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23B-046 (189) COOLE''i DICKINSON HOSPITAL, 3RD FLOOR, NED - _URG UNIT j jars lil�! i ��� f �► it � ! ! � I 1 1 i i i i i f l i l l i ? 1 ! —i •_ _ _ � fi iii 1 ! i 1 1 � i ? 1 ! 1 ! ��''► 1 1lt11I�1 11 I ! ! lIII ifi � l � 11111 ! ! 1 ! � 1 1 11 � 1 1 1 j7 ! � 1Lil-_-- i 'i i i 1 i i_ 1 1! 1 1 3 1 i ?MI t 111 11 , I 11 1 1 1 1 1 1 1 1 1 j i 1 I 11 1 i s _00 i 1 1 ► � 1 t ( 1 1 1 t I ! E � i 1 . i � _._ 1 i �'• iI i! l li ! 11 1 I i I ! ? ! t l i ! 1 1 f i f 1 t l ! i 1 j 1 1 1 1 1 i l l l l i i 1 1 -___ 111115 � 11!i11i(i(�Iflitllfi � ! i � � 1 ! iI ! 1ii ! ! t ! ► ! } t 1 f i ► ! (( � i ?_ t ! ? f ! _t I I ? � E► r ' �i ! ) ii ! ► ? ? ! ► 1 ( ? I I I I t 1 ! ! ? � ! i I I i ? 1 ! � i I ,' 1{ j ►► ; � _ i i 1 � � i ii � ' 11 ! 1111 • 11111 I1 i � I r'yl Pi li ► ! 1 Tiff 1 11 R1 ii 811 !II f 1 11111 i ! I ! ! i 1 i ► ! i t 1 l ► i t 1 11 •'!r! 1111?�II!lil !' ll IIi � ' lli ! ! II 11111 111 1 ? I ! i l l ? ! ! I i ? t l I i I 1 1 1 1 ! t 1111 i i 1 1 II11ii;I 1 il ! i 11 1 1 I ! 1lI11li I ! i ! ! i I i ! 11 11 ? i l t l l i i 1 1�: , 11!11 �E i i i i j 1 ! I i � � i i � k 1 's I ? ! I i i ! i � ► � � it I1 , � � ► 11 E � � ! 1 � � I ! i 112 . i 6 7 8 9 it 11 12 18 ,i0 it 00065 R P=' d a I=C a F*i? =ti 2 7 : 7 7 ; 0051.67 „'r=r- rGrt jd1s aJ i l d L1 e at 91 hr!I 1 LS 63. 1 os S atdJ i a L : with 88 Z.Pi flowing [T R[ FROT E:T1 N DE Si G} W. 1 C _O. B x :692 I R[M2 MR 01 081.11 5 OF 6 ---COOLEY- D I CK.I N SON, HOSE'. , 3rd- FLOOR, AREA -#?q 5 HDS -IN LARGEST ROOF! - --- ROUTE NO. 1 DESCRIPTION --- O-ADD DA T PIPE PT P REFERENCE LOSS/FT E FIATS PE. PE -- O.-TOTAL C-FACT -LT .----TOTAL __ P - -- P _ _ __ NOTES ----------------------------------------------------------------------------- OUTLET 1 14.82 1 .049 1 8.7 6.79 _K=5.6--- - C),07 ._._ -i 0 22 - _ F'IF'E 1 14.82 120 C) 15.7 1 . 17 7,C;1 ---OUTLET 2- _ 15.00 -- ..1 ,38C) C) 10.0 7.96 0.28 :=5. _38 C).(-)7 C) C) S,CrCa ;x.22 F'IF'E 29.8 1 0 c_) 1 ci,ci ).72 7.9c_a OUTLET _ 14.011 1 .38C) ci 1 .5 8.6B c:a,6 ' K=5. 18 0, 15 C) c-a 0, C; --FIFE - - 44.74 120 C; J .'_ ci 23 8.27 OUTLET 4 15„ 53 1 ,38C) Ca 8.9C) 1 , 12 K=5.349 0.26-- C)- - C) --- _(--),66 - -- 0,65 - - F'IF'E 4. 60).27 12ci _ OUTLET 5 15.08 1 .• ,.J) i i2.0 1('r,._}9 _ . 1 , ; K=5.0)79 c ,40 2 12 C),ciC) C). i8 • F'IF'E 5 75.34 1. 1 Ca 24.C) 9. 55 8.[31 2.REF 9C)1 0.00 2. 1.54 is 7L . 5 19.x•4 ` X7,046 5 ____-PIPE -__ _6 -__ _a 5._;{l. --__. 12C)- - REF 902 0.00 2. 154 1 1^6.8 24. 56 0.30 P I PE 7 75.34 12C1 C; 192.8 8.78 2= .27 - --REF. ..._19c)=- . 1(_)0.00-- ---4.260---- 1 - 14.9 3 34 --- C) 10----- - - -- - - -- - C),C)C)8 0 24 C),C)o F'IF'E 8 175.34 120 9 C;.31 _ .24 REF 904 0.00 6._57 1 5(--).(-) .6 5 C a.C)2 C),C)C)1 C) 48 °. -I i 2 _ 98.0 _ 0. 11. , 4.6.? - --- F'-IF'E.._ _ 9 17_55 .'34 - i2c=) - "' _ _--- REF 905 15(-),(-)(-) 6.357 1 iC)C),C) 42.87 C).c i7 F'IF'E 1C) =25.34 12C) 10 2521.0 0.88 42.3Ca ---- REF 9c_)6 t:a,(-)C)- 7 980 C) --4(.-)(-) (.) -- -4':_-066- 0.0--r------ _ -- -- ---- 0.(:)C)1 C) C) 0.0 0 PIPE 1.1 _25. 4 140 0 4C)U.c) C).'r5 47.6= REF 907 ci,c)C) 9,9170) C) 1C),C) 48.01 C),C)1 C),C)C)(:) 0 C) 0.00 ---FIFE - -12 �. 4 -14c - -C)- _ -1Ca C)- - ^� 48.0 1 Supply 3-25 GPM AVAILABLE AT 6'2.8 PSI . • 4 OF _-._--COOLEY- DICKINSON, HOST='. , -3rd FLOOR., AREA #2 5- HDS--IN-LARGEST ROOM. --- OUTLET TABLE --- OUTLET # f:-FAC1"OR PRESSURE FLOC; ALIVE. (FEET) MIN. FLOW 1 5.60C) 7,006 14.82 1 ,cm, 1 5.3-38 - -- 7-.9t:y1 _ 15.0(- 3� i yl i- 14 822 _ 5. 18? °.274 14.91 =1 .00 14.82 4 5.349 8.431 15. 5 14.82 5.0-70 _ S 9 i ? 15.f)8 29� 5P 14 e 42 ----------------------------------------------------------------------------- 4:= 5.60 Diameter= 1 .049 Tee=1 Pipe 2.171; F'T= 7„!;n} ARM OVER ----- 0=14.82 Loss/ft.= 1:).1=175- Ell=1- Fiats= 7 F'= 6' C=1201 Total= 9.1"1!7 PT= 7.68 *m:k 6 - Diameter= Tee='2 -, rT- 7.00 Ar?I"i OVER 0=14.82 Lo ss/ft. 1:1.075 Ell=2 Fiats=14 F'= 1 . 51 -_20 TotaI=2'0. 17 F'T= 8. 51 K= 5.60 Diameter= 1 .049 Tee=1 F'i p e= ,_.42� PT= AF:ri OVER 0=14.82 Loss/ft.= 0.075 1-1. 1=1 Fiats= 7 F'= 11.717 _..C=120 - __ _ Total= -9.42 - PT= 7 7: :Trc 4:=5.-'--0 K= 5.6.0 Dia.me;-�m: = 1 .(-1-49 Tee=1 F'i pF;= 8.67 F'T= 7.1-DO ARM OVER -- =14.82 Loss/ft.= O.0-175 E11=1 - Fiats= 7 F'-- 1 . 17 - C=1217 TotaI=15. ._:7 F'T= S. 1-' 1 5. _-r'-. -- - F I PE TABLE:: --- FRICTION --FRICTION ---VELOCITY_ F'IF`E NO. DIAMETER LENGTH FLOW LGPM C LOSS/FOOT LOSS/TOTAL FEET/SECOND 1 1 .049 15.67 14.82 121 1 !7.1.1748 1 = 171 . 2 - I .__T SO ____.lC).00 -- --._.___...--2c?.-E3:3---- 1 .?8t 1 i . 51:1 = 4.74 J'?!_1 t 1. 1518 {1.228 9.6 4 1 ..3807 _ . 17 60_27 1201 i 1.26'4 0.834 12.9 1 .380 24.i ys y- 7 5.34 12C) 0.3,?81 - --- 9i. 554 -- 16 2 6 2. 154 1611 . 517 75.7.4 1201 17.0455 4.621 6.6 7 22. 154 1.92.8? -75.754 1217 C-0455 8.781? 6.6 _ 8 •4.26C1 --;o.92 175.34 1211 ---c .(-()79- - -ij;x.05 - .9 9 '- . 57 98. 1 ) 175.34 i2[y !1.111711 !?, l.iy9 1 .8 17 6.357 ^52.11)_1 _"225. '4 121:) !_1,!_1)1-;5 0.033. 1.1 7.981:1 4til7,00 325.34 -1417 - - y,!_yf1 0 9--- i;, 12 9.97 t7 1l7,ixy ,_, 34 1417 l7,i1i)i7. OF 6 -COOLEY- DICKINSON-HOSP. 4 ?rd FLOOR q AREA #i ,- HDS IN ROOM + 2 IN CORRIDOR. --- ROUTE NO. -1 DESCRIPTION --- O-ADD DA T F'IF`E PT P REFERENCE LOSSIFT E FIATS RE F'F O-TOTAL C-FACT LT TOTAL - F - - PO _ NOTES ----------------------------------------------------------------------------- OUTLET 1 15. 15 1 .049 Cx - 12.0 6.67 -K=5.6 - -- -0.08- _ 2_- ___-4 ca tac> - - 0 'L5 --- PIPE 1 15. 15 1210 0 16.0 1 .25 7.='2 - OUTLET --2- _ ---14.3 2 -1 .1:x49_ - -1 - 4i-,-:-7 - _ t) 3 ._ _ - 4;=5.329 (--).28 Cx 5 ",-).00 0.65 F'I RE 29.98 120x 0 9. _ ?. 55 . .74 OUTLET" _. 16.76 1 ..�so C) 10 10.46 0.68 K=5. 187 t_). 16 i - o..b 5 t-) 5 -F'-IRE - 3 46.74 120 C" 16.3 OUTLET 4 19. 11 1 .:'30) 1 4.8 1.•7.79 1 .34 -_ -K=5.-386 0.'1 i_) 6 - C).S;C).PI PE 4 65.85 1.2(_) C) 10.8 _ .316 12. 59 _.REF 901 i_).t)t) - 2. 154 _ _C)_ -12. 5 -- 111 . 15 0.0.3 5 i) 0 C).,-)o * PIPE 6 65.85 12(--) 0 12.5 0.44 OUTLET 5 21 .93 2. 154 1_) 89.3 17. 59 0.4 ) K=5.268 {_x.06 7 35 (_).00 0. 14 -___P-I RE -_- 5 87 78 ---121_x --- 54-----1=7-t--3,4------- --- --- ----.... -_ ----- ---------------------------------------------------------------------------- REF 9022 0.00 2. 154 1 126.3 25. 13 0.40 PIPE 7 87.78 1210 C) 192.8 11 .65 24. 7? ------- C).009 0 24 0.00 F'IF'E 3 187.73 121_) C) =8.9 0.35 ?6.66 REF 904 C).0 6.35-7 1 50.0 X7. 12 1x.0x2 0.001 C) 48 9. 1.1 PIPE 9 187.73 12Cx 2 98.11 1x. 12 377. it) REF 9Cx5 1.5C).o-":) 6.257 1 10C).0 46.36 C).0x8 0.00)4 C) 152 3.91 P I PE 1 C) -l'r 77.'78 121' 1 Ca 252.0 1 .02- 46 .28 REF 906 C;.t:;Cx 7.980 t-i 4C)C),t i 51 .29 i i.i_:_'. 0.001 01 C) 0 0.(--)C, PIPE 11 33 7.78 14(--) C) 400.0 C).?'? 51 .26 REF 90 7 i;.C)i f 9.970 1=) 10.0 51 .66 Ca.C)1 i�.c)(-)C) C) 0 1_),1)C) F'IF'E - 12 33 7.78 140 0 10.0 0.00-) 51 .65 51 .67 Supply 3 8 G 'M AV A T LABLE AT 62.8 PS I . 2 OF 6 -COOLEY DICKINSON HOSP. 3rd - FLOOR, AREA_ #14 -HDS-I N _ROOM 1 A IN CORRIDOR. --- OUTLET TABLE --- OUTLET # K:-FACTOR PRESSURE FLOW ALIVE. (FEET) MIN. FLOW 1 5.600 7.324 15. 15 30.00 14.82 ----- � __ -5:-329 _ _ 7_.7 37 _ -14 82 _ - 30100- - _ 14x82 5. 187 10.439 16.76 30.00 14.82 4 5.386 12. 591 19. 11 29.67 14.82 ____ 5.268 7 -21 ,93- - - -- 29167 ----- 14;82 K:= 5.60 Diameter= 1 .049 Tee=1 Pipe= 2.75 PT= 7.00 ARM OVER - - 0=14.82 - Loss/ft.= 0.075 - Ell=1 • Fiats= 7 P=- 0.73-- Total= 9.75 PT= 7.73 * # K=5.329 ;x -K= 5.60 Diameter= 1 .049 Tee=1. - Pipe=. 6.50-- PT=_-7 w00- - ARM _OiyER 0=14.82 Loss/ft.= 0.075 Ell=2 Fiats= 9 P=... 1 . 16 C=120 Total=15. 50 -'T= 8. 16 K=5. 187 K:= 5.60 Diameter= 1 .049 Tee=1 Pipe= 0. 58 PT= 7.00 ARM OVER 0=14.82 Loss/ft.= 0.075 Ell=1 Fiats= 7 P= 0. 57 s;,i;_.... Total= 7 d % __PT= 7;57- -*** K=:5.386 K:= 5.60 Diameter= 1 .049 Tee=! Pipe= 5. 17 PT= 7,00 ARM OVER . .0=14.82 . Loss/#t. 0._y75--Ell=1 ---- Fiat s= 7--- _ - -P- 0i91 -C=12(..) Total=12. 17 PT= 7.91 K=5.268 �K; ---- PIPE TABLE --- FRICTION FRICTION VELOCITY PIPE NO. DIAMETER LENGTH FLOW GPM C LOSS/FOOT LOSS/TOTAL FEET/SECOND -------- �, t - - --1 ,049 __ _ 16,00 -15 0�,5-----1,.,i� -----�^?:i��779----`--1:.�.4u .._�Q 6,- _- _ __. ---- 2 1 .049 49 9,25 29.98 120 0.2751 2. 545 11 . 1 1 .380 16.25 46.74 120 0. 1646 2.1�74 10 0) 4 _ - 1 .380 . ___ 10.83 -- - 65.B5 -- -120- -t;;, 1t:._ ---- ?61- -- --144.1 - --. 5 2. 154 124.75 67.78 120 0,0604 7. 535 7.7 6 2. 154 12. 50 65.85 120 0.0355 0.444 5.8 7 2. 154 -192.83 - - __ _. 87.78_.--- 120----c";-e O6O4 ._-- ._- t l _647...- 7.. 7 E3 4.260 38.92 187.78 120 c_;.OOB9 0.347 4.2 9 6.357 98.00 187.78 120 0.0013 0. 1.'24 1 .9 10 6.257 252.00 337.7B - 120 0.0041 1 ,023 - .5 11 7.9BO 400.00 337.78 140 0.0009 i r.x:73 2.2 12 9.970 10.00 3 ;7.78 140 0.0003 0.003 1 .4 ...a� 3 HYDRAULIC DESIGN INFORMATION SHEET Project Name: COOLEY DICKINSON HOSP. , 3rd FLOOR Date: 5/28/93 Calc by: FIRE PROTECTION-DESIGN, INC. ------------------------ -------------------------------------Sht----#la----of----6------ Protection by: WAREHOUSE MECHANICAL CONTRACTORS, INC. 250-A OLD LYMAN ROAD SOUTH HADLEY, MASSACHUSETTS 01075 COOLEY L NORTHAMPTON, MASSACHUSETTS -------------------------------------------------------------------------------- SYSTEM DESIGN & CALC SUMMARY: HAZARD DESCRIPTION: HOSPITAL LIGHT HAZARD. LARGESTMROOMUr+ 2EHDSNINRUNPROTECT�DaCSMMUNICATING SPACES. BASED ON N.F.P.A. #13 WET SYSTEM SPKR ORIF. SIZE = 1/2" K-FACTOR = 5.6 REQUIRED WATER AS CALCULATED: SYSTEM REQ' T 88.00 GPM I/S HOSE &/OR RACK ALLOW. 250.00 GPM AT B.O.R. OUTSIDE HOSE (OR COMBINED) 0.00 GPM TOTAL WATER REQUIREMENT 338.00-_GPM AT P.0 C. PRESSURE REQ' D: @ P.O.C.= 51 .67 P.S. I . @ B.O.R.= 51 .24 P.S. I . -------------------------------------------------------------------------------- - WATER --SUPPLY:--- - - STATIC PRESSURE: 65 P.S. I . RESIDUAL PRESSURE: 55 P.S. I . @ 827 G.P.M. FLOWING FLOW TEST DATE: 5/28/93 LOCATION: 10" CITY MAIN ON LOCUST ST. INFORMATION SOURCE: NORTHAMPTON DPW & FIRE PROTECTION DESIGN, INC. FLOW GRAPH SUMMARY: TOTAL-PRESSURE AVAILABLE -@---338.00---G.P.M.--=---63.090 -- P.S.I . —- TOTAL WATER AVAILABLE @ 51 .67 P.S. I . = 966.01 G.P.M. -------------------------------------------------------------------------------- ABBREV I ATI ONS: ---- PT- =--PRESSURE TOTAL------ --- - -E -___90 DEG. ELL BV - BUTTERFLY VA ALV - ALARM VA PE —PRESS. ELEVATION EE - 45 DEG. ELL GV - GATE VALVE DELV - DELUGE VA PF - P. FRICTION LOSS LT - LONG TURN CV - CHECK VALVE DPV - DRY PIPE @--OUTLET/SPKR ---- T----TEE -- --------DCV ---DETECTOR-CV------STR--- STRAINER-- CALCULATION SEQUENCE: OUTLET (or sprinkler) TABLE: Discharge Summary - Shows flows at all outlets. ROUTE #1 DESCRIPTION: Primary Water _Path _.__f_r_om .startin.g_Spr_inkler--_.to_Suppl_y_-_- __ - ------- point -- followed--by subsequent Primary Paths. LEG ( pipe) TABLE: Describes ALL PIPES used in System Calculation . i +4