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25A-185 (18) 1 ' TF REFEREi CE LOSS/FT E FIT"rS FE F'E O_TOTAL C-FACT LT TOTAL_ P='F PO NOTES OU T LE'ii 34. 53 1 .45 C; i It 18.63 OUTLET 22 3.5.37 1 .637 0 12 , 55 ni ITI FT ?7r , , R2 1 4 C) 1 n PI1E »,' kt�a7 10 r t` m �s��?'`��...<.,�r z�..,.a�"'�,4:�::... �._;...W..��._.v�_� w......::_ �_:.�z �:,.� .���::.. .�-...z� r::+�.•� [� =:w �.:t k G.3'� =7:7� x;154 1 5.0 22..26 OUTLET .�q. �..a_ K=8 (). 15 i i 1' -0. 11. t),00 . 47 In () 1 R Q nn nL T � 1 Sy) jj i COOLER AREA 1 ?_ DENSITY OVER ENTIRE AREA - REFERENCE ASS T E - F!TTS V`PE PE C3KOTAL C--F"ACT LT TOTAL PF PO NOTES OUTLET 13 30.16 1 ,452 = 12.5 14.15 K=P 0,06 0 ij 0.00 0.00 -- --- OUTLET 14 31 . 52 1 .687 is 12.5 1.5. 52 PIPE 14 62.26 120 0 12.5 1 .32 15. 5 ni mi PT 19 .2 R3 0154 0 _R4 P�FE 1SY :1p�fiWool OUTLET ..16. :.:103 3.6?r 21154 .:_ 1. 5.0 17:71 K=8 x). 12 0 13 0.00 0.00 '-SIP 1 4 ��z 77 12C) r a 143.U ' -1-" -71 Z. ,.t�X,��y .f."C "t>?c`gx-> I pis ..a t REFERENCE, , *LOSSWT. :. E FITTS PE PE O--TOTAL C-FACT LT TOTAL PF F'O NOTES OUTLET 1? ^7. 1.X52 t y 12,5 y YnAj6V27 K=8 t :06 t) 0 -0.00 -- , - - `:. �,..,.,, _t __ 1 _, =-I - __ l� �_ -, , OUTLET 1 .637 0 12 . 5 17 - - .a PIPE 143 65.33 120 0 12. 5 1 .44 17.08 _.....--... ....__.._-- _ 8 PIPE 19 99.75 120 0 12. 5 0.96 18. 52 OUTLET tj 'S :; ) ; ^. 154 1 15.�) 19.47 ^ REF 905 21 .1C? + 74 OF 77 w~ ^O COOLER AREA .23 DENSITY OVER ENTIRE AREA - --- ROUTE NO. 2 DESCRIPTION --- ,,E=cnc/,CE Q-TOTAL C--FACT LT TOTAL PF PO NOTES OUTLET 5 29. 53 . 1 .452 O 12.5 13.62 K=8 0.05 0 0 0.00 0 .00 - ��� '- ^ ` ' OUTLET 6 30.26 ` 1.687 ' 0 12. 5 14.31 ,^ PIPE 6 59.79 120 0 12. 5 1 .22 14.31 OUTLET 1 5.0 16.34 voz DESCRTPTI ;0 LT TOTAL PF PO NOTES OUTLET 10 30.63 1 .687 0 12. 5 14.66 ' PIPE 10 60,53 120�`� `{ '� ''�0 12.5~`� �^�=1^'25� 14.66]\...�`� ` K=8 0.07 0 0 0.00 0.00 PIPE 11 92.44 120 0 12. 5 0.83 15.91 { REF 903 18�84 / , � 73 OF 77 � Q-ADD DIA T PIPE PT PV —REFERENCE Q-TOTAL C-FACT LT TOTAL PF PO NOTES ___________________________________________________________________________ rIrc 49 759.4" 120 . i. . . 0' 17 REF 925 21 . 16 6.357 1 30.0 77.36 0.018 0 90 12.80 _ p 2.12----' ----------------- ____________________7 --------------------------------------------------- ____ ___ _ _ �__ __________________ ________ _ ____________ R F q� " Q.00�� �� ^ 8'.-0c�- 1 4.0 , 92.29 ~ �- ` ' ^ - _ 0.006. _. _0 40_ - ._0-GO ___-_- _________-__________-______ PIPE 82 780 .64 120 0 44.0 0.24 ___________________________________________________________________________ PIPE 86 1280.64 140 0 75.0 0.28 REF 931 ono 9.970 1 15.0 103. 19 PIPE 89 1280.64 140 0 10.0 0 .02 - - --'103.51 Supply---- '� - _ -- + _._ OF REF 910 -30.85 4 .260 0 10.0 67. 14 0. 115 0 0 Q,0C? -_x_I •-'�_,.--.vim-- ���.!�a'----j.. �1------t-�---�-��} �--' _ FIEF 511 .� 27.79 4.260 0 10.0 6&29 F`IF`E 36 722.00 120 t_? 10.0 1.0S - F`IF'E 37 697.33 120 0 10.0 1 .01 F'TF'F ;R F:75.-p 1 ^C) -- ��F �r"I.4 18atat)< 2b if ,1C),0 F'IF`E 39 657=88 120 0 10.0 0.91 ---_-_-__--------------------------_----------------------------------------- --faE� , i A 1 7 F "g .. 4 6 C) CL- 1 ) t) 7 r^ya.t r "� T 3'f vu}' •�..7�' Y,{4 Y �c ..z7.. °� 7 REF 916 _...9.43 4.260 t_) 10.0 73. 11 0,085 0 0 0,00 g 2Yx t .yk.Y x•fi� s .a � �x z 'fitEfi 917 � �•,:� �i.z.�s�� C2 1� �:a 7� 9�, .< F'IF'E 42 636.73 120 i s 10.0 0.85 ?ter-- _ Q ABS F'IF`E 4 6.47.(_)1 n NAIM voln AO. 1 0.=C) REF r_':r 9 14.33 4.260 i 1 10.0 75.68 i rL 1. , REF 920 18. 59 6.357 i 10.0 76.6,C) PIPE 45 680.42 120 0 10.0 0. 14 ZZIE. t? t j c ' -0-10-0 i 7 1 tt F'IF'E 46 69911:5 120 ti 1'c),t,) V1 REF 922 19.48 6.357 0 10.0 76.88 0.015 0 0 0.6c) 7: 77777777-7-7 REF `923 20.01 6.357 t.) 10.0 77 a 0:7, - . p n i.r .t)I , r T l.) L.L.!U Cl 10.0 0. 16 � 71 OF 77 � COOLER AREA .23 DENSITY OVER ENTIRE AREA E N Q-ADD DIA T PIPE PT PV REFERENCE LOSS/FT E FITTS PE PE OUTLET 1 . 29.49 " IV452 0 12. 5 PIPE 1 29.49 120 0 12. 5 0.69 13. 59 ___________________________________________________________________________ --125----14�28- OUTLET _3 31 .49 2. 154 0 12. 5 15.49 K=8 0.06 0 0 0.00 0.00 VAT town 5 yy PIPE 4 ' 123.42 120 0 18.0 2.05 16.3L pop Cril- Z-260 rl REF 902 123.65~ 3.260 0 10.2 , 18.40. 0.054 0 0 -0. 11` -PIPE 31 372.34 120 0 10.2 1. 19 REF 905 135.06 3.260 0 10.2 21 .78 0.313 0 0 ---�)---�0.2- --'-3,21 -- --- - --- ----- '-- - ___________________________________________�-_______________________________ ^ ° ^ REF 906 144.47 3.260 0 10.2 24.88 PIPE 91 780.64 120 0 10.2 4.69 ________________ ----------------------------------------- ------- PIPE 02 7SOAKA120 1 11 .5 . 5.26 1 --------- � REF 908 0.00 4.260 0 97.0 34.83 0. 174 0 23 0.87 REF 004 0,00 41260 1 33.0 56.60 PIPE 34 780.64 120 4 118.0 14.67 ___________________________________________________________________________ 70 3F 77 --- PIPE TABLE --- FRICTION FRICTION VELOCITY PIPE NO. DIAMETER LENGTH FLOW GPM C LOSS/FOOT LOSS/TOTAL FEET/SECOND 56 040260 lb,00 A46.35 120" ' NOW" 0056 3.3 57 4.260 10.00 143.Yl 120 0.0054 �" 0106C 312 59 4.260 10.00 118.81 120 0.0038 0.038 2.7 60 4.260 10.00 100.22 120 0.0028 0.028 2.3 62 4.260 -40,00 , 61.73 120 . 0.0011 0.011 1 .4 63 4.210 16.00 41 .72 120 0.0006 0.006 0.9 65 1 .632 225.00 -jO.35 120 -0.0291 -6. 543 4. 5 66 1 .632 225.00 -27.79 120 -0.0240 -5.398 4.0 ,:6 77� V 68 S 69 .68 . rl: 00 00- -both, q., 5 5 -2 71 7. . 1 .682- .225.00 -9V43 120V . 10.0032 -0 731 1.4 72 1 .682 225.00 2.43 120 0.0003 6.060 - 0�4 -7 .61s,.097 w ;,v;,t,, 7 77 1 .682 225.00 19.48 120 0.0124 2.799 2.8 78 1 .682 225.00 20.01 120 0.0101 W39 2.9 79 1 APT QQq Qn- 170 - 57 ryU z U 4 1 60 -5 7go 83 7.980 133.00 760.64 140 t W044 ;0.535 ' 5.0 84 71.980 866.00 e73.86 140 0.0054 41691 5;6� - now-00---.4-06 86 -o9,970 =100 ( - 1250.44 1405 QW0037A 5-3, 87 : ,.10113 .00 42SO.64 12V 0.0046 5. 105 5. 1 89 11 .980 10.00 1280.64 140 0.0015 0.015 3.6, 90 3. 260 10.25 636. 17 120 0. 3133 3.211 24. 5 1 V 3.260- 40�25-----780.64 t` 30.0 92 3.260 11 . 50 780.64 120 0.4574 5.260 30.0 ^ �9 CF 77 � COOLER AREA .23 DENSITY OVER ENTIRE AREA � ------'��- --- PIPE TABLE --- _EB IIO -- PIPE mu u^ ` C � �.L091/Fuu! LuSS,Iiu|ALxFEE{ /SECUNU 1 - 1 .02 `�12.50 `, ' ~29.49 ` ` � -0.685 5.7 3 2. 154 12. 50 91 .21 120 0.0648 0.811 8.0 4 2. 154 18 .00 123. 52 120 0. 1136 2.045 10.9 l.0549 _'-__-l).687_'-_---___5.Z___-_-_--_ b 1 .687 I2. �� � 5� 7� 120 0 1 220 8 6 . `' . , - .`�^~"� � ' ^ . � ~ �' ' . 7 ` 2.154 - ^ 12.50' 91 .31` 120 0.0650 0.812- 8.0 9 1 . 452 12. 50 29.89 120 0.0562 0.702 5.8 10 1 .687 12. 50 60. 53 120 0.0998 1 .248 8.7 16 2. 154 18.00 128.77 120 0. 1227 2.209 ` 11 .3 9 lay" 21 1 .452 12. 50 34. 53 120 0.0734 0.917 6.7 22 1 .687 12. 50 69.90 120 0. 1303 1;629 10.0 Now 11 3.260 - 10.25 372.34 120 0. 1161 .192 3,2 3.260 10,25 501 . 11 120 0.2014 2.065 19.3 37 4. 260 10.00 697. 33 120 0. 1009 1 .009 15.7 38 4.260 10.00 675. 89 120 0.0952 0 .952 15.2 ---'39-- 40 �' ` 4.26W '10.00 � ^ ^643.72 '120 -0.0870 � ��0.870�`���,�^� ` 14.5 41 4.260 10.00 634.29 120 0.0847 0.847 � ^~` `� -14.3- ` ' 43 4.260 10 00 647 01 120 0 0878 0 878 14 6 } ^ ^ ^ ^ ^ ~ 44 ^ 4^260 10.00 661 .83 120 0.0916 0.916 14.9 ! 47 A V257 10.00 718.91 120 0.0152 - . 0. 152 �743 49 6.357 10.00 759.48 120 0.0168 0. 168 7.7 50 4.260 10.00 30.85 120 0.0003 0.003 0.7 - _.._ _. DENSITY COOLER AREA . 23 ;� • r r OUTLET # K -'FAC I.OR PRESSURE FLOW ELEV. (FEET) MIN. =LOi ---_--��___ L-u-LJiL,.F.-_.--__ � •':a-v,-Sidi--- ` 1 °Y 1.-__.___-.__.__.,_- � alt f _- _ 1�} -- __....-.__.-__.__..._ 2 S;tioo ! ii 14127S _ .2=: ti' 5ti 29.50 ' E3.t=}C}i i 15 a 495 'f. .49 2i_i. 5t:} 29. 50 S ' 1.3.62" 29i53 20.75 29. 50 6 S.000 14.309 30.26 20.75 29. 5(:'! S 8.000 16.341 :52.34 20.75 2-9.50 9 a.000 1.3.9x,1 29.8? 21 .00 2?e 5{=) 11 B.000 1 5.9?. 1 31 .91 _. �^2 1. .C`t='= 29. 50 _ 12 S.000 16.741 32.73.73 21 .tii) 29.50 lost ^;S , r�1 r^�ir`��ai s � F, f� (�.��} ''1 7.''7111. '' ••�»Fs7 .z .:�-►a ^.•+�i �� s ?` �g=�v�ty1��`�° �"`^ '` ` �''' 17 a.000 16.270. :1.2.27 ^1. 50, 29.50 18 8.000 17 a 079 ._,Tai)6 21.5{) 29.50• #9 R-t){tit_- #f `i#1 4 4^ '# `ii•} 21. B :t"?L?� 1�..{5-. � ""'� '�a :s 1. "'7'':5 f •. N �., ,.�, ��y z , � � ,, ��t ,: S.060 y 1 . 1.r 9 36.82 . 21 .75 29. 50 24 3.000 22.26 37.75 21.75 29. 50 - - , .s M * 17 REFERENCE LOSS/FT E F I T'i C PE PE Q--TOTAL C--FACT LT TOTAL PF PC, NOTES OUTLET 46 3 6.3 5 1 .687 C} 12. 5 -20. 52 . WS -•i_) 00 2 8 -0. 13 0.13 z RE= �. O 7 .:6.21 .i .637 t) 0.i; 20.- �iJTLET 4. _ 1 _ _ _ ',:J PIPE 56 29;82 120 0 10.0 0.27 20.49 ___--_--_...___-_.__._.--_._---_...-__--_--_-_.-__--_-----___-_.--_----._------.-----__--- -- ---= k:.-8 0. 12 0 0 2.26 M l l FIFE 57 66. 16 120 C} 10.0 1 . 18 20.63 -----------------------------------------------------�. CI!lTLETi 49 7Ea: 1.b87 , t# 172.�► 2 ^.'9b w k 8 t� "7 Awl S t# 7'4 ----_..-----.-----------------.,:._...- ------------------------------ -----------------.-_ FIEF C; 0.00 2. 154 1 26.0 73.23 C)S'2 i ! , t} c,+, tzm , .F z t" :i-.fi:,« i:3 a. `4+ •Ys^.. .G 3 b� f ��s ; y rh zJ�• �c Y?' *re .� , ^., -Z52 - 0.017 C) 54 9.87 Y FIFE 93 775.55 120 b 279.0 4.88 9 SK S ''Sa'S '^7i C#c f f S ,.. REF C# 100.00 T.980 1 60;0 0. 10 ri f4r'jZ 4' 64 r� 4}Sl- „ f'T'F'E' 95 BTSISS 1'40 1212400 t} X47 •7 9 - REF ii 4i��Es. 1��' 9.97C} C) ; .75.4} 9,45 ' ----fi�-�--t_. ---r--r----�.�.�-c:. _ '_ �:�^_ -r :. . •-fir_ F'IPE -98 1275. 55 120 i_# cvfm 5.25 INC 5 PSI FOR BFF 77 i C_}04 tl 0 01. )0 FIFE 99 1275. 55 140 [) 75,0 0.28 FIEF # , C;.C#i_} -111930 C? 10"O 105.26 1 -R!4'2 400 " 42-7-5 55 1.4#_x REF 105.27 M _. ROUTE NO. 7 DESCRIPTION —•--— `_ _—�____�_.._.___.^.---._— _ ZEFERENCE` LOSS/FT E FITTS PE PE :7. 04TOTAL C-FACT LT' TOTAL P1 PO NOTES OUTLET : 9 3:7.01 1 .6u 7 0 12.2 16.01 K=8 --0. 12 B —0. 13 1 .01 OUTLET 40 29.49 1 MS7 r 10:0 i .���, 7777 7777777— P I PE 43 --37.37 . 120 0 10.0 •-0.41 13. 58, W, Cr Cr Cr '' 44 k $ i i Cur Ct r OUTLET '42 2a.75 1 .6$7 t r 10.0 12.79 YO .<k sYs °Si'k'b Y{'gsti4v tir ,W «+ ni iTl FT 44 99 :—A I. AR7 (t LS-Z._Cr 17.1_'.;A, $ vm j r 11 y� ;" >� � .YT�L th acs, 3 ? " x . � x: �. t �t u '�'� ,.yc •- � s: f v. OUTLET .45 �' . c6r.95 1 .07 0 172. 17.23 --- K=8 '0.30 2 $ 0.74 —2.26 _ :. 21154 i 26.0 71,69 COCA COLA, ZONE 09, AREA #2, 0 .23 OPM/3000 SO F-F - FRO-t. _ 140. __ DESCRIPTION - ... REFERENCE OSSIFT, E FIT T 3 !"'E `E ------------ Q-TOTAL C�-FACT LT TOTAL F`F PO NOTES OUTLET 32 7.2.93 1 .687 0 11 .9 _ 16. 11 `K=9E -0. 12 2 8 70- 13 0.89 OUTLET 7.3 29. 5:7 1 .687 0 i o.0 1?. 53 PI PE (--) 38.29 120 0 10.0 •-0.43 13.65 ni ITI FT -74 ? _QCi 1 ASK i a 1 i" C) 1 ^ ag- to! TONS ,. - OUTLET" 35 `'28:80 "10687 0 10.0 12.8' K=8 0.01 0 C) -0.13' 0.13 F I PIE d is _12.. OL1TL•£T �5,-` " �8.'79` 1.b8? ' 'C�, 1 i•).c�) ;f 1 c.8� ` `• F' rPE 4= 46.25 120 0 10.0 0.66 12.95 OUTLET . 7 ''9 7 1 ,bP7 y to Cl 1 �� � x x ��� � L . OUTLET 36 ,.?0.94 1 .687 0 171 .9 17.22 K=8 0.29 2 8 0.74 --2.26 FIEF t a t_a.c:0 2. 154 1 26.0 70.89 PIPE 31 108. 56 120 0 41 .03 3.67 � 64 OF 77 ~ Q—ADD DIA T PIPE PT PV —REFcERENCE�----- --- ----------- —___--_--_'_—_ 0—TOTAL C—FACT LT TOTAL PF PO NOTES ___________________________________________________________________________ �O 64��`� ~`''' � u`00 `�''� � '` PIPE 95 ` 0.67 , , REF 0 —6. 18 7.980 1 760.0 94.78 ` 0.005 0 112 0.00 �—_____________—____ _ _ ____________ ~REF 0 '' 406. 18 � '"7.97(} ^ V 75,0 99.45 ' ^ ` ` PIPE 97 1275. 55 140 0 75.0 0.28 Qc PIPE 160 1275.55 140 0 10.0 0.02 Will � ` , � 63 OF 77 ~ --- ROUTE NO . 5 DESCRIPTION --- ' REFERENCE LOSS/FT E FITTS PE PE Q-TOTAL C-FACT LT TOTAL PF PO NOTES OUTLET 25 A6.45 =_ _--------------- __________________________________ OUTLET 26 29.82 1 .687 0 10.0 13.77 PIPE 33 -10.74 120 0 10.0 -0.04' 13.31 PIPE 36 76.83 120 . 0 10.0 1 55 13,64 MW 0.046 0 0 0.00 PIPE 64 454.23 120 0 12. 5 0. 57 2`/5 ^ ' ' 0.068 0 0 0 `00`-��'^r� ~ ___________________________________________________________________________ REF 908 109.34 4.260 0 12. 5 75.40 P I PE 66 672.13 � 0 .017 0 54 9.87 PIPE 93 775. 55 120 6 279.0 4.88 REF 200" . ___________________________________________________________________________ + 62 OF 77 ~ --- PIPE TABLE --- FRICTION FRICTION VELOCITY PIPE NO. DIAMETER LENGTH FLOW GPM C LOSS/FOOT LOSS/TOTAL FEET/SECOND 56 1 .687 10.00 29.82 120 0.0270 0.270 4.3 58 1 .687 180.46 103.42 120 , 0.2689 48. 530 14.8 59 41260 :10.00 68.91 120 0.0014 0,014 ITQ 61 4.260 10.00 206.89 120 0.0107 0. 107 4.7 62 4 . 260 10.00 276.33 120 0.0182 0. 182 6.2 17Q 0.01276 0.31ml 7_R cost Vill ERNE too 85 1 .6B7 9.71 68.92 120 0. 1269 1 .232 9.9 97 9.970 75.00 1275. 55 140 0.0037 0.277 4.63 98 10 .390 63.00 1275. 55 120 0.0040 5.253 101 7.9SO 1564.00 406. 1S 140 010013 � 06791 2.6 � 61 �F 77 ° COCA COLA, ZONE #q, AREA 42, 0.23 GPM/3000 SQ FT --- PIPE TABLE --- PIPE NO. -DIAMETER -.LENGTH FLOW GPM C :�LOSS/FOOT : ;LOSS/TOTALFEET,/SECOND 3 1 .687 21 .83 68.91 120 0. 1269 2.770 9.9 4 1 .687 12. 50 68.91 120 0. 1269 1 . 586 9 .9 7 1 :1687 219.87. . 68.C71 120 0. 12601 27.892 9.9 9 1 . 687 12. 50 68.92 12O 0. 1269 1 . 586 9.9 10 1 .687 22.04 68.92 120 0. 1269 2.797 9.9 15 1 .687 31 .00 69.07 120 0. 1274 3.950 9.9 16 1 .687 12. 50 69.07 120 0. 1274 1. 593 9.9 22 1 .687 31 .00 69.44 120 0.1287 3.9q0 10.0 ' . .` . 33 1 . 687 10.00 -10.74 120 -0.0041 -0.O41 1 . 5 34 1 .687 10.00 18.28 120 - 0.0109 0. 109 2 .6 ---�35'-- -10_00---'--�7"-.28- 120- 0.0632 -- -0.632- - - '6.8- - 36 _ `_�1 ,�^, 10 0 ` 76.83 1 0. 1552 1.552 11 .0 37 1 .687 179.67 107.91 120 ` 0.2909 52.268 15. 5 ' -�-2/}- 0. to6 5-13 2 5----- -- -- 39 1 .687 19.92 -67 .85 120 -0. 1233 -2.456 9.7 40 1 .687 10.00 -38.29 120 -0.0428 -0.428 5. 5 4^� 45 1 .687 179.92 108. 56 120 0.2942 52.931 15.6 46 1 .687 20 .00 -99.87 120 -0.2521 -5.041 14.3 _. .. OF COCA COLA, ...5NE AREA *2, 0.2 iPM 3000 SLR FT OUTLET # K-FACTOR PRESSURE FLOW ELEV. (FEET) MIN. FLOW 26 S,60 13.897 29.82 31 .29 22.75 27 8.000 13,308 MIS 31 .58 28.75 29 8.000 13. 140 29.00 32. 13 23.75 0 8.000 1 3.644 29. 55 32.42 28.75 $,tit]0 16.994 02.98 29,x° 28,75 33 B.000 - 13.652 29. 5 31 .29 28.....75 -15 t3. 000 '11,2,959 28.00 31 .87 28.75 36 8.000]00 1 '.. . v _ 28.79 32. 13 2 8. ."= 17-481 =9_77 ,^ .4" -rte 75 14. 54 _t-x:94 7.2.67 '?$.75 -- - S :.28,a 28.75 $C] Rr:''i 6 1 14 4 ^q_t►g '1 _'..aq alma 41 E3 e 000 13.049 28.90 31.58 28.75 42 8.000. 12.915 28.75 31.$.w. 28.75 . .44 E3�t�t���• �. .r4fx7 .'w.�,'>�b� 3fl� ''�`� 4 .2.4� �z��¢� ��,� $�7�,.�`'� � �� F, , s s 4ri $e`f3fl�> 14 969 ,t S'."95 3:..>�"` `b? -46 ai 47 B.i 0f) 20.486 7.6.2 1 =2. 1•? 28.75 48 e.600 20.627 36M 32.42 28.75 <. r $ � COCA @8LA Sheet No' -_E)rid Drawing, (Fin al)_ __-__ --___'---_____-__-___- -_- _ _ #1 #2 #3 04 #5 #6 #7 #69 206 v ��77007174117-#24 #25 #26 027 WS #70 276 Loop number 4 277 #62 3z' IMM38 100 v 100 67 38 9 20 49 78 109 109 #73 142 Loop number 7 563" 465- - 4 31 44 loot #8 O--<--O--<--O--<--O--<--O--<--O--<--O--<--O--<--O-- Supply ~- --__-' _-_- | nn = outlet 0 = junction -0 COCA COLA , ZONE #9 CALCULATIONS, AREA #2, 0.23/3000 w -----'--- -SEARGH--- - -- - ------ ---- --- - -- --'- --- - System has 30 heads on the branch lines. System has 9 branch lines. The heads are Spaced 10 feet apart,. The lines are spaced 12. 5 feet apart. The riser nlpplp,Ayqgth,ls,2.17 ,feet .,with. an 611 on top. There are 7 heads operating on the branch lines with _ a total of 25 heads operating . � Head K_factor used �is�8- -__--_-Branch-l'ir�e-�i~amete��_is�_1�/�B�-__'-__----_'-___-_-__' ___�____��---____- �-_--__'_-- Supply crossmain diameter is 4.26 Tie-in crossmain diameter is 3126 increase in friction loss thru- the grid :from the preced7' ing position . fps .77777777777 ` � 57 OF 77 * Q-ADD DIA T PIPE PT PV -REFERENCE' Q-TOTAL C-FACT LT TOTAL PF PO ___________________________________________________________________________ PIPE 56 19.SS 120 0 10.0 OUTLET 48 0.00 1 .687 0 10.0 39.86 K=0 0. 13 0 0 2.26 0.26 OUTLET 49 . 0.00 1 .687 -0 194,9 43242 PIPE 58 69.88 120 0 206.9 26.94 0.00 ------------------------------------_-------------------------------------- REF 0 643.26 6.357 0 225.0 71.64 0.015 0 54 9.87 I to Ott MIT T PIPE 94 713. 15 120 3 84.0 1 .26 1 0.005 0 02 0100 -7 V777 777777�-Vno. PIPE 97 1213. 15 140 0 75.0 0.25 ___________________________________________________________________________ - -'0 -2. 13.0....92.05 - - 0,004�'�/ 2 50 ��'-��/l.J0� - � PIPE � 98r 1?13. 15 120 0 63.0 5.23 INC 5 PSI FOR BFP ~ . - REF 0 0.00 9.970 0 75.0 98. 58 ` 0.003 0 0 0.00 ' PIPE 100 1213. 15 140 0 10.0 0.01 __________________________________________________________ . _________________ - � 56 OF 77 ~ COCA COLA, ZONE #9, AREA #l, 0.23 GPM/3000 SO FT --- ROUTE NO. 9 DESCRIPTION --- - 0-70M C-FACT M TOTAL "IF PO MOTES OUTLET 1 29.82 1 .687 0 27.0 15.36 K=7.607 0. 19 1 4 2.01 0.00 REF ___________________________________________________________________________ MP- REF : s65 Z67.OS 3.260 0 11 .2 06.66 PIPE 72 207.46 120 0 12. 5 0.49 ___________________________________________________________________________ ..0 . �- 12. 5 . - ' � ,� '.0 `- { � v- � - 0. PIPE 73 �. 19� � / 138.93 ' 12A 0 12. 5 0.23 REF 308 -69.04 3.260 0 12. 5 28.34 0.005 0 0 0.00 PIPE 92 69.88 120 0 13. 5 0. 54 ___________________________________________________________________________ PIPE 54 _QAS 120 0 76.4 9. 95 OUTLET 46 0.00 1 .687 0 12. 5 36.13 K=0 0. 13 2 8 -0. 13 0.31 5 OF 77 COCA COLA, ZONE E 19 4 AREA 01 , 0.23 =F't`•1/3000 SU FT ROUTE 140. 4 DESCRIPTION --- REFERENCE LOSS/FT E FI T TS F`E FEE Q—,gTAL C-•FACT LT; TOTAL FF F'Q : NOTES OUTLET 19 30. 52 1 .687 [? 12. 5 — 15.79 PZ 'C _=, --------------------------------.____--____---_ OUTLET 20 29.41 1 .687 0 14 .5 14.11 V=071607 . —02 F'IF'E 24 —27. 56 120 c i 22. 5 —0. 52 14.94 n1 ITI PT 19-70 i tiff; <�r —t - ;P'IFE ;. UUTLET P749:55 1`.07 0 12.5 13. 50 0.03 i t 0 —0.16 0. 15 tons .. r[ 151tl�} i F'IF'E y7 01 ,50 120 0 12. 5 1 .28 13.B8 —n1�. iP T 7A An 98 i 4�7 c.r�208-9 � Z Amm HIM `::.. ..:.. REF fir'; ' 0.00 1 ;687 1 1.7 66.06 0.219 0 --8 0.00 r REF 9i_r4 bv.i9 ~ 54 OF 77 ~ COCA COLA, ZONE #9, AREA #1 , 0 .23 GPM/3000 SO FT --- ROUTE NO. 3 DESCRIPTION --- C17TOTALYC4FACT LT TOTAL PF PO NOTES OUTLET 13 30. 14 1 .687 0 12.5 15.48 K=7.607 -0.09 0 0 -0.36 0.22 OUTLET 14 29.06 ��" IMS7 0 14.3 1005 PIPE 17 -26.61 120 0 22.3 -0.49 14.60 _-________ ---------------------------------------------------------------- WMN B 0.001 7r 7 REF- se"00010 Wasyl*&-ass wo � ' ^ ! - - i . - COCA COLA, ZONE #9, AREA #1 , t=:.^? 61 1 .`�;:i=ii-f 30,1 F r REFERENCE. :!. LOSS/FT E FITTS FE FE O—TOTAL C—FACT LT TOTAL PF FO10TES. OUTLET 7 29.92 1 .687 0 12.5 15,'5 . 1-7 FIFE ° —F,Ci i14 120 C) "7 OUTLET 8 28.86 1 687 0 14.0 1-41.94 — - — FIFE 10 —26. 1.8 .2"0 O ^.0 —t;'..47 14. _ . ni IT! PT 9 ^9 7-7 i Cl I ? k �I ^"`<�.,�,:.,:., � �•s ;���. �ti,��x,�s.3 PasC2,�A���" r t;s;e +\,y, Q ;l�'. ``` �' T yr\ a. s� ...,...�......;...:'i«•.a. +wags.... 'r: l,.w .«P...w,«—.....«:...:....r.,.«.:.5 ..y" .: ,„.. i OUTLET 10 29..;21 . 1::687: ' , ' ' . 12.5.' .- 13. 19' t_ K=8 0. 3` 0 0 -0.16 0. 15 ...r..s ` ,. ..� ,«.�, r <::.,r m$ w � �w;'a,. :?xq.,ea�wf cg v' a1 ee�b�C,t,.�.�y�..• »�£�3a� ��<,s �`fi°:j^.� Y.n:..r+.�5�v"S��'�v��SR'rn�,...��.ac'"S m'za,k�\, '�i�'ry„'�', ��,;�q� ^�, #« ,s.9+f�eR'�3�;�+4� ,,l. '£�>� - '�'�.♦r�'7 ��sn�.7T.:i,�u' ¢,�.a;yi' `t'�'�r, yn�F^k��`4F -'� �?x�s+ � �•�w:,1,.F ��v�-::�,a� �. �..e'r d V LE7' ��. w7•,w�ti:{ t?U -���'GS f a �J .L'v„y� �xw ,�. Y e's s i�9 s R'"5:: '�'�tt '�` 'C y �3� l ;., vZ d n PIPE 1.3 61 .89 120 t7 12.5 1 .,C, '7 z��'yy*'��``8 { /j s am fix'#} s .:yr.t....°h� 5 w? .G:(i'.�. ;`y J�*(,��►�r� <' ¢ 11 ?: :. _. 1"':.1�E 1`f l �r��2�.y q F� �1.?'� «$ ;�a# f 22�.V y 3^.1'L?:Y.�..3.,�,YnA}�?i �'�������`'3�>a '�yy�`j `'.�'+�,�• `�+�$��r`'�J9?3�)a,A R C 3. k ,m:n.... ... .: .. ... .n, £.,.. ..'swwif:ar.rsgr'wi,.:w �ad...c..wr».«w.�w.r'wi..r.a.�:rrw r.w.r..rxw..�:i,.n. •?'.. REF 0 :.0.c.>0, .. .1,�b87,;e . : .. 1 .... .::1:7 65 r 79 0.219 0 8 t_r.00 F;1 FE 73 '12.5€,.: 2c� 13 �� ;REF 67,.92 i ~ 52 OF 77 Q-ADD _DIA T PIPE P PV --RE]��RENCE------ G�---- Q-TOTAL C-FACT LT TOTAL PF PO NOTES ---------------------_-----------------------------------------_------------- REF 908 69.04 4.260 0 12.5 70. 56 0.087 0 0 0.00 REF 0 69188 — AMY : 0 225.0 71164 PIPE 93 713. 15 120 6 279.0 4. 18 ----------------------------_---------------------------------------------- ail M 0.005 0 64 0100 PIPE 96 826.85 140 3 S72.0 4;26 0. CRIME it 7777"7 7 PIPE 99 1213. 15 140 0 75.0 0.25 ___________________________________________________________________________ 0 - -' 0 0.00 ,�� � �/ ` ` PIPE 100 1213. 15 140 0 10.0 0.01 98.85 Supply 1213.w15jPWAYAILABLE AT 113.3 Pwo | ` ! � 51 OF 77 ° ~ --- ROUTE NO 1 DESCRIPTION --- � REFERENCE LOSS/FT E FITTS PE PE Q-TOTAL C-FACT LT TOTAL PF PO NOTES OUTLET 2 28.75 1'.687 0 13.8 13.93 K=8 0.00 0 0 -0'. 15 0. 15 PIPE 4 3.24 120 0 12.5 0.01 13.47 ___________________________________________________________________________ OUTLE- 0.009 Cl 0 0.0O PIPE 60 185. 19 120 0 10.0 0.09 ^ REF 904 92.48 4.260 0 1O.0 68. 19. ! 0.043 0 0 0.00 PIPE 63 437.28 120 0 11.3 0.48 .....................____________________________________________________________ � 50 OF 77 � --- PIPE TABLE --- FRICTION* FRICTION VELOCITY PIPE NO. DIAMETER LENGTH FLOW GPM C LOSS/FOOT LOSS/TOTAL FEET/SECOND 52 1 .6S7� � Awoo 69.04 120, ,071271 1127W 9.9- 69.04 MY Q. 1273 26.31K 9.9 55 1 .687 20.46 69.BB 120 0. 1302 2.664 10.0 56 1 .687 10.00 69.88 120 0. 1302 1 .302 10.0 58 7A .6S7 - 206IS7 69.SS 120 0. 1002 26.941 10.0 59 4.260 10.00 92.61 120 0.0024 0,020 2. 1 61 4.260 10.00 277.73 120 0.0184 0. 184 6.3 62 4.260 10.00 370.21 120 0.0313 0.313 8.3 ANIQlAvonlEv"if AT. 67 31260 10.00 34i69 120 0.0075 0.075 3.31 68 3.260 10.00 169.64 120 0.0272 0.272 ' 6;5 to 73 3.260 _ ~12. 50 _138.93 . 120 0.0188 0.235 ` `^�' 5.3 74 3.260 � � 12. 50 69.88 120 '- 0.0053 ~^^ ^ � 0.066 -' ` - ' 2.7 ^ ' 79 1 .607 4.71 67.08 120 0. 1207 1 . 172 9.6 so 2. 154 13. 54 68.41 -12W- -040381 6.0 85 1 .687 9. 71 -84.96 120 -0. 1869 -1 .815 12.2 86 1 .687 9.71 -85.82 120 -0. 1904 -1 .849 12.3 91 2. 154 13. 54 69.04 120 0.0387 0. 524 6. 1 / 92 2. 154 13. 54 69.88 120 0.0396 0. 536 6.2 P7Q 00 7 12 1611 KA. P 1025750 95 7,qSW: :12&pq S13115 14P 97 9.970 75.00 1213. 15 140 0.0034 0.252 5.0 98 10.390 63.00 1213. 15 120 0.0037 5.230 4.6 ` 9-970 15.00 1213. 35 140, cl,0034 o 100 11 .980 00.00 3S6.30 140 01 P012 74,164 2 5 r � 49 OF 77 + COCA COLA, ZONE #9, AREA #1 , 0.23 GPM/3000 SO FT - --- PIPE TABLE --- 84.69 n -120 � 0: 18501 5,760A§�71-12,2 4 1 .687 '12. 50 3.24 120 0.0004 0.006 0.5 1 .6s7 219.S3 92.61 120 0.2192 4p.191� 9 1 .687 12. 50 -55.04 120 -0.0837 -1 .046 7.9 10 1 .687 22.04 -26. 18 120 -0.0212 -0.467 3.8 15 11687 - 31100 05M -120 "411904 -5.903 ' 12.7, MIMS 21 . 1 .687 220.25 92,54 120 0.218? 46.218 13.3 OWN 33 1 .687 10. 00 68.41 120 0. 1252 1 .252 9.8 34 1 .687 10.00 68.41 120 0. 1252 1 .252 9.8 moo 68.41 120 0.1252 39 1 .687 19.92 68. 53 120 0. 1256 2. 502 9.8 40 1 .687 10.00 68. 53 120 0. 1256 1 .256 9.8 � 45 1 .687 206.33 68. 53 120 0. 1256 25.917 9.8 46 1 .687 46.42 69 .04 120 0. 1273 5.911 9.9 49 1 .687 10-00 69.64 0. 1273- 4B OF 77 COCA COLA, ZONE #9, AREA #1 , 0.23 OPM/3000 SO FT OUTLET 4-T K::--FACTOR PRESSURE FLOW ELEV. (FEET) MIN. r=LOW 0607 1412S6 20 4 R non aia t ''6 12L72126 -111 --L , ^f3.7 5 6.000 1?. 574 29.47 31 .96 23.75 6 8.000 14.715 0.69 32.0-r 28.75 7 7-607 0 Q W74 `^Q on - n c £3 7 'bia'7 14. 9 28 P 86 30.25 .:15 9 81000 13.474 29.37 31 .27 2S. i 5 11. t,'_anal_, 13. 5B2 29.43 __ .a6 28.75 8n7 i 12 3.iaia a 14.721 30.69 32. _. _ 28.75 1 " 7..r i7 1fe7()� an � 4. � 26.75 14 7 bt3? 149 I �9,t76t�t 15 8 bib :> 1�A -`67 �! `Il '%.�.1.P i`�."i .w�..I•.7 Yr:�.J'' a 5'� s X was 17 8.000 13.671' 29158 3106 '2S.75 18 3.000 14.805 3Q.78 32.-nom. 28.75 9 7 uti7 i 6 Uc?4 .�U 5? ?0 _ MEN #' /•` y J' < Y'k W ""}w.ac{ t '. Q � \`r<vx ;.ZiS �v•�Y�� � `b y•!,F '�k � �t Iii l,.� � J::417 �' I S �i}' ' Y '~ ►� ...f„rc�K� fi MXxF�r�'VF � }^���.. 2:3 BPt oo 13.876 29.80 T1 .96 28.75 ^4 8.00C-) 15 P t_O a 30.98 32.33-- _ ,28.75 k- f3 op I3�am ter 1 47 .0=120 Totals 6.67 • PTWAS F'-W 'K_7:607 ** ° COCA NOLA Sheet No . #1 #2 03 #4 #5 #6 #7 _#8 85 ^ 85 54 26 4 33 62 93 ^ 93 067 85 Loop number 1 93 #59 N<--- 256 - Loop number :7 278 #61 87 e7 56 27 3 32 62 93 9 73 ^ #70 343 Loop number 4 ' 371 #62 466 7 --7-7777777777 69 69 69 69 69 69 V9 69 69- 69 #73 13? Loop number 7 575 #65 WINway ALLOWS ^ O--<--O--<--O--<--O--<--O--<--O--<--O--<--O--<--O-- Supply ! | / J nn = outlet 0 = junction ~ COCA COLA, ZONE #9 CALCULATIONS , AREA #1 , 0.23/3000 ~ - REMOTE AREA SEARCH - 25-,heads-so- the -branch- lines.- - — .... �---------------- _' _ System has 9 branch lines. The supply main enters at loop 1 ds--are-��*ace par�,r---'------ ----------------'-- _--_ The lines are spaced 10 feet apart. Su pp l y ma i n s t ar t er p i ece is 2 f ee t long . C-factor is 120 a total of 24 heads operating . Minimum flow is 28.75 Branch line diameter is 1 .687 Tie-in crossmain diameter is 3.26 ing' position . I all MAMMA ' � 45 OF 77 � 0--ADD DIA T PIPE PT PV E- `FITTE, -PE- -__--_]�E_- '___---' __ _ --___--_ --'- Q-TOTAL C-FACT LT TOTAL PF PO NOTES ___________________________________________________________________________ 0. 110 0 55 2. 17 PIPE Aj � 1030.4 4 120 80.0 8.79 REF 0 100.00 7 .980 1 80.0 65.99 ' 0.005 O 95 0.00 PIPE 66 515.05 140 6 2872.0 5.85 ___________________________________________________________________________ we c if NEED PIPE , q9 1230.43 140 0 75.0 0.26 ` 44 OF 1 COCA COLA, ZONE S, 0.23/3000 --- ROUTE NO. 5 DEti CR I P f'I Ot•.1 REFERENCE ! LOSS/FT _ E FITTS PE FE C-TWAL C--FACT LT TOTAL PF POOP MOTES OUTLET 1 30.98 2. 154 C a 0. 5 15.00 _ - K=B 0.09 C) Ca 0.93 0.Cat_) PIPE 1 106 6_b9 120 t:a i� _5 �>s ate__ REF 0 MY- 1 15»98 OR7 PIPE 55 106.69 120 0 11 .7 1 .01 i) i is A. WAO is o T..., 777777777 qty t Uti) .� ti WON) t t)t) assa REF 302 107.62 31260 d 120 8 17. 1.T 0.042 i)4.'2 0 C) 0.00 nPTPT Al TIA Al ion T -2 MON -PIB,9 42 325-.40 120 i5 12.8 1 . 16 r s �.o £ y. ��� �' w•zt Lw7 i� �j%t�T� `, x s' tc > F` FE 4 19 L f a REM n305 ', _ 2-32 8�..•_ti.� ---N A60 '2bC)-; tj 1 12.5 60056 C) Ca 0100 REF ?C}b =-82. 1b` ut7 PIPE 45 168. 71 120 0 12. 5 0.34 '-' .2 r. t� ,3-t_)T�.tt----1, i-_---•-..:�1.-.-1.t.�r---- PIPE 46 > 85.43 120 f_a 12.5 O. ?.Ca REF 308 0.00 2. 154 3.2_ 21 . 15 ----------------------------- REF Ca' 0.00 2.237 0 387.3 21 . 55 PIPE 2 85.43 120 0 387.3 18.91 - 00 54 0.057 .0 2W . 0.00 PIPE 5K SIAY" :A20 " 0 23.2 1 1AW REF 0 645.01 4.260 0 4.8 42.13 0. 110 0 12 10.46 F - - COCA COLA, ZONE S., 0.'23/3000 R O U T E 4 O. D _S rr 1c'? I Ot :! --------- nI T- _ REFERENCE LOSS/FT „E FITTS E F O-..TOTAL; C–FACT LT: , TOTAL FF PO DOTES OUTLET 22 _ _ .81 2.227 0 10.0 17.:4 K=8 0.01 0 c, ---0. 12 0. 121 i)— 1s) C-1 OUTLET 2' ` 33.74'" 2`.2^7 t) 1s-i. ") 17.67 FIFE 27 59.76 120 C) 10.0 i).y'S ? 7.79 77-P. C) ":) FIEF 0 'C).00 ,- 2. 154 2 .3 2 38. 13 0.068 i y 20 0.00 PTP1z' ,.. firl, Q� "NL' t_t)--- : . 5$ . r, a e 1 � z { COCA C,CL._A., ZONE-- 8, ROUTE I'�18. � r�E.�.'+r�'{IF'T i ON[ ---' REFERENCE LOSS/FT. El' FZTTS PE PE U—TOTAL C—FACT LT TOTAL PF po NOTES OUTLET 1° ?11 .60 2. 154 i itz,0 1 ;.48 `- K=B —c--a.05 C) 1.ta —0» 12 C . 12 PIRF 18 ---7949 2:)—tl OUTLEET 16 30.4.7. 2„227 0 10.0 14. .::-5 PIPE 19 49.06 1120 0 10.o --0. 17 . 14.47 plIT! ET 17 Tta 2.2 7-7 is 10-0 14 (W-- _ 0 12. FiIFE 20 18 9 ,< 12th t-t 10 U t� , 14 18 OUTLET 18 29.96' 2.227 0 10.0 13.91 K:=B 0.00 0 i a 0.12 , t_r. 12 F'.IFF 91 11 -07% 1�?Q Sa ttr ca (7 01 14 () �- r�-'�r H+• i._ � -' >.,' K!.}, 4 `mow k '! CUTLET ._ 40.8-7. 1yea 0 10.0 0. 12 1•'.92 - F'IF'E ^^ ^_ ij �J - PZ 'E 7f2 � t7 is to tj: 4 1l «9� F OUTLET 21 30.09 2.227 i� :329.i a, 14.02 0»07, ca 0 1 .78' 0. 12 ; -_ RIFE "'4 lsSU 81 1^ a REF t3 t:},Cyr 2`.154 r' 2 "'7. 2 41 OF 77 COCA COLA, ZONE B, 0.23/3000 --- ROUTE NO. 2 DESCRIPTION RT--- REFERENCE LOSSMT V FITTY 'P& PE . Q--TOTAL C-FACT LT TOTAL PF PO NOTES ............. OUTLET 8 31 . 11 2. 154 i 10.0 15.0(--) K=&3 -0.05 0 10 -0. 12 0. 12 .776 51 , 12W ---------------- OUTLET 9 30.01 1 2.227 0. 10.0 PIPE 11 -46. 50 120 0 10.0 --0. 16 14.07 -------------------------- ------------------------------------------------- jtt jA 2127 Q---la 0 PIPE,P E' 1-:6 79 12 OUTLET 11 29.15 2.227 10. 52, K=8 &00 0 0 70112, OAK PTPP IN 1 2.7,4A .--1C3. . .... 'bU 4) T- TLE, ........................................... ..............0 ................... PIPE 14 42. 19 120 0 1010 0. 13 13. 54 ------------ --7-------7-7-----------7----77 ----------7---------7-------- -777-- , At AT A,Z ............ ............. ................. ::::.................... OUTLET 14 29.70 2.227 0. 329;01 K=8 0.07 0 0- 1 .7W 0. 12 REF 401154- PIPE 4B 101 .34 120 0 23.2 1 .87, ---------------------------------------------------------------------------- � 40 OF 77 ` � C-11-ADD DIA T PIPE PT PV --REFER -E-- -FITTS---- &E-- PE -----___-_-_-_-___-___-- -__-_ Q-TOTAL C-FACT LT TOTAL PF PO NOTES ___________________________________________________________________________ 0.068 p REF 907 83.28 4.260 0 12. 5 41 .63 0.087 0 0 0.00 . REF 8= PIPE 63 730.44 120 2 16.8 1 .84 REF 0 100.00 7.780 1 80.0 65�99 0.005 0 95 0.00 SAM PIPE 66 510.05 140 6 287 2.0 5.85 so REF 0 0:00 10.390 2 13.0 72.96 0.004 50 W 00 REF PIPE 69 1230.43 140 0 75.0 ON ___________________________________________________________________________ PIPE 70 1230.43 140 0 10.0 0.01 78.47 Supply OF _._._ ROUTE NO. 1_ DESCRIPTION - -- REFERENCE LOSS/FT E F I T S ' PE PF O--TOTAL. C-FACT LT TOTAL PF RD NOTES OUTLET 1 ` 0.48 2. 154 1 14.58 K=8 40105 0 10 -{x. 12 t). 12 - 'I ='�F----r--= -.�1.-.--7- :.- -ems} --•--i; -.pct_.:0._..--- :-'J' �i+ y-- "--�. n1„) OUTLET 2 29.B9 2.227 0 10.0 13.84 .PIPE --45 a 8?, 116 A 10"M ni{"1"i F T a 1xf1 Z . 1 7,_Sn K=8 -0.00 t; 0 -0. 12 0. 12 12 F'IF'E 4 -16.22 120 0 10.0 -0.02 13.69 Evil 99 C#l...r7LET 4 "?�i .44' .i `�Y•,7 i�) 1 t') 4.2 OUTLET , 5 29.33 2.227 t_) 10,0 13.32 16 12 x snow-1 .. PIPE �7 71 .83 120 t_) 10.0 0.35 1:=.45 OLJT#�E i ! .mow.T m sf T L s �: ti7 a b •:.. �9 �M _----t=.�-t... _ is .: .. <. .n "?'nti '"k'1 t.� •I !b f$ ft.:5'%< -i^N ..t.t `A 5> REF i) 0 00 2; 154 2 3;2 37.4 PIPE 47- 42C) t ? .: :8.1 PIPE t 12.8 t REF 902 101 .34 4.260 0 12.8 39.30 0.010 0 0 0100 _-�`I S`t� ''' .,_i i.�-S.c_1 -i--may__-___�_._{:•y____�.1_^e�:__..�.--(�}a.'�_. --__-.° _ REF 903 100.81 4.260 0 12.8 39.43 PIPE 35: 3 03.62 120 ,) 12.8 0.28 --,.f. ..F-- 4 i is1--�_�;T-p PI1'L' 36 397 .25 120 t' 12.6 tJ.`t L+ REF 905'' 82.32 4•.26C} t;) 12. 5 4O a 16 r .._..._-0-----�--z:�c ---A-63 a= �----. • - 8 OF 7 ___ F`IF'E TABLE _- FRICTION FRICTION VELOCITY F'IF'E NO. DIAMETER LENGTH FLOW GPM C LOSS/FOOT LOSS/TOTAL FEET/SECOND 52 ' 2. 154 23.20 82. 16 120 06524 " 412467 .7.2 5_: Z.�IPUA QTU20 83,28 120 55 2. 154 11 .67 106.69 120 0.0867 1 .011 9.4 56 2. 154 11 .67 -107 .62 120 __0.0881 -1 .028 9.5 57 J-40 # 1,67 -# 1 # _s .---52D. -s, C}pga 44, 9 F,' 58 2. 154 02120. -7,79 120 -&00W AQ,c os 7 59 21154 23.20 82.32 120 0.0536 1 .2 44 7.2 '?s`i Ci_t"?rt:'_i 1 ;�?+2 t 702LIVA 61 2. 154 23.20 83.28 120 0.0548 1.271 7.7, 62 2. 154 23.20 85 .43 120 0.0574 1 .333 7 . 5 20 srtrtQ 1 s{•�29 841 1 h. 64' "t' ' U�) C•J F!v�C). 7:?�.sJ.44 .1�„s'1 :..`J. 1',-+:"7 r79, y r 4 65 OWN. fps P 67 9.970) 7S.C)t) i2.rt).4. 14c') c),sit) iy.259 5.i 68 10.390 63.00 12-30.4.3 120 0.0035 5.236 4.7 r 9 97ttZ 75y CCU 1 ^ r yUsR�)t 1 n ^KA : 7£� �.y a�8t�r �.�.l.��� y .: .,�..'"�..>f j y�'�3,iK.Ln1 14c� 2 ?.V f)C}_,1 A' $ ,m �u��.�q',�Kc'�§*^rY���'�� .'J•ixaC'lt�=�7'� `"aF +�s.�b - 71. .! . ':� �` 37 OF COCA COLA, ZONE S, 0.23/300.) --- PIPE TABLE -•-- PIPE AM DTAMETEFR LENGTH F=LOW GF'M C OLOSSIF&V L$SWTOTAL F=EETISEC�31dD 1 :'. 154 0).5C1 1C�6a6 12C1 0)a0S67 t:r.0)4^ 64 -•, ��r'i�; � x 1_'4 t�t� ••-=F-rZ--��------,�-�1___':t3_.,»Ck1j. �..�_.�-I_.i.�f-° ------,��-7- ------- 3 2.227 101 A 00 -•45.82 120 -0.0154 -0. 154 3.8 4 2.227 10.00 --16.22 120 -0.0023 -0.023 1 .71 5 , V-227 x.1--.-4%1.) j 120 5 1 6 227 10.00 42.54 1201 0.013 s_I 1:x,4 51 7 21227 , 101001 71 .SS 126 t_I,t_>'515 C)..�55 ,.9 R 2-227 `;^��c`) )`. i t 1 A�3= ��;2s?���.t+?b1 i :22.A:a912--�__� 9 2. 154 0. 50 ' -107.62 120 --0.0881 -0.044 9„ 5 10 2. 154 • tl,t_i ) --76. 51 1 • tl --ij.c,•T68 -0.937 6.7 .. , 00 50 12-C,;:, .$-.-712 2 ,? 624` 1 4 014= � 1 r :1 i'r i? 15 2.227 10.001 71 .64 120 b.0353 . 53 5.9 16 2.227 329.00 101 .34 120 0.0670 22.006 8.3 T?�� i A Cz "i0 1 1 i 09 1''t) C) 09 4 ,s1 [r4Z 9.8 x > , I l :tLY1. 4 �aYS�h 79 4WE=t} _C3t trr yl�.Y 1YC2Ci 7Yt� :: � 2 1 A'27 101,cri7 -49atr6` 1�f_r -U.0ai.7 tr --------�'fr-=-----.....--.•"� �'�7 1-t L t rt:� -.,1 s��� i'`.t� -i) t a� ,tr a --t")_t"r'x�. 1 f,' - 21 2- .227 10 .00 11 .03 120 0.0011 0.011 0.9. 22 2.227 10.00�� 40.877 .120) 0.0125 i0. 125 .4 ---- 7--^ 0- :7 ---rwrn`a/ '--4L.a+if+.r"4-ft-�i ,.,�--+.•»_w.-..iw:.�....i.. . -+.....�....w., 9. Ct 1L? 81 1a t`31 '6� ^1R$2 oil 8Y no 7179TRY?fr f.. t r t�C t"r6 t= Y fr2, tr,6 AT T ^ �- ,.� T�----- Cr ti� 1 - 27 2.227 16:66 59.76 120 0.0252 '01.252 4.9 28 2.227- 329.0)0) 93.63 120 0.0579 19.034 7.7 .rs. .' 2 '7 307.33 - S2. 16 120 q,i?454 17.599 6,S WAS AS _1.2C1 0.0446 18.0144 &W 9 F3 L' _- 4 . 260 12. 75 101 . 49 120 0.036 .,y.. 34 4.260 1.,_. '5 202.82 120 0.0103 0. 131 4 .6 _ 2 .T l n 36 4 a.1.61.1 12.60 397 .25 i.::t? ij,i;i.3,5 6 0.449 4. 260 a.2.t%0 479. 57 1 x.11 0.0505 0.631 10.8 _----?t.t --°Y_�-..t¢`_;�1-- _.:a_:-v.�:i _.__.__%!.?.n:-re--_....._..-_�,y_,t�- �.i-..l:,+ist-f_iJ---'-`-._-t.1-.-$=���'-_ -_'-�.:....�-�•, i 4.260 12. 50 5.t»)1 tit 1 0.0873 1 .092 14. 5 40 3.260 12.75 .1f16 .69 120 0.0115 0. 141 4. 11 _-�*-*--- -�.,--�t_)----��7�--- --yam:4,.--_��---_�:�1---_[,1�-,:1?t.�_.,��---�-.-.,•-.r� 42 W260 12.75 325.40 020 0,0906 1 . 15bA , 01215 43 3.260 12.60 333. 19 1201 0.0947 1 . 193 1 2.8 45 3. 260� ,.�, .:� ., � =tt-) ,-;c�• -; -,'�-t.,i '+1�.� fa-.:�-�� t"� mac. ....,_._.-..-°T'S`Y-� fir"{•c-___.�x,t-m- _ ---E..�_ �_,rY�f --_-.1.-mr* -r>t...in s.r J ' 12. 50 168.71 2 9 6. 5 46 3.260 12. 50 85.43 120 0.0076 0.095 3.7 ,.-__-�-r-------__ YS-x-a-�z_' l'r-�.__'� ..fix-s.::��- �;_L)i v a'Y Z.�-_-_ _:�.-a•••l,.% .^vrrt -tee+-r^t{+.y � �c.+io � �t� -. 4S ^254 7 2' 20 101 .34 VIM "0,017SS 1 A 828 3.9 49 A. 154 23.20 100.e l 1:201 0 1 07SO ° 36 OF 77 ^ COCA COLA, ZONE 8, 0.23/3000 --- OUTLET TABLE --- '1 15 30 98 31 .25` � ` - 4 8.000 13. 542 29.44 32.08 29.33 5 8.000 13.437 29.33 32.36 29.33 )cl � � �� �L 10 8.000 13.789 29.71 31 .81 29.33 11 Ej.000 13.644 29. 55 32.08 ' 29.33 cost iv 16 8.000 14.472 30.43 , � ,` ^31, 53 -x �` ' ^ 29.33 ^ ' ^17 ' 8-000 14. 177 30.12 �31 .81' ` 29.3Z ' ' ` - to 22 E3.000 17.07 33.81 31 .25 29.33 ' 4-T tT? :fi ii' tP1 #7 #G7 1i)7 _.C)! Iv 4 -16 1.4 s4? 7�' #4(--) 1 Loop number 1 1=)2 #? •. #56 :)cr' ;: 1 ;}-. --i l __1 '- ; 1:7. --;14 <-------0. 448, 1 07 1i-)7 76 46 16 in 4'_t if) 1� 2 #41 21 L000 number ' CaL '# 4 #57 CJ----_____. _ 1v- >--16->-- -------0 #49 11 79 49 18 12 41 71 1 71 1 C)1 -304 3 #42 326 Loop number 'Y ##25 #26 #27 #'28 ____ ___ _____ Ca 0 #5 #58 ❑- #4.? _ 74 Loop n�.cnber 4 =98 #.Tb #^9 51 #44 251•L Loop number.. , �} A X•f .:Y #3 #bt7 0------ t_:;._-__ --------_----.•--_-----------•---------- ----•----0 #52 $ 8 L � yet4# .�1Y� l af,Kx�Y y a ooh? rTl4fal; r x E} 5shrk $ .xz r - - 0 84 84 ,._. 84 #46 86 Loop number 7 ••646 #39 #312 aQ Sb , See Below Supply 0. 0 _©- 0 _0 Q.i - 5t_tAF-`Y 731 7 ;1. 8 1 51 1231 1�?31 1^31 1231 p -4 reCi���__—._�.__ #nn ipe no, nn nn = outlet (I = j�-ir,_tion ° COCA COLA, ZONE 8, 0 .23/3000 ~ - RE>1OTE AREA SEARCH - _-heads-on-the.bran ch. lines.- System has 8 branch lines. The supply main enters at loop 7 The lines are spaced 12. 5 feet apart. Supply main starter piece is . 5 feet long . Tin-in main wharf er,placa,i s__�_ The riser nipple length is 2.2 feet with tee on top. a total of 24 heads operating . Minimum flow is 29.33 ' Pranch line diameter is 2.227 Tie-in crossmain diameter is 3.26 , UAW ing position . claim ONE- ` ` ' " I--ADD I;,I A T F'I PE PT F'',' --- Q--TOTAL- ACT LT TrJTAL_ F'F f'u ta8TE8�._ w. 0'.Cam _ () 10 0.00, PIPE 63 b-3.1 ) 120 . t) 12.^ FIEF ) 718.89 'u- .T57 0 34.8 75.91 � _ ().Ole a �7 11 .3^ --PYF—E ;4 7-g1 7 i,1 8 1 C} RE= 0 0. 6.357 1. 2 5. RE3. F'IF'E 75 781 .99 lit=; 90.0 1 .60 Fi�F tj 1=zZ f-1(-1 7 98(-} RO f) 91 Y'? 7t.+'7 179.0 04�6 FIEF 0 �164.25 7.930 J 185.0 92. 19 C).0 )4 t=) 197 0.i)C) IPE 7 71- -7,a 3fit, A _ ri P I PE 78 1281 .99 140 t o 75.0 t.). . 8 &I EF �) L.t 1 a-1 r,- 1Q(-1 '? 1� ("1 1f in �)� IFE 79 1 $1 :FLI ..L�FF' FIEF 0 Q.00 _. 9.970) 0 75.0 105,-. 0.C)04 C) t) 0.0f=) G'IG'S 8C) 12 1 .9 , 1ii,i) r,t 5 REF f) ti.c yC 11`.98f=y t:) 10.Q 105.61 F'IF'E 81 3.1- 1 .1719 1 4t A , _._ OF 77 COCA COLA, ZONE 55 0.23/3000 -- ROUTE NO. 5 DESCRIPTION _.-_ REFERENCE. LOSS/FT E FI'TT8 PE PE O-TOTAL C-FACT LT TOTAL Z. PF FO = MOTES OUTLET 1 0.44 1 .687 1 60.0 15.94 - ---- -_ - K=8 0.26 i s 8 0.00 0 --1 .46 RTEF 100-21 120 0 REF i_a 0.60 2. 154 1 2.2 31.43 0.078 C; - to t?¢_t;kt;.�_.._ _---- - W_._�.._.__�: �__. ._.___ F`IF'E 6.4 100.96 120 0 12.2 0.95 .-R EE- Ca 1 0.00 '�,�6 i� `t_k PIPE 45 45 1t«0WA6 12tk .:? 0 REF 302 101 .21 3.260 0 12.5 ' =4. 51 0.0318 t_a Ca 0.00 ;t F'IF'E 47 304.28 120 0 12.5 i oi_a �' a AT 'g TY -?An 0 { 1. ' AFL - r .t-M QR splo,TOOK wr"to REF 305 --60. 58 3.260 0 12;5 37.39 0.081 0 0 0.00 F ICE- 49 1j 56 1g 1^c:1 REF 306 760. 17 06 0 12.5 38,41 PIPE 50 246. 02 120 0 12. 5 0.63 F'IF'E 51 185.74 120 0 12.5 0.40 REF 308 -60.B4 3.260 C 12. 5 39.4S REF 309 " -61 .80 3.260 t a 12. 5 :9.68 --- Q.00 4t~ PIPE 53 63, 10 120 0 12.5 0,05 IzE� _ its 0 5 39-21 04033 0 10 1 .71 F'IF'E 73 _63. 10. 120 0 12.2 0.40 REF f; 0.00 1, .68 7 2 289.7 41 .84 0. 108 i; 16 0.72 1 _ c _ -__ O F COCA COLA, ZONE 5, o.23/---M0 -----------`-- -'---- fi O U T E NO. 4 DESCRIPTION REFERENCE LOSS/FT E FI T T5 PE PE O-TOTAL C-FACT LT TOTAL PF PO NOTES OUTLET 2:? =°.28 1 .687 i 1 tj,tJ 24.224 PI PE OUTLET 319.2 5 1 .687 i t 1.0.0 24.20 i PIPE 27 16.04 12�r t_r 1ir,c,; 0.09 2'4 (i7 PIPE 28 : 5.46 1��� . t°j 10 tr U 8� 24: 8 OUTLET 25 40.19 1,687 1 169.7 .28.41? .. K=8 o 25:- i t 8 C .00 -3. 17 4 2j L �rd s a PIPE 57 95.65 120 12.2 0,86 _._ t OF 7, COCA COLA, ZONE 5, ROUTE E t-%1O. DEBCR I PT I ON --- REFERENCE CE LUBS r F'i E F I T T 8 PE FE --TOTAL C--FACT LT TOTAL FF PO NOTES OUTLET 1.5 :7.0.65 1 .6e7 C, 1C).i:' 14.81 K=8 -0. 14 i s 0 0. 13 —o. 13 _ F-IE'L 1 R -71 4b :1 i) •�1! 14 /n OUTLET 16 29.34 1 .637, 0 10.0 J3.58 PIPE 19 —42. 12 120 fi 10.0 —0. 51 1.3.45 nt m FT 17 ^ i 10-0 FIFE ;'[) _ 1 zt? C 1 . [) OUTLET 18 28.97 1 .687 f_i 10.0 '13.?4 K=8 0.01 0 0 0. 13 —0. 1._, P T PE 21 9 ^o 0 f) O 3 }k h £,., } r.`!}N•'N � k i* k .t¢y r}iy 3'b \ d�• Z 5� NUTLET 1 9au 1°»fa87 J M n PI PE ^^ 44.97 12o y 0 10.0 0. 58 13.32 ; 15 f7 I t �� y ray zua s k2y�. ;sk s e OUTLET 21 31 .6: 1 .687 1 169.7. 18.78 K=8 0.^8 i 7 a 0,00 --..17 r +•° 7'7 St i titl REF t_r: 0_00 2„154 1 2.2 69.27 t_5—n—t_ � t c � . F . . COCA, COLA, ZONE 54 0.23130(--)C) ROUTE NO. 2 DESCRIPTION __.._. Q–ADD n T A - P!P E _ PT REFERENCE, LOSS/FT E F;ITTS PE PE GI–TOTAL. C–FACT LT TOTAL PF PO NOTES OUTLET 3 Tc_;.48 1 .667 n it ,0 14.65 K=8 -0. 13 i; t;; 0. 1.-; i,,;. 1 [OUTLET 1,.6£37 0 it_r.ti 1?..44 '' — — P I PE 11 41 . 5.3 120 ; 10.0 —0. 50 1-;a T, n! ITI FT 1 f; 2R 7R 1 -687 iL 10 L.Q �.J. '. { :. i ✓OFF 12 I LST 1iw t %; 1t; OUTLET 11 2S.84 1 .687 0 10.0 1 3. 12 — _ -, i ri cD 1 n- , -, - - OUTLCT PIPE 14 45. 16 1.20 0 10.0 0.58 13.21 at yL T _ F• C3 < 1. C ��ryy -� ti �.. i k PIPE i6, z OUTLET 14 X1 . 51 1.637 1 -169.7 18.68 K=8 0.28 G i 3 0.00 3. 17 ---8If°E 16 1i-�6. 1 12 �?- -7- ,7----. 5r -.46--_T_,.1.�51 REF t;; ;5.0(_-) 2.154 1. "2 69. 1 . F'i .106. �}! yo OF 87ADP ILIA T FIFE FT PV FITTS f Q--TOTAL C-FACT LT TOTAL f-'�= RO NOTES --..-.-t��E' L--__.�,�..Ci6___-_--.... ;-J'•-------4. 0.062 f) f) 0.00 FIFE 41 535:97 120 -0 12.5 0.77 REF 907 6 t=).27 4.260 t.' 12.5 72. 5(-.) '._____..............,.... -----�=�.��E•--'-_'�• '' `.�-ate-•- '�--_.--_-,-�.-.�.'.0 .tU- �.....�.. ..,�.f._._._.._..,.-..t.}.�=�.'�,...-. »,.w ._ ....._� REF 9oB 60.84 4.260 0 12. 5 73.45 FIFE 43 657.08 120 t; 12. 5 1 . 13 REF, t,) 63. 10 6.••T57 0 34.8 75.91 0.018 t.) 27 11 . 3...� of nag Xi 5:3 1 S >fi k I,r {p �5,i7 E38 2 FIFE 75 781 .99 120 0 90.0 1 .60 inn no I 7. r7'1 PO4A v o 95 A,t_yt_) FIFE 7b 881..99' 14t=) .: i7S:t) ti 96 .' r REF 0 -164.25 7.980 ? 1S25.0 . 92. 19 0.004 i_) 197 0.[;t) RE17 564.25 9.970 ' 0 75.0 99.80 11­0 04--____^0_____ _! _ _�____.t}.{_)t,). PIPE 73 1281 . 99 140 75.0 0.23, FIFE 79 1281 .99 120 0 63.0 5.26 I NC 5 PSI FOR BFF REF i;; t.),t=) i 9.970 0 75.0 105.33 0.004 _ 0 0.i it_; 75 REF t:; 0.00 11 .980 0 10.0 105.61 PIPE 81 12SI .99 140 0 10.0 - ~ ~ 27 OF 77 _-- ROUTE NO. 1 DESCRIPTION _-- REFERENCE LOSS/FT E FITTS PE PE Q-TOTAL C-FACT LT TOTAL PF PO NOTES 77_-_______ -_�__�__-___-_-_--_--___________---___-=-'= --_ _ OUTLET :' 1 ` 44;� ° 1.6 87 '`` 0 _ 10.0 14..60 ' K=8 -0, 13 . 0 0 0. 13 -0. 13 - ~ - ___________________________________________________________________________ OUTLET 2 29. 15 1 .687 0 10.0 13.40 PIPE 3 1 K=8 -0.01 0 0 0. 13 -0. 11 PIPE 4 -12.63 120 0 10.0 -0.05 ~2.91 _____ ol ---------------------- ------------------------------------------- -------- OUTLET 5 29.04 1 .687 0 10.0 13.30 PIPE 7 75.03 120 0 10.0 1 .49 13.89 bu 1477"7 50 W42. _____________________________________________________ REF 0 0.00 2. 154 1 2.2 69.09 0.003 0 0 0. 00 PIPE 36 106. 50 120 0 12. 5 0.04 REF 902 106. 51 4.260 0 12. 5 70. 18 -` ~~~. ___________________________________________________________________________ REF 903 106. 55 4.260 0 12. 5 70.32 � 0.039 0 0 0.00 ' PIPE 39 415.22 120 0 12. 5 0.48 REF 905 10.56 4.260 0 12. 5 71 . 10 ^ ___________________________________________________________________ ti 6 OF 7. ---- ;'I r E TABLE FRICTION E7 f-,,T CTID VEL�CTT`r' PIPE NO. DIAMETER LEND T-1 FLOW GPM C LOSS/FOOT LOSS/TO FA!_ FEET/SECOND Z'-2 6!..r___.-_1 2...-50-_...e1 BE[-_.'_4 ._ _._1.::!f_-__0-.Qz2 __. _��2�si(i� ---- --- '...L_--- - - --- 2bC) i 2. 5t:) 124.91 120 0.0154 0.'19' 4.8 5� 0 2'. 50 '" 1210 0.0044 0.054 2.4 < ��4 < � '��Lk 1^ '17 i i yb-•.5U__:___1�tJ_-___._�...5:2864__.y.�._�..i s:.k�.i __5'�4_------__...__. 55 2. 154 1-:1. 1-7 1`6. 51 120 Cr.t}864 1.051 C,.? 56 1 . 154 12. 17 1 :.6. 55 12T-:i 0.0864 1,t.i5'' 9.4 58 2. 154 12. 17 60.58 1201 (-).(:)3()4 0.370, 5.3 59 2.154 12. 17 60. 17 1.20 tY,etr.Vt:)Cr Ci._gib 5;3 't ti4 12- 1 f he n^-7 -12-r i) t i.,i r1__�_' 0..:.A,7 61 2. 154 1^. 17 c�Cr.84 12t:) C).C)•'C)7 Ci,?7? 5.4 62 2. 154 12. 17 61 .80 ti ","16 t i.Y84 .- .4 b 17 100.016 120 , . :? '-•101 .21 120 =0.0786 9 f,f} 17 Iry 67 2. 154 1'2. 17 -6.2.49 1.20 -0.0322 _0.392 5. 5 -68 2. 154 12. 17 60. 58 120 0.0:304 0.370 5."31 7ry 14 1 1.:17 60.27 1u�) tf c77�) za }`y r 71 2y154 i ;`1r' 84 1^23 C}kc� �y7 :n. r3Y4 . 72 x`54 1 17 ,1,f3) 7' 2. 154 12. 17 6'. 1 Ci 12 2) 0.C)X28 G.X 99 5.6 7.4 6.x.57 61 .75 781 .99 120 C,.0178 1 .096 7.9 b 397 7.(DCy -'8 i 9! j ?C) 76 7 9 i75.>_) r 831 .95? 1iJ s:),tC? ` �s4 7 77 7 98t) �} 'uf:}iy 717.74- 140 .. 79 10.390 63.00 1281 .99 120 Cr.0040 � 4.9 80' 9.970 75.00 1241 .99 !4Cr (--).00:7.7 0.279 5.- _ C)1 6 82 7.9 t? 7'.'()t:) 564.25 1' C) t:).Cry:��,2 7r .611 .6 25 OF 77 COCA COLA ZONE 5, 0.23/3000 PIPE .NO. DIAMETER ; LENGTH FLOW GPM C LOSSlF00T t OSS/�OTAL.;FEETISECOi�i� 1 14687 6S.60 100.16 1.20 1257 17.499 14.5 Z{l-- --- 120 132 61 �r.� - --4 T} J m 1 .697 1.i_a.00 --41. .?7 120 i' .0 4 _ _ .. 9 -i_a.494 50 4 1 .6B7 10.00 -12.63 120 -0.0055 -0.055 1 ,8 _ 6 i 687 O.00 45.2 120 c),ti �8 ?. 58 b.5 7 1.6S7 A0.00 o75.03 12 0 0.1485 114M AN.S _- R 1 _AR7 ±1 1 77 br !/= 52 120 __1.2 TR32 5{a_447 11. 9 1 .687 68.00 -101 .21 120 -0.2584 -17. 56?? 1 4.. 5 10 1 .6P7 10.00 -70.72 120 -0 . 1331 -1.331 10.E 11 1 687 1cl s'at:3 --41 3, 12n. 4n,ag,7 -c'a 497 1, t a lw� 1 .687 it)p`?i) i6.t?9 1qp t? 0056 W 15 - 1 .687 10.00 75.01 120 0. 1484 1.45%+ 1 0.8 16 1 .687 177.67 106. 51 51 120 0.2840 5i_f.45}6 15. _ 487 AM nn 4a., 1�o- ''br'f ,�.f � i (�)0 �7' � YOM 't y 1. 4ae7 1!rl 'UG -i ?Ct _ 1._s a Ca_-t=TUa`a -i7 i-Lad L.S' 21 1 .687 10.00 15.77 120 0.00S:' 0.083 2.3 22 1 .6e7 10.00 44.97 120 0.0576 0. 576 6. 5 rt V .�� -� 1,'_}�j�_t -1-�{•.r-o 1,..;r.(wi_-_,f.-».-_} 1 y..�-�."_' _^__-^'.�.�,.�.n •e!„y��_ 5 : 1:6£37 9S.Ca{� 6 .4 ? i.?(? c)p It 59 . . _7 1t=3 z 6 - 1 a bS7 eta,.fats ���tr •-1��:3 -�i�-a-?-b9 �._xj.1F.:� ��:.-. 27 1 .687 10.00 16.04 120 0.0086 0.086 2.3 28 1 .07 10.00.t=ai? 55.46 120 0.0849 0.849 8,i? cm-i 30 1 n 687 105 167 60. 5S 120 0. 1000 30.560 8.7 31 1 ,687 05.67 60. 17 1..�0 0.07B7 30 n 17�" S.6 - Cl :33 1 .687 305.67 60.84 120 0. 1009 30.802 8.7 1 .6S7 305.67 s 8 0 120 i:+, 1+:•+.` ="< 7 1 3 cam? _. •_ _ ... -.:3x-_�.-z w a .z+_-. ._-S..:c:..a __---ii x _:._r 6-- _.r. } 36 4,260, 1^.50 106. 50 120 0.0031 0.039 2.4 '! 4.260, 1_ n i_ 213.02 i 2. : " i 1, i_a. 141 4.'C' �W-c.'i e x_f_?(_.- 3-:s-x--��-:•-..._----c'�-!-rvt.;7_____.__ �.�{;F--�{3 x.(.yl:,_�a-----__ _f:T-a�� .�?----------"-7 T.,::----_,____.__.�_ 9 4 .260 1 2. 5i? 415.22 120 i? i s.1 387 0.483 9.3 40 4.260 1 C. 50 4.75.80 120 0.0497 t i,622 10. _*1 ;. 42 4.260 12. 50 596.24 120 0.0755 0.944 13.4 43 4.260 12. 50 a 65 7.08 120 0,i x904 ' 1 n'1 _.0 14.8 45 3.260 12. 50 1.00.9+6 120 0.0104 0. 100 3.9 46 3.260 12. 50 202. 17 120 0.0376 t a a 4;0 7.E: 7_•� -.• n - .-� _ 1.20__ -i=i,�ir?0t?__ _.. _--- 4a 3.260 0 1..:.;_}(_a 366.77 120 0. 1131 1 .414 14.1 3.260 12.50 306. 19 120 0.0810 1 .012 11 .S 00 4.260 0-2-- go �i!n n(a3 l i t.3�_.._.(a�t 3--:4 i _._°-- -^+ ,�_?.• �___ �__�i_ ��___ --_.._- 24 Of 77 COCA COLA, ZONE 5l 0.2313000 - OUTLET ## K ACTOR PRESSURE FLOW ELEV. (FEET) MIN. F LOW 14 -47A E1 it L.._k 3- ' j l!4 no 2 ; s 'pop is.278 29. 15 37.7 5 28.75 t� 8 00 12.410 28.74 37.46 28.75 4 8 Son 17-'9AT 28_-8Q 27:20 HOW 5 8.000 13. 176 29.04 36.92 2:8.75 6 8.000 13.886 29.8:1 36.u3 28. . L p-000 15 Apo 71 ,4B My TV .2 8.75 8 ' 8-00 144520 0148 38.04 28.75 9 8 '000 1 r 315 29. 19 :37.75 28.75 11 B.Cain_) 12.996 28.84 37.21 28.75 12 8.000 1 ..208 29.07 36.92 28.75 14 8 cat)i? 15 1501 31 .5 ri i 5 8 'Cic_aC) 14.682 ;)..'b5 ti8.i�4' ASPHAV 1b fit 't5[aia i"� i ^9_SA LL "e.m 17 8.000)00 1.3.066 28.92 37.46 29.75 18 6.000 13. 115 28.97 37.21 23.75 2t 8„Catai3.., 14:f?28 29.96 36.13 28.75 21 B .Cat�C� 15.Ea18 31 .62 003 28.`75 23 8.0 00 24.067 39.25 36.92 28.75 24 6.000 24.281 39.42 36.63 28.75 COCA COLA Sheet Nor . uee Below 8LApply #35 4' 64 V 64 64 #53 64 Loop number 719/ #44 V #•_4 #522 125 Loop number 8 658 #43 V #33 _ V N 61 V 61 V 61 #51 186 Loop number- 7 597 #42 ? V #•=^ —_ V 61 V 61 V 61 #5C) ^47 Loop number` 6 536 #41 •.: V #.'1 V 61 V 61 V 61 #49 T0 7 Loop n_imber 5 476 #40 V 61 V 61 VV 61 -- #4} ,67µ � Leo pumberr 4 !_ "4 "# ,` V #25 91156 #.r7 #i..3 #2 Y #61 7-_____ _-. �'�'� -, -^' '_ -4_.;.:_-{c ;____ ____ _ _------. _ _ __._ ,#iii;' _ .72 V 62 27, 17 56 Gib V 26 #47 ti�)5 Loop n�imber` y r} # .�S --1 - 1 -i8- -i9-- - 'c} -^1- - =0 #5L r� ' 1012 V 102 71 42 13 16 45 75 107 #46 2 i)4 Loop number ^14 #37 V *•9 #1 (-) ##11 #1 ? _ #14 #15 #16 V #65 0-----_- -O #55 c_)1. V 1f?1 7�i EF1' 17 46 76 107 107 #45_ :-.101 p—auuttbr=s 1 i 07 # ;t} 4 - 1 i i ! r; '' �' j , i -_,'��_—_i_)-.'�_ `•_i j i'l --__�_.__'_'_LI.__ #74 #75 t!'6 #T7 #7 8 #79 #80 #�`.3 *nn "-#•)'-per nn no z n p m filovr•;nn_ r!irpr=rirJl� nn = oi. tl.et n = j).tr'IC IJ_on Ib COCA COLA, ZONE 5, 0.23/3000 - — -EMOTE AREA SF.-CH____ -� -- _------------ System has 0 heads on the branch lines. System has 1y branch lines. --- — S The heads are spaced 10 feet apart. The lines are spaced 12. 5 feet apart. i'1'1 pep Is= 1 P fn 1 i_ _.' j,fR P t Lsl 3 t h ti-�__�tC1 . ' �--factor its ..12�J There are 7 heads operating ,on the branch lines with Minimum flow is 28.75 Head K-factor used is 8 Branch line diameter is 1 .687 Supply crossma n diameter is 4.26 The positions shown below represent the position of the fir t head in the��p�a�ing_area_ The figures to` the right of each position ' represent the incre se in. fa ction loss thru the grid -from the`; preced- i ng Position. -- --- Position 2 11171875 Position _. 0.967693 i on 4 0.7Qjjj6,, Pos . 1-•inn 5 0. M71 Q77- Fosit.ion .::b '< W7077.<? F`osition 7 Ci.184bt.7W F'casition 8 -t�,c�ti`j8�i 21 OF 77 Q-ADD °:DIA T F'IF'E PT ' Pv ---REFS-RE-t4C-E L-CISS/r-T------E---FITTS--._._�_ O-TOTAL C-FACT LT TOTAL F'F PO NOTES 000 l t 3 °197 i_).oo ; F'IF`E 56 b 2=22.0 U>f)b 5El= i) 51 .27 9.970 0 75.0 113.99 0.000 ) i s 0.00 -----FIRE 57 1 i;it r';r°; 1 ZL fD �:� S.S:1_ o s 70 REF 0 0.00 10.390 2 13.0 114.00 F'IF'E 48 100.00 120 2 6- .0 5.00 INC ,_ PSI FOR DFP F`IF'E 59 IOOTOOQMWT 0 7 5.0 FIEF- 0 0.00 11 .980 t_: 1t).c_a 119.00 0.iji"'ri_; 0 ti a.00 60 1 r;s z z! 140 �'� i Q REF t r 119,00 i x O.= COCA COLA SOUTH AREA STANDPIPE, ( 1 ) AT 100 GPM AT 65 PSI ROUTE NO. 5 DESCRIPTION --- REFERENCE. LC1pS/F T E P I T TS T L_ C- TC}TAL< FACE" ""T tJTAL NOTES t 2 OUTLET 1 100.00 2.067 _ 37 . 5 96.26 K=9.628 0.05 0 .11 4.41 11 .61 -PIPE 1 8 4 1201, t.;?_.__ S. __ ^ Z4,7 _. _. REF 0 t-},0 #; 2;667 t 2.2 1=93 PIPE 47 63.44 1211 0 12.2 0. 57 .2A1) C} 1 ^ s? 1 (}- _4c?. FIFE & fs8 44' 12C} �� 1 8 TWA, ;mss REF :7.02 -13.12 4.260 0 12.8 163.51 0.001 0 0 0.t_}ti :7 ? 1?c) cl 1 ^ 8 NEW w PIPE 8; 41:22 120 0 12.8 0.01 a , PI�� t9 7W r a a 1 t? 1 6 CO - - 0 X 9 .:,.._.:.r....u»:....wwr.r:«wi:iGww.«i..:«www'+w+vwwar'«»aw:w«w.i:'iw.u...r.«+i:'ur»..w w....:«.w.«_..wnw+w •; 4 : k ...^ .; .;,.•: REF 305 A3.7-2 4.261=1 0 12. 5 _ 1t-)' 5•R 0.t)0 } 0 C} 0.00 REF 00000#:#. > #< ,C)67 '. Z 2 1o•4.54 PIPE 52 13.92 120 0 23.2 0.06 9;002 0 0 4.41 PIPE 30 13.92 120 0 487.3 0. REF 0 0.00 2.067 2 _ 104.42 . 0.002 i_i 20 0.00 - ICE •. n^ 1 >REF C) ` 86.O 4.260 , 0 9.8 ' 104.48 PIPE 53 100.00 120 2 21 .8 t i.06, PEE1} cj }.)U 4 '2 6.C.;-__--1.__ : } _ 11 1 1 - - -- -- __-� --------- ---- C}a 003 55 2- 17- PIPE 54 100.W 129 0 80.0 REF t_i 0.00 7.980 1 8t i.i i 113.92 0.000 0 95 Ci 00 _.. . OF . G--AlJD DIA T F'IFE PT PV , --REFERENCE !USS FT - E 1_:—i O T AL C-FACT LT TOTAL_ PF PO NOTES ,6 EE 't] 1 `� r "" Ct 9_S i r-4_ 119 0 12 6.99 P I pt 53.; 1 o },t_>o'! 12C} 2 21A S 6.t_}6 REF i s 0.00}Q 4.260 1 25.0 111.53 0.003 0 55 2. 17 PIPE 00 0 TV REF 0 Ct,O 100 7,9801 swo 11'.9^ --a9-59— F'IF'E 55 100.00 140 2 175.0 0.02 IBM MIN �a REF 0 . 51.27 9,970 0 75.0 113.99 0.00t_} t_} i} 0.s.}t> P I K E 1 t a f-1 t}.t,} 1 Ai-I C) 75 x OR s 1,14 0 t} F'IF'E 58 100.00 116 2 63.0 5.00 INC `} PSI FOR EFP REF t.} 0.00 11.9so U 10.0 119.00 inn nn lttrt to 119,00 Supply 100 0 OPM AVAILABLE AT 124.9 PSI 18 OF 77 • ---- ROUTE NO. 1 DESCRIPTION --- REFERENCE LOSS/FT E FITTS PE PE Q-•-TOTAL C-FACT LT TOTAL. PF PO NOTES OUTLET 1 1004OO 2.227 0 2.2 96.26 10112 11 ;61 OUTLET 2 0.00 2.227 i} 10.0 96. 16 K=Q tom,t)1 r L) PIPE W ?1. .56 12ta 0 10.0 ; 0.08 - 0„Oct K=O 0.01 0 i s -0. 12 0.00 PIPE 4 31 . 56 1210 p 10.0 0.06 0.00 OUTLET 5 0.00 2.227 0 10.0 96.03 k' o� L C�, C) p t) tr)L} vim K=O 0101 0 t) -10.12 0.00 PIPE 7 31 . 56 120 U 10.0 0.08 0,00 -- - -- _ - -- - - - - - - -- - - - OUTLLT 7a t1C>` 2.227 c7 97 7,W '. 9 .94 lei =t� t .C)1 is fj 5 1 ta,seta FIEF t:) 0.00. 2.067 2 3.2 104.15 oo_ 0 PO WIPE PIPE 31 31 . 56 120 0 12.8 0.00 REF. 902 1:3.62 4.269 0 12.8 104.41 PIPE x� 4 �.1i3 1?it fJ I� t o t}i _ - REF 903 13.60 4.260 0 12.8 104.42 PIPE 35 5 3.70 120 t.) 12.B Z 0:61 c?t") S '71 0 _l^_.6____!_J_'4 4Z 0.002 0 f} t).f_o PIPE 34 72.36 120 0 12.6 0.02 REF 905 13.72 4.260 0 :1:2. 5 104.45 002 0 6:66 -ibis .a ,.,1.`...s.� tJ 12 ..,.ter:.. OF --_- PIPE TABLE --- FRICTION FRICTION VELOCITY PIPE NO. DIFit€ETER LENGTH FLOW GPM C LOSS FOOT L88S/TOTAL.. FEET/SECOND N 52 13.92 120 0.0024 0.057 057 1 ,- 53 4 Q60 . 21 .-75 100.00 120 C>>�'028 0.060 2.3 s.z� Ito -____t __o_oo2° _o ^^ 2 55 7.980 175.00 100.00 3.00 1 40 0.0001 0.017 0.6 56 7.980 2322.00 48.73 140 0.0000 C,,060 0.31 - 57 58 10 01.0w. , 100,00, 120 0.0000 5.002 0.4 J9 " 9.970 75100 100.00 140 0u0000 0002 0.4 hip 61 7.980 2_L 14. 0 51 .27 140 0.0000 0.060 0.3 4, .. MONO ...2:. 3 :_ a... - t � s , y 1 16 OF 77 --- PIPE TABLE --- FRICTION i'R I L_ t S O t`I VELOCITY PIPE NO. DIAMETER LENGTH FLOW GPM C LOSS/FOOT LOSS/TOTAL FEET/SECOND 2 2,227 o 20 131 . 56 120 010077 0.017 2«6 2«22 7 1.t7 00 ;1,16 120 C#b 0910 #.t?77; 2.6 1.�3 i✓Z[} "•y1._._56` 1"Ca��"�..t�t'�Z� ..s'i..S#77 ^_�, 5 2.227 i i_.oo 31 . 56 120 0.0077 0.077 2.6 6 2.227 10.00 x'1 . 56 120 0.0077 0.077 2.6 Z 2 211 10.CID 51 _ 9A S �,2 .:�97«66 41 .56' 120 �#,i-airt77 b ta77: .'.6 9 2.067 ,iOO •13.62 120 0.0024 0.00W 1. 9 t-} 2.227, 19,67 11.62 120. 0b0016 t� sari 1 1 11. 2.227 10.00 13.62 120 0.0016 0.016 1 . 1 12 2.227 10.00 13.62 120 0.0016 0.01 1 1 . 1 1 �? •, '777 10.00 im, )• �''_ _ _ - - ll t) t) trt n 19,t1sa 1. 62 1: �� t316 LaZ 1 ( y 4 y { .: �k.�b�� S ' 17 2.067 1 .00 _ 13.60 120 : 0;0023 s a,is 02 1 is 2.227 19.67 13.60 120 0.0016 0.032 1 .1 .L _ ,,- ,y 0- 14 to �t}� • �i-y1 '7•.-..t. : -�.G.►y.,L7 ^4_ 2.227 10.00 1 ti 60 120 0.0016 0.016 16 1 24 2.227 42S.33 13.60 120 0,0016 i a.69S 2 010016 1 _ - i7 -. �•.w m�».Fh+ : �ta a'�..}�a .lL wt s+. 7 .i..w..f fix tA'.r'A.a V¢Gix �l si��� : «�s..7w ` > k r., ' :5 29 2.227 =7131 13.72 120 0,0011 %t'a,S07 1. 1 30 2.227 487.33 13.92 120 0.0017 0.029 1:1 1 Q ^�tl 1 ^.• 7 i 1 Ai�7 '1) t) C)i}t) `) C)f)A L 7 32 4.2tata 12. 5 45. 1 1i=# fa,taCra6 ?. #�aB' 1 ,Ca _� y.� �•.,�; .�.-, +sC�r) 7'� p;,� �„,�.t) t)t)S„#.1„�3-----... -.1.L.[-)1 q t f� -...__.....___._ 35 4.260 - . L50 86.08 120 0.0021 0021 t_a.t}26 1 .9 36 4.260 12. 5 6E.44 120 0.0014 0.018 1 . 5 1....___ �•Y�'•tt3l�- E :..v^-.�-c:v --s•1'S• 4':7 z...-..__--�a..l)_.�_l„ )•.J y. }_/ �_�_-_-S..j- wy.._ ___ ' ---38 4,260 12.75 41 «2 120 0.0005- 0,007 0.9 39 4.260 12«60 27.63 12;a 0.0003 M003:x03 t-r.6 «92___- •1w})- ---- 41 2.067 27.20 31 « 56 120 0«0111 0«258 3.0 42 2.067 ,- .^t_) 13.62 120 0.0024 0.055 _ . _ 44 2.067 y 2i) 1 1,59 120 0,0023 1 « 45 2.067 , .. :�t,a 13 .72 120 0.0024 t_a.055 1 . __o 47 2.067 12.20 68«44 120 0.0466 0. 56B 6. 5 48 2.067 11 .20 13.12 120 0.0024 0.026 50 1 . _ C.o i;:.�• 11 ~.?;"} 1 -._ 4f) i ^.•t-i __1i..�S.a.�.':+_.__ �> !�L�i:L .__.���-- ----- - 50 2 067 ^c`a 2. « 59 120 V,fa023 0 X54 1 .3 15 OF 77 COCA COLA SOUTH Ar tEA S 1"ANDP I r'E,, ( ) AT ii:0 GPM AT 65 PSI -- - -- OUTLET TABLE __- OUTLET 4:-FACTOR PRESSURE FL0-V! ELEV. (FEET) MIN. FLOW 9.620 ti 1{}i fir 4. 5" Iii Z,00 Di zmatar = J .A'1 0 T 0=1 im=x t l 't OQr PTt69 ; i,���y.= 1 r 7.0 i Loss / f _.— 0.= 1: E1 , =4 F PF=42 .S. C=120 Total=%135.00 F =r 1s};.8? K 9.6^O < k '^ £a s s a '2 i yam., hZ 2^a• `i _.. 3 r z a COCA COLA SOUTF4 AREA STANDPIPE She=t No Be- Below - Supply v 4 V 14 _ #40 14 Loop number: 5 87 #35 V # 9 V #51 ------------------------------------ 14 V 14 V 14 #39 28 Loop number 4 73 #34 V #25 #26 #27 s. ��.._ 4' N 14 V 14 14 14 14 V 14 , #3t3 4^ Loop :number _ _.�__ 59 #33 _ V #17 #13 #19 #2Ca #21 #2^ # #'7��?• V #49 ------8 #43 14 V 14 14 14 14 14 14 14 14 V 14 #:7.7 �5 Loop number, 46 '# ^ V #9 #12 #15 #ib #48ii, 0 -tilt. --t 9- _1 ) -11� '---1 - - ., 14 V 14 14 14 14 14 14 14 14 V 14 #36 69 Loop number 1 32 #31 V #1 #2 #31 #4 # #7 47 a t _ �?_ : t 6 r) 69 69 t_) :' () .�ryr t) :•� t),: +'�' ; r'' j .' t �w*i3ws > it � ti #53 #54 #55 #56 #57 #53 #59 #60 Q t u s d✓ :�� :M1 .' .: i. .. 77- -, ... /fir a c 10 _ ?.],�`)�) js J•i SL4'C �` io at,n pi-[21R r10 nn a n _N:� 1� aN�t� , y = f106 direction' nn — o u t C:1 JUnCtion 1= OF M-ADD DIA T PIPE PT PV Q—TOTAL C—FACT LT TOTAL PF PO NOTES 197 _O-t-0 PIPE fib ?9:T-834ta b .fa 6. 15 REF t? 624.76 9.970 0 , 75.0 96.3_ 0-003 q 0 to-iae"a ,7 1016—51 REF ' 0 . 0.00 10. ,:,90 2 13.0 96. 59. PIPE 58 1218. 59 120 ,._ 63.0 5.23 INC 5 PSI FOR BFF_ C)_Qc _>_8 __ U Ca i a %a y.E;a i_a PIPE 59 1?18.59. < 4Ci cr 7510 G: S REF 0 0.00 11 .980 0 10.0 102.07 RI RE ti i ^i p Cif 9 A[a _ () 1 tS to �L-�ll �. oftn5 > COCA COLA ZONE 1 , 0.2-3/3000 - - ROUTE ND. 5 DESCRIPTION --- T,_ -------- REFERENCE > LOSS/FT E FITTS 'PEI. PE C2-TOTAL C-FACT LT TOTAL F'F FO NOTES - OUTLET 1 30.24 2.067 t) 1 .i a 14.2c) K=8 0.07 t.) i a 4.41 C).cm 1 , 7 ; REF t 0.00 2.067 1 1 .2 19.76 , F'IF'E 47 8=T. 14 12 Cl t.) 11 .E ".76 _OFF 701 ii„iaC) is to 12.6 19. _9T D t )C)2 0.QC) . REF 302 84.38 ' 4.260 0 12.8 19. 55 F TFF 77 1,4,R I-)1__ l -C t� j^ � 0_09 H 7777777. M REF ' �"{ s F!4 9 4."'6t) t"i 12 9 19 S4 k ­ F'IF'E 8 25_.35' 120 t_) 12.8 0.20 XX O L -• 4 7 J FIFE 7 L�n�Y Y✓ do �) 1i GI r16 F sM REF 305 -112.54 4.260) 0 12. 5 2C?.t:0 REF °i�b { ){ .{;67 2 2i).t:)4 C 4.41 F'IF'E :7,0 .117..78 1.20 0 437. ._ 4t_,.44 REF C) _),i=aia ?,t-67 �' „ 6:7,„25 REF' t') 604.81. 4.260 t_, 4,8 66.02 F'I PE ��' 1 1.8. 5:' 1 s _t 5'2.E ---RE t- i.? z, 4_2Z, r - r, 0, 1t;7 C? 55 . 17 F'IF'E 54 718.59 120 ) eO,t") 8 5' REF ii 1.t)ia,t_? ? .7v��8i; 8tav0 89,-; 11 OF COCA COLA< ZONE 1 , 0,23/3000 -- — ROUTE NO. 4 DESCE:T FT I Obi D.I I-) y r `��E F� _-1' € EFEFfENCE LOSS/FT E FITTS PE PE O—°#OTAL C t=ACT LT TOTAL F'F PO NOTES ..,. OUTLET ^" 31 .34 2.-2"'7 C) 10.0 15.36 Fits 5R OUTLET 2 3 X1.46 2 227 0 1C),0 X5.46 t)+ i)�i ti ) -t) 12 --t) (")1' F'IF'E 27 89.3^ ? ) c,r 10.0 0. 54 15.46 F=Tt'' , ', 28: 12i692cr )` 428 4Cr5 15.138 ys REF 2.067 2 3.2 61.25 0. 1 5 0 20 0.00 RTP A'a i ^1 —Alc? +M ct i ` -`_i OF 77 COCAS COLA ZONE 1 , 0.21/3000 ---- ROUTE NO. 3 DESCRIPTION -- Oi—Arj P TA__— REFEFtEt CE LOSS/FT E FTTTS PE PE L?—.TOTAL` C—FACT LT TOTAL PF 'FO NOTES OUTLET 15 30.37 2.227 1 8.7 14.41 K=8 —0.02 0 11 —0. 12 0.00 F'IF'E i g Q4 120 f) 19,7 12 OUTLET 19 %80 2' 27 " 0 10.0 13;87 L 'IF'E 19 '"..24.66 120 0 10.0 -0.05 13 .87 ni!Ti FT. i 7 17-19 h 1 ? 2?7 c°r 10),.� i) 17-70 F'IF'E �3 ! 4 95 1 ?+ tr 1q.C; t_ (rCr 13;7 OUTLET 18 29.49 2.227 ' 0 10.0 1=. 58 K=S 0.01 C) 0 —0. 12 0.00 »- QUTLET -' Cl L 12- Ci_frt) F'IF'E 22 63.89 120 0 10.0 0.29 13. 55 nt tTI FT ?ca 79 41 ? ^J i', 1 OUTLET 21 30. 12 2.227 i y 428.3 14. 17 K=8 t_r. 10 i_; i;; 5. 1:1, 0.0o _t L- PIPE 43 123.64 120 i": 23.2 t OF ,, COCA COLA ZONE 1, 0.2-23113000 --- ROUTE NO. 2 DESCRIPTION REFERENCE . LOSS/FT E F I TTS PE PE.:. LI-TOTAL C-Fr+CT LT TOTAL_ F'F !='O NOTES OUTLET S :30.23 ^. 4-2 7 1 8.7 14.33 K=B -0.0271 0 11 -0. 12 t:i,C)0 FIF'c j to -Sn i} 1 ^i' 0 19.7 -0 _St1 �-. OUTLET 9 29.71 2.227 0 10.0 13.79 FIFE 11 --24.39 120 0 `10,i? -0,05 1tl7�, K=6 0 --0.1 c F`IF'E 12 ?:x.141 lyt to 10.ta (r,t,7c� 1 h OUTLET 11 ^9.40 2.227 0 10.0 1;;. 50 K=8 L it`7.01 0 t.7 -0.12 0 0 ER I Rp i 7? ?4 94 190 G Q,-09 131- t}UTLET . 1 "19.�.7 . ... ? ^^7 Ci 1ca.t7 :: 1. .47j F'IF'E 14 _ 6 3.90 12(--) 0 1o.0 0.29 13.47 nI iT! FT 1 7 '4 =to ''' ?7 7 i} PL E 5 ` 9._..4 is . ; t I i!.i_7 0.58 13.64 OUTLET 14 30.03 ?.22-7 0 4'.28. _ 14.09 ---F'1,RE 16 1 . 4O 1 41 -35_-_ 1 4-- REF 0 0.00 2',067 _ 3.2 60. 55 PIPE r 4= 1. 1 2 _ C t.-Z CD ~ B OF 77 � Q-ADD D I A T PIPE PT PV -- E - FITTS- P& - ---- -1=E------- ------ ---- '-- -' 0-TOTAL C-FACT LT TOTAL PF PO NOTES ____________________________________________w______________________________ 0. 107 0 18 ^ 6.99 PIPE 53 ` 718. 59 120 3 52~8 5.63 ^ , REF 0 0.00 4.260 1 25.0 78.64 0. 107 0 55 2. 17 _--_�_�_--___-_--_____-__' ________________________________________________________-__________________ REF 0 100.00 7 .980 1 80.0 89.34 PIPE 55 818. 59 140 2 175.0 0.84 ___________________________________________________________________________ REF Q 74774-71 7-990 0.003 0 0 0.00 PIPE 53 1218. 55 i2o 2 63.0 5.27, INC 5 PSI FOR BFP ___________________________________________________________________________ REF 0 0.00 11 .980 0 10.0 102.07 0.001 0 0 0.00 102.09 Supply 1218. 59 GPM AVAILABLE AT 113.2 PSI - � - ' ` ` ~ 7OF77 ^ --- ROUTE NO. 1 DESCRIPTION --- ��--PIPE_--- REFERENCE LOSS/FT E FITTS PE PE Q-TOTAL C-FACT LT TOTAL PF PO NOTES OUTLET 2 29.67 2.227 � 0 10.0 13.76 K=8 0.00 0 0 -0. 12 0.00 PIPE 4 5.26 120 0 10.0 0.00 13. 59 _________________________________________________________________ 61JTALIET� V 29:560- 21227 0 10.0 13.47 ___________________________________________________________________________ OUTLET 5 29.33 2.227 0 10.0 13.44 KIP 0,00, OUTLET K=8 0.06 0 O -0. 12 0. 00 PIPE 7 93.46 120 0 10.O 0.58 13.60 Yo ________________________________-__-_______________________________________ REF 0 0.00 2.067 2 3.2 60.53 PIPE 41 123.45 120 0 23.2 3.202 0.004 0 0 0.00 PIPE 31 123.45 120 0 12.8 0.05 - -� cEF 902 123.48 4.20 0 12.8 63.80 0.015 0 0 0.00 ---{)---Fg]P' ---'-- ---- -------------------------- --------------' __________________________________________________________________________-' REF 903 123.64 4,260 0 12.8 63.99 PIPE `. 33 370.57 120 0 12.8 0.40 , - ___________________________________________________________ _______________ _ 0.053 0 0 0.00 PIPE 34 492.26 170 0 12.6 0.67 REF 905 112. 54 4.260 0 12. 5 65.05 6 OF 77 1 ---- PIPE TABLE --- FRICTION FRICTION VELOCIT"Y PIPE NO . DIAMETER LENGTH -LOW GPM C LOSS/FOOT LOSS/TOTAL B=EET/SEC Nn 5� 2Z 20 n- 1169 2- 717 1L 52 2.067 23.20 113.78 120 o. 1193 2.768 10.9 51 4.260 52.75 7.1B. 59 120 0. 1066 .0.625 ..16.^ ELF -2,rtX -- 20 00 71 s 5 M931 i6 55 7.9BO 175.00 819. 59 140 0.0048 0.840 5.7 56 7 .980 2322.00 593.83 140 lJ.ii;_j._.,' 6. 154 3.8 -z` _ _ . 2!;4 58 10.390 63.00 1218. 59 120 0.0037 5120 4.6 59 9.970 75.00 120. 59 140 0.0034 0.254 5.0 I PRO i n 00 S z Ct MIA--- 0-014 >_5 61 7.980 .2114.00 624.76 140 0.0029 155 4.0 5 OF 77 COCA COLA ZONE 1 , 0.23/3000 --- PIPE ! ABLE ---- .--,--F-r�•-rSu�T..d,L{:•f }-R i PIPE NO. DIAMETER LENGTH FLOW GPM C ASS/FOOT LOSSUOTAL FEEWSECOND 1 2.067 1 .00 84. 14 120 0.0683 0.068 8.0 n sn r >n2os -0141(01- - r. _. 2.227"..... 10 ._i0 -24.23 120 -0.0047 -0.047 2.0 4 2.227 10.00 5.26 120 0.0003 0.003 0.4 _-_,�`'•_._ ^' 1 e's SL} "iM-• tee :�:::�.-�-> --0 s _ T' 32 �^-5! /••� 6 227 10.00 63.95 12`_i 0.0286 0. 86 7 2.227 10.00 93.46 120 0.0577 0. 577 7.7 8 -0.069 8 10 2.227 19 .67 -54. 10 4. 10 1"-'•,'_7 -0.0210 -0.413 4 .5 j 2 ^,•-:-; tai DL -2A-79 12D =0.0048 12 2 7 l=0 y 5.a_4 120 --0;0003 &r-]t-3 014 14 2.227 1 ).00 34. 54 110 i ..091 0.091 n ^.8 15 2.227 10.00 ?3.45 126 i_i.0)577 0. 577 7.7 16 2.227 428.33 123.48 120 0.0965 41 .351 10.2;}� t 1 Lt�J __C•t;+- ,:'t..-._-.1. �3 _'-C] t]�y rti"•-•, -i-yr O'- 1.. _.- 18 2,221014&67" =514.46 1 10 -fj' 12 00 18 4.5 19 .227 1Ci,'r_]C] -24.66 120 0610049 _-0,t X49 2:0 21 2.227 10.00 04.44 120 0.0091 0.091 2.8 nA 2.227 10.00 6.3.89 120 0.0285 O) 285 5.3 --.-_-__.-->✓- -?_-_-'`-`--�--.�i l.11i ._.-__.-f_..;��:.-. _-__..i,:arf.%-----��-s-��.�"]..f-�.--_._,...-.--••-'•i- --.t_i ...___._.....-._ -.-..L.-.-i-....._._-_..._.-.._. _-_ �4 '<2.2 7 428>°33 123.64 120L V01096S t'F1 .449 25 2.227 =59.'00 ^7.0 120 C],005S 0.226 0222 Li 2z 1-woo _ fit°r._.���_ _�_^ti__��9.t�. �1-= Z- 27 2.227 10.00 89.32 120 0.0536 0.536 7.4 26 2.227 42e .33 121 .69 120 0.0940 40.252 10.0 _--r_=f ----T-s r�-f----�i�i-c'�.-'- -lrk-s_,.fi4•-- _j.Y_t:.+----•.)-.tJ�L-_' --. - - 9' e::r-_�,i-- '� - 27 487.33 113.76 20 0.0830 40.442 9.4 31 4.260 12.75 123.45 120 0.0041 0.052 2.B -_._-_. - _ _.-_.----�i•-n:r,'.+'..">{;.}------�.-�n f^=--..-:_ 246-93 -12i)_ 33 4 . 260 9 ....._ . _. 370. 57 120 0. 0313 0.399 99 � n 34 4. 260 12.60 492.26 120 0.0530 0 .667 11 . 11- 1 �1 -0,07T5 _ 4 _ _ 6 4.260 12.75 E4. 14 120 0.0020 0.026 1. . , 37 4. 260 12.75 168. 51 120 0.0073 0093 3A3 .x'=34- "-t --V c. ''!'.z 39 4. 260 12.60 226.33 120 0. 0126 0. 159 5. 1 si''.. n.,.....if_ 12. 50 113.78 120 {1.{::1�%._51 0.044 2.6 T 2a.45-120 - -- --- 42 2.067 23.20 123.4B 120 0. 1389 3.220 11 8 43 2.067 23.20 123.64 120 01391 3.22B ' L.. -_� '"3-'• .^r _. _ _2-l-,6 V_. --.L--20 0 -1 T-Y1- --,.. 45 2 . 067 23.20 112. 54 120 0 _ . 1!'._9 2.713 1 - . -- 0 113.78 120 0. 1193 2.768 10.9 S4.14-- =}- .-z= ---- ----- 48 2.067 11 .20 •-84.38 120 -0.0686. -0.769 3. 1 4? 2.067 11 .2f_; --84 83 120 -0.0692 --0.7 7 6 8. 1 � 4 OF 77 ~ COCA COLA ZONE 1 , 0.23/3000 ~ ' _ .. ___ OUTLET # K-FACTOR PRESSURE FLOW ELEV. (FEET) MIN. FLOW 2 � � `= �^ 8^ 0 0-� t' � 13.756 29.67 � 31 .53 �� - - ' ' r 3 8.000 13. 587 29.49 r"1 .81 29.33 __. __---29. 5 8.000 13.439 29.33 32.37 29.33 6 8.000 13.603 29. 51 32.65 29.33 -�___'_______- 8 � ' ' 8.000 ,� ' � / 14.326 30.28 31 .25 29.33 � 7 ' 9 8.000 13.792 29.71 31 .53 29.33 1.0____---_ _f�.1)(l0_-__-__13�'�23_____�29.53--____-_�]1,'81-_-_-----_ 11 8.000 13. 504 29.40 32.09 29.33 12 8.000 13.474 29.37 32.37 29.33 15 u � 31 .25 �� ,^� /� , , a 29^33 ^ ^ 17 8.000 13.704 29.61 31 .81 29.33 18 8.000 13. 585 29.49 32.09 29.33 R 0001 20 81000 13.718 29.61 32.65 29;33 23 8.000 15.463 31 .46 32. 61 29.33 24 8.000 15.878 31 .88 32.89 29.33 ' ^ COCA CU UM ___+(•tU __ sheet ;•.fir,,, See Below - Supply #3 i #52 0-------- .-------------------------------------------------0 #46 —114 V 1 1.4 _ 1 =i # -F 40 14 Loop n b- 5 � - 605 #35 -- V #29 v x510--------- - ---- __ - ----- - - - - � 113 V I'__ 1 #39 227 Loop number 4 493 #34 050 0--------- -- --22 : -- -<---24-<:---.--__----_.-w-_..___------__.--------_0 044 - 28 V 28 59 90 122 V 122 , *38 254 Loop_numbe, 371 #33 V #17 3;-10 #19 #20 #21 #22 #23 #24 v>--15->--16->--17-<--18-<--19-<--20-<--21-<-------0 #37 169 ' Loop number 2 247 '#3 V #9 010 #11 #12 ##13 #14 015 3#16 V #F40 0--- _ :.-_r--' ---i}0 -C?9-`' - -1f;_';:_ J 1- :.- -ih-.;.- _1•= --i4 - -0 #42 —_ - 84 v e.4 54 24 6 35 64 94 V 124 #36 05 Loop number 1 124 #01 ##47 --- 85 85 0 53 0 24 0 6 - 0 35 64 i i 94 ' 0 124 1..2•'_4 �._(,_:: _.-0_ .: ---Ca-- .s�.�Pp},y._ _ 719 < 71? 819 594 .1219 121? 1219 1219 nn outlet 0 junction System has 50 heads on The branch lines. System has 6 branch lines. The supply Main enter-s--at ' oo_p-_5--__The heads are spaced 10 feet apart. The lines are spaced 12.75 feet apart. Tie-in main starter piece is 1 foot; long . The riser nipple length is 2.2 feet with a tee on top. There are 7 heads operating on the branch lines with a total of 24 Heads operating . Head K: factor used is 8 Fir-anr5 1 i na diameter is " -� Supply cr-os=main diameter is 4.26 Tie'-in crossmaln diameter is 4126 The positions shown below represent the position of the f irst:. Ihead< in the operating area from the Tie-in side. increase in friction los s thru the grid from the preced- ing position . Position W -0.20756 Position - 1 r a' �, r � q �> Aay. '%«. ,d� -..R..,. F r .t ..�1= }.., � �,+ `� ,,.. �� !♦ ry i '9: § .. A ,� k t � ,. .. _ �� +� f v. � �• j� .. t,. r - 'A ,� ',. � �; v yb k0. � v,4 f' ��. X ��4 �� 1 o _ _- - THE L-fl-COMP - NORTHH MASS ETTS pE P"��� �C0 'T irl A�Ga tLC�.LA'/f;�5 t1 6 tA a {;` ' s FnrGp t 'Yj1 �. ♦ �.iS n,yay�C , yr�,O,. ,qN AL Ak .- 0CCUC A}ult"K`5t, l N INARY HAZARD 'EFi SPRINKLER 1330 SO. FT. _ F 'SPRINKLERS CALOUL'Al"ED 24 - P8 TOTAL_ WATER REQUIRED 1218.59 GPM -S-TftEA . - AM �Ri�flt fJR --WAREHOUSE—MErt#AN�CA nP Tf A SR NAME OF DESIGNER - RYBAK ENGINEERING, INC. AU1'MOR IT MAU T NG RUC;SD I CT I ON FLOW TEST - STATIC 125 RESIDUAL. 90 FLOW 2189 SYSTEVI DE. AS ff SYSTEM DEMANS7 A!T SUEi�Y IS 718. x. G 'M A"1" !: 10209 RBI 1-JOSE REQUIREMENT NOT INCLUDED ABOVE IS 500 GPM. - - r 10 _ 113 L.E'S I AVAILABLE W I TH r .12 18.59 GPM FLAW I NG