIFICE OUANT • 1 • • • • • • 114 'FRNsi.\14L. 4 SPRINKI_E5k P Pk_k1.1 ACTUATING DEVICES s TYPE SYMBOL 111111111111111111111111111.11111111111111111111111111 OUAN 1111111111111111.111 1011.111111111111 TOTAL r N1111111.11111111111111111111.1.11 1111.1 111111111 TOTAL /- TOTAL TOTAL SPRINKLERS OUANT CARA 41141-1„ 0111111111111111111111111111 11111111111111111111111111111111111111111111 11.118111.1111 MOM .1111111111111111111111 11111111111 animminmommaing TOTAL ••r SYSTEM • • tl 12 • 4 4. • r 0 • • • ▪ 61 N. • • 44. • • • • • • • • 44. • • 3,4 0 • .44 Di r_7-4.44, ▪ 4 14, , , 1 POP P rlp v ep WASHINGTON SURVEYING & RATING BUREAU SEATTLE WASH As mee ng requirements of this Bureau for classification is sprinklered, , however, system changes or additions as recommended on, the attached sheet(s)4.will result in improved rates Acceptance appltet to plans as submitt d and for construction and occupancy shown thereon Finished Install^ 9n subject to inspection for final acceptance • comments approvets and acceptances relatetescluslvely le relettva 's affect various conchbons Upon fire insurance rates They are not to be con riteei as bespng in any way upon the quastron of whether due care h s bAen exercised with respect to possible habdity for personal &.,_.„. cg'L-.,,,t— \_ILI \''''': result in loss WI exist • DRY DELUGE 11 PREACTION —0 SELFCON FOAM pRimAC ri 4474 FIRE PROTECTION SYSTEMS EXECUTIVE OfFIC.ES 10 These Plans Prepared At Engineering Dept Date CONTRACT NAM E TLIKW tr. N. vi,kstrl, CONTRACT WITH 100 11Z tsl 09.071 • 5, • PUR 0 NO PPIOJECT FILE NO DRAWING RO CONTRACT NO • r A k 10 A APPROVED AS NOTED The drawings affixed hereto have been reviewed and accepted as meeting or exceedin3 mi 11 I m u m requirements of the City of Tukwila Fire Dept., Bureau of Fire P1 evecition. Additions or revisions to these drawings after this date shall not be construed as being approved or view _DELI ?9Z7 ... ' CITY OF TU ILA BUREAU OF FIRE PREVENTION FIRE DEPARTMENT TO BE CONTACTED TO WITNESS THE FOUIE R TESTS: 1. Dnlergrsnnl final Inspection 2. Undergnnnd Hydrestatic 3. Underground Fleshing 4. Overhead Nyrlrostatic TUKWILA FIRE DEPARTMENT 575.4404 • EV STt4L. MA[til W\1"4 A L. RV. ALIT LET EtEY z Z5-5 8" E) NV LCL. i LC--O'ZczMA1t.1 --- 5 /2-11 RLN 11NE:s 1 1L�3r(a 7 it B -[)-11' B1 lndv 1`E4.1c, NANJ& w gz / 11" HAra�,Eir I - 2z(c) STU11 v1ALL tic").11-1t 11Nt.1L. 2-3 12)111.. 671\ F t>=/"F ver / Stt;E, SEAM NGS. • EIZV BULK - 12-1 SUN N,AkNS Z to Q,1'_1nwr CECT itU+l 1�F Iry ii111,4E`� $ �I1 C ,9 4 ©'K EF)JW DELK - 14 Lekf. ' 1)K -IT -'7.a ARE. l� -t7 TYP U13Lt.^_E NOTE AtK<,lA(►,� Na`t4e-d fsu�rc 2 Y Z % LA& FL UTEL -co -TOP ' t►.EN:$E.E int 3 .Tot VT5 , H1.N4. FfN& L wtT}I L-6.1_AN.1' 3c3 t2oG 4 i�1NG r 14A14 cBtiA KI d-vcT R. 11F_FiELT1_G 1/8.`_ ...i ,FT. ArrlOV ii) A BY /'v o -rte WASHINGTON SURVEYING & RATING BUREAU SEATTLE. WASH. DEC 61977 As meeting requirements of this Bureau for classification as sprinkiered, however, system changes or additions as recommended on the attached sheet(s) will result in Improved rates Acceptance applies to plans as isubmitted nstallatiionand for construction and subject to Inspection for final paccept acceptance thereon Finished 2Z� } es�7S 1w All comnwnts approv, acreo,ances rein E.,cluslvely to relative effect 01 vinous couci1 o,' uoon ore rtisurance races They are not to be construeo as bearing in any way upon the qurstlon of whether "due care" has beer exercised with respect to possible liability for personal Intury or damage to property It is recognized that hazards which may result in loss still exist NO DATE , REVISIONS PROTECTOSPRAY NOZ --Q— -X- TYPE TEMP ORIFICE SPECIAL PURPOSE SPINKLERS/NOZZLES QUANT SYMBOL SYMBOL TEMP ORIFICE ACTUATING DEVICE SPRINKLERS SYSTEM ITV til 'itEttIPA, fit►, Ati i 110 Eafx f 444tPis 1111EilitiVkE.b r i v,,sts.44ti };22!'1,1,. 1 avv.tttols AIM ti s li,'=.�' IattNEt2 Nt 3 1. '4S'1,24EV. SCALE QUANT SYMBOL TEMP STYLE QUANT SYMBOL IM PORTAE T IN LOCALITIES SUBJECT TO FREEZING CONDITIONS IT IS THE OWNER S RESPONSIBILITY TO PROVIDE HEAT THROUGHOUT WET PIPE SPRINKLER SYSTEM AREAS- AND IN ENCLOSURES FOR DRY PIPE DELUGE AND OTHER TYPES OF VALVES CONTROLLING WATER SUPPLIES TO SPRINKLER SYSTEMS DRAWN 8Y CHECKED BY PUR ORD AM PROJECT NO I TLE NO . TOTAL TOTAL TOTAL v. Date ,il-21-7> y. 1 5 AS5 CITE /fie' draw' , 1 d r re o svq 4aak1 reviewed brtd acc p s.d mgtZtll14 G tx 13dl - r4111urium a qa gmnt1 at Lha Cali a u' -s to Fi e C ' ` arOAu at FirQ VimiorlV 1 Add t►s s ©r re4I3 J t3 is tii33t tItaViInv ratter VII dst h 11 /WA tiI I as 12e,s ,., ,..w i, dr DEC 21977 only op. -mw Wigai941.11 CF FIRE DEPARTMENT TO BE CONTACTED TO Y'ITHESS THE FOLLOIDIG TESTS 1 t 4J cod Visual I,sp ctoen 2 i. i 9J 1-2 r1s12 4 C ad c ' 1k1 Ta Trig T t FIRE DEPARTMENT � F 575 4404 x 16 a. v 4 1 it V f 1 �r ^s,. 4`' c REN \blot £ WALL 4 FIN/. U\ W ELL t Fr* T 10 } LATEST REV PROTEGTOSPRAY NOZ SPECIAL PURPOSE SPINKLEASINOZZLES ACTUATING DEVICES SYMBOL .,SYMBOL TEM QUANT IMPORTANT d 1N I bCALITIES St)8JEGT TO PREEZ NI C Nt TIONS IT IS THE OWNER PES ( NSSL►TY TO pflOVCDE EA TFiRdUtSliQt$t !ET PIPE SPR NKLE1 SYSTEM AREAS AND IN ENCLOSURE 17R t?RY PIPE DELUGE AND OTtIEl Y ES OF VALVES CONTROLLING WATEI SUPP tES TO SPR AMER SYSTEM$ I kr CONTRACT NAME, GRINNELL FP ECA 1E w.tsrvE PfNG RENTON 4 p441 TEC,T 711 ' y CT W1TH SEAN ►Sc"r E ,^ 114T$A. PUR. ORD NO- TOTAL ONTRACT 3154.943 AI 0- tttt � t yam 9 Yr 44. -t rf 171 > 1 /2-G "748i•-4. • /37 -To it 0 41. 1+ 50 O' r O 35o-0- 300 0- C A CALL ;-/' (53 Zoo 0 r t - S9 0" 7".m tic, REO[//Rto PVORAVAI4 0.4A•A4 £LEcrR/t Jw/rCW KA0K I i A - --`- �5PR//YA-L,f R f'KjErq .1 t_ J t C—? G i'G = 23 0 I j 36 1 101 /44 " 1r ©FF/C4.b- Q 4 0 i C1 Ti c4 v 44 2 i 'Al.0 R 0A ACC4-5i 4 90 -1 /23 5" Wa!' 7£t�1 1 /10' It" 55' 7" A 1 S a • 1 s I L o 301t0 �9' 07._ 36t_a` ( watt 9 34 -9.. ; 35o`-0 • �-�1� /2 o -r -- 22 ✓ r 1 :9-7t 1 I4 s' I 3/3Y" -y"- I Z$4" /0". ZOe,' :4 - 34'o o 3 2/ -B 303 =q' 2 76 `/o 2St 10 0 ►"— -111 • �100� .a /0`Q 1 i 9 roar 1- ! 9 0 /d/ Or Z-542:40.- 2 23f- c9' ?C1'- ZJZ =0 2/3- — /78 8 4/6' s/ --- Q s, /0 0' — ZO/ - Z" 44 /0-a /0 0 otId" /SG"is4" 11 0 0 t 9-0 /Z/=0" 1 9-0 1 6/=0" -� /33`/D' _ //5 1..s (5 8 1 Z" t 1 53-3 10e 0" .4 r /0 -0 /O" 0' s sot -4 --- L37-o- 1" - Z7' Q 1jI l 1 t �� DOCK ZZYLLiR ms's G o" wide s- 7 "' 1 11 j ,,9'o_ / -O 22=i41 s�i J ,IY01. 71.-,AZAALJL r TO 500711 .1/17,6 A /..11.Z Tos7#c/CIAr.L'I , CLEAR A/JtE W/12 -d1 SHEET IDENTIFICATION �S 70RAGE. PI.A/\ DATE REVISED APPROVED DRAWN BY CHECKED BY PROJECT IDENTIFICATION C7ULF' ATLANrJr. rA Agf.A A.,. Tu X Iv f A WAS h . DATE DRAWN /2 G- 77 /0/srA'f,Sv,-/21., J,ERY #4 GULF ATLANTIC W-AfEFIOU-SC CO ENGINEERING DEPARTMENT HOUSTON TEXAS FILE NO JOB NO SHEET NO ,5"/ 0 - 1/ 5ECAj5 RECEWED 7,7 BY DEC 8 5977 Tl� lC1 FRE PREVETfl PO's BIWWJ 1 -£. .._.•••••..-- - — 5 4 0 i C1 Ti c4 v 44 2 i 'Al.0 R 0A ACC4-5i 4 90 -1 /23 5" Wa!' 7£t�1 1 /10' It" 55' 7" A 1 S a • 1 s I L o 301t0 �9' 07._ 36t_a` ( watt 9 34 -9.. ; 35o`-0 • �-�1� /2 o -r -- 22 ✓ r 1 :9-7t 1 I4 s' I 3/3Y" -y"- I Z$4" /0". ZOe,' :4 - 34'o o 3 2/ -B 303 =q' 2 76 `/o 2St 10 0 ►"— -111 • �100� .a /0`Q 1 i 9 roar 1- ! 9 0 /d/ Or Z-542:40.- 2 23f- c9' ?C1'- ZJZ =0 2/3- — /78 8 4/6' s/ --- Q s, /0 0' — ZO/ - Z" 44 /0-a /0 0 otId" /SG"is4" 11 0 0 t 9-0 /Z/=0" 1 9-0 1 6/=0" -� /33`/D' _ //5 1..s (5 8 1 Z" t 1 53-3 10e 0" .4 r /0 -0 /O" 0' s sot -4 --- L37-o- 1" - Z7' Q 1jI l 1 t �� DOCK ZZYLLiR ms's G o" wide s- 7 "' 1 11 j ,,9'o_ / -O 22=i41 s�i J ,IY01. 71.-,AZAALJL r TO 500711 .1/17,6 A /..11.Z Tos7#c/CIAr.L'I , CLEAR A/JtE W/12 -d1 SHEET IDENTIFICATION �S 70RAGE. PI.A/\ DATE REVISED APPROVED DRAWN BY CHECKED BY PROJECT IDENTIFICATION C7ULF' ATLANrJr. rA Agf.A A.,. Tu X Iv f A WAS h . DATE DRAWN /2 G- 77 /0/srA'f,Sv,-/21., J,ERY #4 GULF ATLANTIC W-AfEFIOU-SC CO ENGINEERING DEPARTMENT HOUSTON TEXAS FILE NO JOB NO SHEET NO ,5"/ 0 - 1/ 5ECAj5 RECEWED 7,7 BY DEC 8 5977 Tl� lC1 FRE PREVETfl PO's BIWWJ 1 „4414 444 f ..gym ». r v,z' r 4 p'4 t`V '1414' r' l "rse^,,w.” rata�-a ammo 4,, V44 r r / a+ ,ir 4.4., Y 44'4.44,'4+ `. 'v 000 s N-31/4117-1 4.4%, 4 l ' T - IM1�CIJ 7.4" sf'" 010**01, 0.0000000 —>, �...:. FAN 41.1 11 414 AS NOTED The drawings affixed hereto have been reviewed and accepted as meeting or exceeding minimum requirements of the City of Tukwila Fire Dept., Bureau of Fire Prevention. Additions or revisions to these drawings after this date shall not be construed as being approved o vie d. SEP 21 1977, CITY OF TU -+ILA BUREAU OF FIRE PREVENTION '< FIRE DEPARTMENT TO BE CONTACTED TO WITNESS THE FOLLOWING TESTS: 1. Under:raand Visual Inspection 2. U hrgrauad Hydrostatic 3. Ilm;c'grci id Flushing 4. Cii:Ite3d f;yrdrostatic 5. Cry Valve Trip Test TUK ILA•FIRE DEPARTMENT Et�T, 575-4404 4 k t t 2. r 3. Pgib"F //f/ OvfSiI'- ,l bQve Pr -Oa 1 Co.n/or) e., L$ 'Red r—Pv i cl e ,on, Copy d f *his s fWa'-S h +0 T.-�(-N,� l k 12,, 124 - Wo/ -/15 /rs !/ e 9. Y-0 r /90"°147I H ielr4 'i per- o,?.0, Provid.e. e.L - (veer ,cer:ti+yvir: ky,rre. 4,4J Q« ..,*, r+r.,..« y. "4 K. + ,,.+ a .uY b4. /- y.17 4,4 *.4--f APPROVED • WASHINGTON AS & RATING BUREAU SEATTLE. WASH. SEP 1 51977 As meeting requirements of this Bureau for classification as spnnklered; however, sYstem changes or additions as recommended on the attached sheet(s) will result In improved rates Acceptance applies to plans as submitted and for construction and occupancy shown thereon. Finished Inotetlat,en subject to Inspection for final acceptance. R11 comments, approvals and acceptances relate exclusively to relative effect of various conditions uocn fire insurance rates They are not to be construed as barring in any way upon the ouastron of whether "due care" has been exercised with respect to possible liability for personal Injury or damage to property It is recognized that hazards which mag Insult in loss still exist. .S0 2 FS vCAr/o C- 7‘44/ O� tT o �c 4V/ Etre' c? / DATE . REVISIONS MULSIFYRE PROJECTORS 4 TYPE TEMP OUANT SYMBOL SPECIAL PURPOSE SPINKLERS/NOZZLES ACTUATING DEVICES SPRINKLERS SYSTEM ORIFICE OUANT SYMBOL TEMP OUANT SYMBOL OUANT IN LOCALITIES SUBJECT TO FREEZING CONDITIONS IT, 'IS' .THE OWNER'S RESPONSIBILITY a, TO PROVIDE HEAT THROUGHOUT WET., PIPE SPRINKLER SYSTEM .AREAS AND' IN ENCLOSURES FOR DRY PIPE DELUGE AND OTHER . TYPES OF VALVES CONTROLLING WATER SUPPLIES TO SPRINKLER SYSTEMS , WET f-7 DRY fl DELUGE - 11 PREACTION SELFCON FOAM _ i •1 PRIMAC...._._ 1 ' These Plans Prepared At Engineering Dept LATEST REV. SCALE CHECKED SY: PUR ORD NO; PROJECT NO r TOTAL" ' a TOTAL TOTAL Date r