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23B-046 (184) �O0 �U UY�K�W��N U�rD « ' �| ��~ � �0 ~�N 0U�� n�^N 0 U�� �N ��N rn�p� �uo��/ u�"xcn~m� n"�. ' x �<�� r�°"�, " . �v u/// uro` nvVo � nu� �n "m/. �r..��' _ TI -i - I-j- ITI row. -1 tii-[Fl--J-1-Ir 20 li I 4-1 LL - - _ - - ' - 6 7 8 9 DesiJua1=55 F1o@=027 SUST80,68 -US,D=48^84 How 2r0 �' �^ ��1� �U�1 ��'1� �� �^ ^� O�� �0^� psi �V�^ ��'l� �� �h �w' � z—^ ^ ^°�~ ~ ^~' ~^ r-~ -- - r-- '-- � � ' � � � 5 OF 6 _ COOLEY DICKENSON HOSP. , 2nd FLOOR, AREA #2, 5 HDS IN LARGEST ROOM. --- ROUTE NO. 1 DESCRIPTION --- ------- -- Q-ADD -- DIA--' -- T--PIPE ------'--p/T- �___ ----- F«� REFERENCE LOSS/FT E FITTS PE PE ' 0-TOTAL C-FACT LT TOTAL PF_ PO _ _ NOTES - � _________________________________________________________-_________________ OUTLET 1 15. 15 1 .049 1 8.7 6.67 K=5.6 0.08 1 7 0.00 0.65 -PIPE -1- 15. 15 120 0 15.7 1 .22 7.32 ,OUTLET 2 14.82 1 .049 0 10.0 7.89 0.83 K=5�338��� - 0.28- 0 �� 0 -� - ����'0.00 ���- O.'65'' PIPE 2 29.98 120 0 10.0 2.75 7.71 OUTLET 3 16.89 1 .380 0 1 .5 10.64 0.68 K=5. 183 0. 17 0 0 0.00 0.65 PIPE 3 46.86 120 0 1 . 5 0.25 10.61 _________________________________________=_=�__��______=___=____=____________ - OUTLET 4 17. 15 1 .380 0 3.2 10.89 1 .27 K=5.349 0.29 0 0 0 .00 0.65 _ -PIPE- '4---64.01- ��- 120 -- 0 - 3 _2----0.93 ---10.27' - OUTLET 5 16. 57 1 .380 1 12.0 11 .82 2.01 --K=5­079----�------ -��--�0�45--- -2----1I! ------T)�65-----0.83---------------- ------------ PIPE 5 80. 58 120 0 24.0 10.82 10.65 - REF 901 0.00 2.154 ' 0 76.5 ---23�29- ----------'----'' - -�- - - - -- 0.052 5 25 0.00 PIPE 6 80. 58 120 0 101 . 5 5.23 - - - -- ___________________________________________________________________________ REF 902 0.00 2. 154 1 126.8 28. 53 0.34 0.052 8 66 0.00 ---PIPE ' - 7 - ' 80. 58 120 0 192.8 --- - 9.94' ' -'28.i9 - - -' ___________________________________________________________________________ REF 903 100.00 4.260 1 14.9 38.47 0. 11 0.008 -- -0- '24 ' -� -' 0.00 - - - PIPE 8 180. 58 120 0 38.9 0.32 38.36 ___________________________________________________________________________ REF 904 0.00 6.357 1 40.0 � -38.79 ' - 0.02 0.001 0 48 4.77 PIPE 9 180. 58 120 2 88.0 0. 10 38.77 ---------------------------------- REF 905 10.00 6.357 1 100.0 43.67 0.08 0.004 0 152 3.91 --­PIPE---10--'330�58----12n----10--252��0----T[ 91----43�59- REF 906 0.00 7.980 0 400.0 48.48 0.03 ��'-----0 Do 0 y'--0 0.00 �---- PIPE 11 330. 58 140 0 400.0 0.36 48.45 �--REF - 907 ' 0.00�� -'9�97()---0'----�l()�7T----z[8�84---_-0�{'I---' -- ------ - -- - � 0�000 0 0 0.00 PIPE 12 330. 58 140 0 10.0 0.00 48J33 =-====,=======�-====,===---------.------------- --------_--______________________ supply � 48.84 -'-- - --730-l�PMAVAILAB1.__E-AT-63PS�.-------------------- ---'------ ------------ - - - --- 4 OF COOLEY D I CKENSON HOST'. , 2nd FLOOR, AREA #25 5 HDS IN LARGEST ROOM. --- OUTLET TABLE --- -OUTLET # -__-1:nFACTOR__ c'EELSt;RE FLOW FEET)-- MIN! FLOW 1 5.600 7.323 15. 15 20.00 14.82 2 5.338 7.710 14.82 20.0,-, 14.92 -- ---- -5-IB3 10014 1.SoS9 -2t).i_iJ 14 4 5.349 10.274 17. 15 20.00 14.82 5 5.079 J79 1 i J.645 16. 57 19. 58 14.82 K= 5.60 Diameter= 1 .049 Tee=! Pipe= 2.00 PT= 7.00 ARM OVER .0=14.82 Loss/ft.= 0.075 Ell= Fi= _s= 7 F`F= 0.67 C=120 Tota3.= 9a_;tJ FT- 7,68 m K=51349 5.60 Diameter= 1 .049 Tee=2 Pi 6. 17 PT= 7.00 ARM O'•.,'ER 0=14.82 1_o s=, __ _ 0.075 E11=2 Fitts-14 - - P: 1 . 51. ..LL 1-12`..7 Total-+._=J. !l PT= 8. 51 r°r�r K=5.079 k..-- 5„60 Diameter= 1a 049 Tee=1 Pipe= 2142 f-'? - 7a00 A i ._'vE;i 0=14.82 Loss/ft.= 0.075 Ell=! Fitts= 7 PF= 0.70 C=12t:J Total- 9.4: PT= 7.71 wa•w K=5. _38 T T T 1• K= 5.60 :i gymete r= 1 .049 Tee=1 Pipe= 8.67 PT= 7.00 ARM OVER 4 .2 Loss/ft.= 0.075 Ell=1 Fitts= 7 F'F= 1 . 17 --C=120- K= 5.60 Diameter= 1 .049 Tee=1 Pipe= 2.42 PT= 7.00 LJs s 7 f t.= 0.075--El l=1 . Fi t Lam=- 7 - -- - Fi -w ' - C=120 Total= r .4.• PT= r *n. t'..--5 ...�, ----- F'IF'E TABLE --- ----- ----- - - -- -------------F'R�I CTIOi<(---'F"Fi I CT:[ON...__Vf=CDCW=.r FIFE NO. DIAMETER LENGTH FLOW GPM C LOSS/FOOT LOSS;TOTAL FEET/SECOND t 1 .049 15.67 15. 15 120 0.0779 1 .220 5.6 _2-.__. --11049 1 Ja J0--------------29.9° ---1-2C)----t;e-2751---- :751 _ 1 Al---- 1 .3BO 1 . 50 46.86 120 0. 1654 0.248 10. 1 4 1 .380 3. 17 64.01 120 0.2944 0.932 9.32 13 _ 3�+t _ i --=. �,�, 80158 120 t_JesgSi_,S Jc_=.°1.8 _M_. 6 2. 154 101 . 50 80. 58 120 0.0516 5 a 233 7. 1 7 2. 154 192.8= 80. 5B 120 0.0516 9.941 7. 1. - '-_- - ------ -_. ------- �, -_ _4•eJ 6tJ _�'8- 9-, 18C)e58 120 0,608 -- -_ 01322- - -. a - 9 6.357 86.00 180. 58 120 0.0012 0. 104 1 .8 10 6.357 ' 252 n i 0 330. 5B 120 0.0036 0.910 _ .--- --i _._. .....--. �.-.-.-.-..._ �. . : _..-__-.__._..._,.-f__._ .. _ .3211 _._ .._4-1 at1�71Ju..._._____-_-�)-o-'•�C� __.______. ._ ....., 1_--._-. .. _.. 12 9.970 10.00 330. 58 14 0 0.0003 0.c:03 1 .4 COOLEY D I CKENSON HOST'. q 2�d FLOOR., AREfi HDS INI, ROOT; 2 I l'd COPR I LSO;:. --- ROUTE NO. 1 DESCR I E'T I ON --- REFERENCE LOSS/FT E F11-TS E'E E Q-TOTAL C-FACT LT TOTAL PF F`O NOTES OUTLET 1 15. 15 1 .<:149 C) 12.0 6.67 K=5.6 0.C)8 4 C),(-)Ca 0.65 OUTLET i 14,82 1 .'_)49 1 -0- 5 t)z00__ -- ---t^)R65--- _ _ --- .7- FIFE 201 .9 2. 54 7 -. OUT 1-T � -,_ i v-.,.817 {) 1t^)= _ __10.4._. ;).c8 LET _ 1 . , PI PE 4.a ..._ 12;, {_' 1L . _ �.L 1_).4 OUTLET 4 19. 11 1 .380) 1 4.8 1=.78 1 .34 (!' u.'r 4 fj t i._�. i.) t.� {_),t_:t_i {7.. -1.4 r REF .(--)1. C) Of- .._, 15 , t 4 FIFE 65.8 120) Q 12.5 0.44 OUTLET PI PE 5 o, z i) O T. :r 17. REF 902 0.00 t 2. 154 1 126.8 25. 11 C).4,=) C).060 8 66 0.00 _..� PE--------,r--_'____37__.75___ -- REF 903 100.00 4.260) 1 14.9 36.75 3, - F'IE'E 8 187.75 12{) C> 3°.9 C).35 =.6. --- - --0.,c C,ai 48 41,7_7 PEE Yid 7 l 12'{) 3 C) r", (,Z -'i7.,t,9 WL REF 9(--)5 250.00 6.257 1 1.0C).C) 41 .90 0 C) 0.004}4 0 152 3.91 REF 9t"a -79 40C),i) 4 � 6, 3 . . - - --- t_a,ty i 1 ,(_t_) u F'IE'F. 11 :7,37.-175 14C) i') 4C aC a.c_a 0.37 46.8,:) ----- - Ci,CiCiCi is to t,a.t7[_a E'IE'E 12 3.T7.75 14,- Ca 1C).,:) 0.00 47. 19 - 47.21 St_tpp Y _._.8. CC,, I A v'Al.LAB�.E- 2 OF 6 ' COOLEY DICKENSON HOSP. , 2nd FLOOR, AREA #1 , 3 HDS IN ROOM + 2 IN CORRIDOR. --- OUTLET TABLE --- --OUTLET-#---'K=FACTOR----PR­ESSURE------Fl_OW----ELEV:-(F . _MI%-FLOW----' -- '---- 1 5.600 7.319 15. 15 20.00 14.82 ' 2 5.329 7.732 14.82 20.00 14.82 20T00- 4 5.386 12.583 19. 11 19.67 14.82 =- ` 5 5.268 17.325 21,93 19.67 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 Fitts= 7 PF= 0.73 C=120 Total= 9.75 PT= 7.73 '*** -K=5.329 *** ___________________________________________________________________________ ^ K= 5.60 Diameter= 1 .049 Tee=1 Pipe= 6. 50 PT= 7.00 ARM OVER 0=14.82 Loss/ft.= 0.075 E11=2 Fitts= 9 PF= 1 . 16 C=120 Total=15. 50 PT= 8. 16 *** K=5. 187 *** ---------------------------------------------------------------------------- K= 5.60 Diameter= 1 .049 Tee=1 Pipe= 0. 58 PT= 7.00 DELETE 0=14.82 Loss/ft.= 0.075 E11=1 Fitts= 7 PF= 0. 57 C=120 Total= 7758 PT= 7. 57 *** K=5.386 *** --------------------------=______=__==_==____�-,__=_��__==-_=__�____--------- __ ' K= 5.60 Diameter= 1 .049 Tee=1 Pipe= 0. 58 PT= 7.00 ARM OVER 0=14 .82 Loss/ft.= 0.075 E11=1 Fitts= 7 PF= 0 . 57 C=120 Total= 7. 58 PT= 7. 57 *** K=5.386 *** ___________________________________________________________________________ K= 5.60 Diameter= 1 .049 Tee=1 Pipe= 5. 17 PT= 7 .00 ARM OVER 0=14 .82 Loss/ft.= 0.075 Ell=! Fitts= 7 PF= 0.91 C=120 Total=12. 17 PT= 7.91 *** K=5.268 *** ___________________________________________________________________________ --- PIPE TABLE --- ---�--------'--------'--------- Ib � ELOCI-TY----'--- PIPE NO. DIAMETER LENGTH FLOW GPM C LOSS/FOOT LOSS/TOTAL FEET/SECOND 1 1 .049 16.00 15. 15 120 0.0778 1 .246 5.6 ----2 - ----YITI-'------- 3 1 .380 16.25 46.72 120 0. 1645 2.672 10.0 4 1 .380 10.83 65.83 120 0.3101 3 .359 14. 1 -- 5 - -'21154 12W75- ----87.75 - 120---'(>�{�,04�---' --7'�53i - - -7.7-- �-'-- - 6 2. 154 12. 50 65.83 120 0.0355 0.443 5 .8 7 2. 154 192.83 87.75 120 0.0604 11 .640 7.7 -------8-------4�260 ---38192------'187Y75---120--l}!()089---- --V347 -- - -74:2 - 9 6.357 88.00 87.75 120 0.0003 0.027 0.9 , 10 6.257 252.00 337.75 120 0.0041 1 .022 3. 5 -----1I------7.980---400�0(>-----337�75---140--- '--- -----�,��j----- -- 12 9.970 10.00 337.75 140 0.0003 0.003 1 .4 ^ ^ "')r ID 1FZ#ck U L_ I C LIGULA1T I C3r%1E3 fr --- -- ------ COOLEY DICKENSON HOSPITAL, 2nd FLOOR, MED-SURD UNIT - - -- ---------- --- ------ ----LOCUST_ STREET_ - ------... - - - NORTHAMPTON, MASSACHUSETTS — --- _ --- - --- ---- ------- -- _ -_CONTRACT -NO. -------- _. - - --- - - DATE - 8/18/93 DESIGN DATA— :;CI..t..!EF-iNC1' .(._f_.A....SIFICATION HOSPITAL, LIGHT HAZ. DENSITY 0.10 GPM :'SQ. FT AREA OF APPLICATION ROOM SO. FT. COVERAGE f:°'Ef.' SF R T Nil".LER 163 SO. FT. L NO .' �?�' E,F 1 :I f`d4,LEf-�.:a l..H!_.. -!1--ATE11; 5 SPK:R. K:-FACTOR 5.6 TEMP. 165 T'=1Tf11_ WATER Ef REn!_1 I RED==D '30.58 C- f INCLUDING HOSE STREAMS. NAME OF CONTRACTOR - WAREHOUSE MECHANICAL CONTRACTORS, INC. NAME OF DESIGNER - N. GAGE/FPD AUTHORITY HA"I NG JURISDICTION .- FLOW TEST - STATIC- _65_._f ES I_DUAI.-55 SYSTEM! DEMAND AT BASE OF r;I S•ER IS 7530.58 Gf='f#•? -1T 48.48 E`S I SYSTEM DEMAND AT SUPPLY IS 330.58 GPM AT 48.84 PSI . _._._. 1_071..9 AVh)_I_L��L._E._.?T_ 4B_.S4-F�Ig------------------------ --- ------ ------ 63 PSI AVAILABLE. WITH 330.58 GPM FLOWING. REMARKS - SYSTEM CALCULATED_USING, _ROOM _DES I GN._.METHOD. THE SPRINKLERS IN THE HYDRAULICALLY MOST DEMANDING a ROOM + 2 HDS IN COMMUNICATING SPACES WITHOUT SELF- CLOSING DOORS__WERE_C ALCULATED.-_T._O__.O_:10--GPM/-..SQ.__F-T_._ ' i }I !�'�i it �i is+' r i,ff}ilEr DICKINSON f�ii:rITHL, ,,r,�f F�fffl :, MED - 'SIliRG UNIT --_1_ f ???sir! j +ii• 11111 ?111!11!� kl! III � ? illt ? ! Ilii � � I � I � � iflil fl � l � i � ll � i I 1 Im It I III 6►i ( I � � f f l i !, 44 I l j L If I ! I ( e I fill I i ? ! �. } e i i ! 1 i 1 1 +� 1111?!!III i, I j11 I I I I ? III ! 1 �1 i }? I I f ? 1 � ' I � ' � I I I ! � I ? f 1 � } I if � t ; },l; Jf�?{I�LI':':! �Ie.P':!1.f!i !'11iN=,;Ifl fir i . J Li i ri '!1 _1 ! + 1 li Lt lij. Li J J�1 D I,ld i w 1�,'i:°I�,I I��I I j[+ t�,+r :!�.�! Ii U�1 } 1:;! I [IS I ICI ti 1�,1 Ic�LI 1}: �!i S +r t? i t i J ELI!;I I I II� L I !E ! ! I C!. I �� !,� CI ri 141 !� (jl { I�r}i �'{J _ .L � ►�TFf.,TIff} I{.�tf�H II}I_ } ,ff, �;f.!i'I !A9 itlPRREf" , 5 OF 6 -----COOLEY- D I C"K I NSON, - HOSF'. . •3rd FLOOR.- AREA #?,--5- HDS I-N LARGEST ROOM. --- ROUTE NO. 1 DESCRIPTION --- Q-ADD DA T F'IF'E PT P REFERENCE LOSS/FT E FIATS PE. PE ---- -- -- O-TOTAL C-FACT - LT - TOTAL F - PO - NOTES --------------------------------------------------------------------------- OUTLET 1 14.82, 1 .049 1 8.7 6.79 - K=5,6 _ _ - _t),07 -1 - -7 -- f) !)t-r- F'IF'E 1 14.82, 12,0 0 15.7 1 . 17 7.2,)1 ----OUTLET- _'2 15,ti(--) 1 .-°;8t:r C lt:a.o 7.96 K=5.3:8 ).07 I) t-7 O,00 F'IF'E 2,9.8? 12,p t) 10.0 0.72 7.92,i OUTLET _ 14.91. 1 .38Ca t-a 1 .5 8.68 K=5. 18.3 i), i 5 i-) c-r c-),_;i; -a.22 -___P_IPE---.__. ._ 44.74 11 - t_2, i . -i a.2,.3 - 8.2,7 OUTLET 4 15. 5' 1 .38t-a c-a _ .2 8.90 1 . 12 K=5.349 _ 0.2)b _a - - i) _ _.. - t?.65 --2,).65 - F'IF'E q 6ti.?7 12,ti c-a = .2, c-).8•? 8.=1= _ OUTLET 5 15.t)8 1 ,3a0 1 12,.0 - 1.t-a.: 9 _ 1 . b _ k::=5.079 ir.4(-) 2, 12, ii,()c-) s). 18 PIPE 5 75.34 1.2,0 c? 2,4.0 9.55 8.81 REF 901 {-),c-)c-) 2. 154 ) 76. 5 1.9.94 - .{-)46 5 2,v t-t,t7i) --6-_ 75.._4 - 1^t-; " - ls)1 . 5 _ ..--4.b --- _ - _ - REF 902, 0.00 2,. 154 1 12,6.8 2,4. 56 0.30 - 0.046------ -8-----bb ---_. -t-) t)t;) _-----T-_�. --- -- - ---- - ----- F'I PE 7 75.34 12,Ca t-) 192,.8 8.78 2,4. 7 ------REF-- 91,-)3 _100.00- 4.26 a - 1- -- 14.9. - ---t r 1t:)----- ----- -- - - -._ -0.008 i) '?4 0.00 F I FE 8 175.'3 4 120 t y 38.9 0.31 _33.24 REF 904 c'.,tic-r 6.3 57 1 5 c-a,C a - _ .6 5 ),Crc-;1 0 48 9. 11 --FIFE -9- 175,.�.�� _ 120 _. 2 93. - t-;. 11 - REF 92,x5 15{-0.00 6.357 1 i(ml. ) 42,.87 0.{-a7 PIPE 12,) 322 5.34 122,) lia 2,5") ) t:).88 42,.8c.) REF -- 9;?6 _ _t-),c it} 7.98t-a _ i) -42,2,c-).t.) -47.66 --t-) 03. - - -- ------ ir,t7t-)1 c-) C) 0.00 PIPE 11 32 5.34 140 it 400.0 0.35 47.63 REF 907 c 2,.00 9.9 7 0 c-) 10.0 48.01 t?.01 - F'IF'E -12, 325.34- ---- -140 _____ ___o__- l i)r t-) - t-r,C)t r-. 48.-(:)0 --- - - ' q.8.i)1 Supply "3225 GPM AVAILABLE AT 6'2.8 PSI . 4 OF ----COOLEY DIGK:INSON, HOSP. , 'rd FLOOR, AREA #?-; -5- HDS- IN_LARGEST- ROOM. --- OUTLET TABLE --- OUTLET # FACTOR PRESSURE FLOW ALIVE. (FEET) MIN° FLOW 1 5°600 ?°i C)6 14,ry r;i, 1- °U 5.. _8 7.?01 15,0 i1 1,t;[; i4 .8 5. 1e' 8.227 4 14.91 31 ,!)!) 14°e2 4 5.=49 e°4.31 15. s, 3C).C1i) "_?°8-:) 5,07? e°e13 15,03 L9. 5e 1.4.8 --------------------------------------------------------------------•-------- K= 5°6C) Diameter= 1 .049 I'ee=1 F'_Pa= ,cli ET= ?, )ii ARM OVER 0=14.8^ Loss ft °= (-).U75 E11=1- Fiats= 7 E,._ i;°6 , C=12`0 Total= 17.(i_l PT= 7.6-8 **)k K=5--341 ;.k P::=- 5.6{) _ Diameter= 1 .0.,11.o Tee=2 F'ipe= 6. 17- PT= 7. ARM OVER O=1 =°e? !_oss/ft :)°��?5 Eli==^ Fiats=14. F= 1 . 51 G=1yC' Total-'2i=). 17 PT= 8° 51 K:= 5.60 D'iafneter= 1 .049 Tee=1 F'?pe 4 ' E' 7.Q ARM OVER 0=14.82 Loss/ft.= 0.075 1-11=1 Fiats= 7 s== 0.70 --C=1 t; _ - - Total=-9.4 PT-7.7_ K:=5. R )kkm =i, =, ; Diameter= 1 .iJ 49 T e= Pipe= 8 -r PT= 7_1)%, ARM OVER K.= �•_ 1)zc:me�_er- e e_-�. E`2 e= � .6% J�..�-e' _. ma _ _ c= .�2 Loss/*t.- � ,U , Fia s= r t .1 j C=120 Total=15.67 PT= 8° 1? - -- P I PE TABLE: --- ---- _ FR I CT I ON- --FR I CT I ON -_ -_VELOC I TY FIFE NO. DIAMETER LENGTH FLOW GE'M C LOSS/FOOT LOSS./TOTAL FEET/SECOND 1 1 .049 15°67 14°82 12t l 0.0748 1 ° 171 5. 5 1 .330 10.00 29.e ._ -i2i?---i7. )?17----- ii-,717 - _6 n _. _.. 1 .7180 1 . 50 44.7 4 1a'i l ( . 1518 C 7°?28 9.6 4 1 °380 : . 17 60x27 120 0.26 34 Q°8:_ 4 12.9 -- 5 i °?Qi7 _ _-24°t ii:) - - 75.34 - 12C l __._ i;-,_;98i c?. 5r,i, _ 16.2 6 2. 154 101 . 50 75.34 12C) 0.0455 4.621. 7 2. 154 1.92.83 75.3? 12t; 0,0455 8,78U 6.6 8 _ 4.26() 38.92 175.34 120 __ -t 0.0078 __ o,".i:)5, _ _ - °q 9 6.357 9 e.i_)i_7 11-5.7.4 1',_'i_7 i-7,(-,.c;11 (1. -i (:)9 1 6.35/= 2 5 2°i)t_7 _2 5° '4 1217 c_;,i)l_l. 5 I_l.8 e•� _ , _ 11 7.98K) 40,1-) 00 _ _ 32,5,34 144 ---- 0..ta009 12 9.9 7c:) 1i,;°i)ii x'25.3=I 14c1 t7,i7tii)' ;,C;i_l:? 1 ° _ OF 6 -COOL€Y-- DICKINSON -HOSP 3rd FLOOR;-- AREA- #1 ;_-_3- HDS I N-ROOM -+_ 2 IN CORRIDOR. --- ROUTE NO. I DESCRIPTION --- O-ADD DA T PIPE PT P REFERENCE LOSS/FT E FIATS PE PE - - Q-TOTAL C-FACT LT -TOTAL_ _ P _ PO __ . NOTES --------------------------------------------------------------------------- OUTLET 1 15. 15 1 .049 t_) ' 12.0 6.67 ._k=5.6 _ _ c),t_)8-- 2 - - 4 0.00- _ 0,65 . PIPE 1 15. 15 120 0 16.0 1 .25 7.32 -OUTLET 2 14.32- - --1 .049- - 1 - 4.3 7.92 _ _-- W83- - K=5.3 29 0.28 0 5 0.00 0.65 PIPE 2 29.98 120 0 9.3 2. 55 7.74 OUTLET _. 16.76 1 .380 0 10.3 10.46 0.68 K=5. 187 0. 16 2 6 0.65 0.65 ..PIPE 3 46.74 120 . =) 16.3 2.67..-.It). OUTLET 4 19. 11 1 .380 1 4.8 13.79 1 .34 . .K=5.386 0.31 1 0 6 _ _i a.00 - 004- PIPE 4 65.85 120 is 10.8 3.36 12. 59 ...REF - 901 0.00 _ 2. 154 ,i_. 12. 5 -- 17.15 PIPE 6 65.85 120 0 12. 5 0.44 OUTLET 5 21 .93 2. 154 0 89.8 17. 59 0,40 ` K=5.268 0.06 7 35 t), it:) 0. 14 ..PIPE... .5---- 37.78-_.I20..---0-.124"8.----- 7.-54 --- 1=i o._+4 - - --------------------------------------------------------------------------- REF 902 0.00 2. 154 1 126.8 25. 1 3 i a.40 i ------------- -._. _ ---------____-- PIPE 7 87.73 120 0 192.3 11 .65 24.73 9----•T6 ---- 0.009 0 24 0.00 PIPE 8 137.73 120 is 38.9 0.35 36.66 REF 904 0.00 6.357 1 50.0 37. 12 0.02 0.001 001 0 48 9. 11 PIPE 9 187.73 120 2 98.0 0. 12 37. 10 REF 905 150.00 6.257 1 100.0 46.36 i).t i8 0.004 0 152 3.91 PIPE 10 337.78 120 10 252.0 1 .02 46.28 REF 906 0.00 7.980 0 400.0 51 .29 0.0:51 PIPE 11 337.78 140 0 400.0 0.37 51 .26 REF 907 0.00 9.970 c_) 10.0 51 .66 0.01 PIPE - 12 337.75 140 0 10.0 0.00 51 .65 51 .67 Supply 333 GPM AVAILABLE AT 62.8 PSI . OF 6 _._.__ EY -DICKINSON HOSP: 'rd FLOOR AREA-#1A 3 -HDS_I N_ R00M _i- 2- IN CORK I DOR. --- OUTLET TABLE --- OUTLET # K:-FACTOR PRESSURE FLOW ALIVE. (FEET) MIN. FLOW 1 5.600 7.32 4 15. 15 30.00 14.82 "' 5.329 7.737 30 WOO _ _ 14.82 5. 1O7 10.4 39 16.76 30.00 14.82 4 5.386 12. 591 19. 11 29.67 14.82 - . - 3-. 2_ .9 - L 4 67 - 14.82 - 268 1.7 � ; , � �,� K= 5.60 Diameter= 1 .049 Tee=1 Pipe= 2.75 PT= 7.00 ARM OVER - 0=14.8'.: - Loss/ft.= OwO75 ._ Ell=1 • Fiats= 7 - P= Oi73- - C=120 Total= 9.75 PT= 7 .73 K=5.329 --------------------------------------------------------------------------- _K= 5.60 Diameter= 1 .049 Tee=! - - Pipe= 50 - - PT=---/ OO- ARM OVER 0=14.82 Loss/ft.= 0.075 E11=2 Fiats= 9 P= 1 . 16 C=120 Total=15. 50 PT= 8. 16 K=5. 187 K= 5.60 Diameter= 1 .049 Tee=! Pipe= 0. 58 PT= 7.00 ARM OVER 0=14.82 Loss/ft. - 0.075 Ell=1 Fiats= 7 P= 0. 57 - C=120 _. - Total=--7-;58---PT= 7;57 - A** K 5.x.8,5 K= 5.60 Diameter= 1 .049 Tee=1 Wipe= 5. 17 PT= 7.00 ARM OVER - 0=14.82 - Loss/ft.= 0.075 --Ell=1 -----Fiats= 7-._ _ -P=-0;9 - C=120 Total=12. 17 PT= 7.91 K=5.268 **3 ,. ---r._-._....._.-.._-----------------_._.._.-._-------------------------..-_.---.--'-.-------------- --- PIPE TABLE --- FRICTION FRICTION VELOCITY PIPE NO. DIAMETER LENGTH FLOW GPM C LOSS/FOOT LOSS/TOTAL FEET/SECOND _1 ____ -- _-1a049 -- __ ----5-.,-6- -- ----- 2 1 .049 9.25 29.98 120 0.2751 2. 545 11 . 1 1 .380 16.25 46.74 120 0. 1646 2.674 io.cl _ . 4 - 1 .380 -._ 10.83 -- 65.85 ---120-----Ov3lO3------ -=;61- _. --14. 1 _ . --- 5 2. 154 124.75 87.78 120 0.0604 7. 5 35 7.7 6 2. 154 12. 50 65.85 120 0.0355 0.444 5.8 24154 192.83 .._ _. -87y78 --- _ l2O--__c">,c:6O4- -_... .,_t _x,47.._.__ 7 . 7 8 4.260 38.92 187.78 121 y 0.0089 0.347 4.2 9 6.357 98.00 187.78 120 0.0013 0. 1.24 1 .9 10 6.257 252.00 37.78 120 0.0041 1 .02 y 5 11 7.986; 400.00 337.78 140 0.0009 0.x'73 2.2 12 9.970 1 c i,tai; 337.78 140 0.0003 0.003 1. .4 t HYDRAULIC DESIGN INFORMATION SHEET Project Name: COOLEY DICKINSON HOSP. , 3rd FLOOR Date; 5/28/93 Calc by: FIRE PROTECTION DESIGN, INC. Slit #1a of 6 -------------------------------------------------------------------------------- Protection by: WAREHOUSE MECHANICAL CONTRACTORS, INC. 250-A OLD LYMAN ROAD SOUTH HADLEY, MASSACHUSETTS 01075 ----Property:-- _ __ _ _- -_ - -COOLEY DICKINSON HOSPITAL __ __ - MED - SURG UNIT, 3rd FLOOR LOCUST STREET NORTHAMPTON, MASSACHUSETTS -------------------------------------------------------------------------------- SYSTEM DESIGN & CALC SUMMARY: HAZARD DESCRIPTION: HOSPITAL LIGHT HAZARD. - LARGESTMROOMUr+ 2EHDSNINRUNPROTECTEDdCOMMUNICATING 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.O.C. PRESSURE REQ' D: @ P.O.C.= 51 .67 P.S. I . @ B.O.R.= 51 .29 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. e 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. -------------------------------------------------------------------------------- ABBREVIATIONS:-----.-- ----- -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 ---P_0 -----P.-- @-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 ._-__from _star_ting_Spr_.ink.ler_-to_Supply-__ --_-. "i_-- _-� point -fol"lowed by-subsequent Primary Paths. LEG ( pipe) TABLE: Describes ALL PIPES used in System Calculation . UL2 81?^ - - C, ine. - I rA Yf AQUADRO & CERRUTI, INC. Texas Road Northampton, Massachusetts Date DRAWINGS FOR APPROVAL JOB 17- C—L...v ,- TYPE OF 411K SUB-CONTRACTOR CaL�;:'- N45 iAota«-& DRAWINGS C2 DRAWINGS DATED STATUS LE- REMARKS: �j ,fit= ���Atz c tar-rz r� ,� A: Nl _f-aL2A\1<" k V, /SaT '�,ynR:L2►r.�lT� CO.Dm vF Z N� I�v ���c�ot--�:►c ;��t E�its,U •�r1 t�►��vldT�r►.� ����'>r' UADR CE TI, INC. By J Architect To Sub-Contractor