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CS & STC Series<br />
The selection chart provided contain an a rray of popular sizes for quick<br />
sizing. It does not pro-de curves for a ll models available. Refer to page 44<br />
8 45 for deta iled calcula ti<br />
on Information.<br />
Computer selection data sheets forstandard or spe cial models are avaBable<br />
through the engneedng department of Ame rican Indust ri al. To use the<br />
fo ll<br />
owings graphs cor re<br />
ctly, refer le the Ins truction notes r1.5r.<br />
1) HP Curves are based upon a 401 approach temperature; for<br />
example: oil leaving a coder at 125T. using SWF coo ling water<br />
(125•F -WF.4 ( rF ).<br />
RPP-24544 REV Id<br />
3) OIL PRESSURE DROP CODING: 4• S.psl ir. 10 psi; 0.20 psi;<br />
A. 50psi. Cu rv es that have no p ressure d ro<br />
p code symbols kale<br />
that the dl pressure drop Is less than 6 psi for are Bow rate Shown.<br />
If 4) Pressure Drop is based upon o4 with an a y ol 100 SSU.<br />
I It the average oil Nscosfly Is other Nan100 l n mul tiply the<br />
Indicated Pressure Drop by the correspo mg value from corrections<br />
table A.<br />
6) Corrections for approach temperature and oil viscosity a re as fo ll<br />
ows:<br />
2) The oil water rat io of 1:1 or 2:1 means that for every 1 ga ll<br />
on of dl ,,,,,,s wnrl 40<br />
circulated, a mi ni mum of 1 or 12 ga llon (respectively) of 851F water H.P.(v, aa ^,r,r) w H.P.(,,,,, lae^ x (AEI 40 x B.<br />
must be circulated lo linatch q)e Curve res ults.<br />
500<br />
400<br />
300<br />
200<br />
150<br />
W 100<br />
JO 80<br />
U 80<br />
? 70<br />
W 60<br />
0 50<br />
cc 40<br />
a<br />
= 30<br />
20<br />
15<br />
10<br />
8<br />
8<br />
. 7<br />
6<br />
5<br />
HEAT ENERGY DISSIPATION RATES (Basic Stock Model)<br />
Ratio<br />
1. su-1 3+FP 21 Originator.<br />
2. 514 -34-FP 2:1<br />
Ira<br />
3. 624.1.3-4-FP 2:1' ,'<br />
7•'^': ? ^^i_s<br />
Date: 7 y17a. d<br />
(?'"<br />
{. 624.34-FP 2/ t :(r a + ^'tA +<br />
Checked by.<br />
T<br />
S. 614-1.7.4-FP2 1 .<br />
1<<br />
i 6. 814 -4-4-FP 21<br />
'<br />
Date:<br />
T. e24 - 1.7.44P 21<br />
. S. 824-44-FP 2:1 _ y -:• ;,<br />
8. 836 . 1.74•FP 2:1 e: ••<br />
- 10. 638-41•FP 21 4' s +<br />
11. 1014.2-6-FP •.8^<br />
Z,<br />
12 101F6&fP2.1<br />
13. 1024 . 26FP 21 -. _'' "' e..^. :••<br />
^.<br />
14. 3024 .56-FP 21<br />
-'<br />
13. ta36.2$FP21 F'<br />
16. 1036.56FP 21 ' , < ^ 264<br />
17. 1221 . 25&FP 21<br />
•.. i-: }^.,-:u .:''a<br />
18. 1224 . 6 4-FP 21<br />
-<br />
19. 1238.258-FP 21<br />
+ .. 20<br />
20. 1236Tt„<br />
-66FP<br />
will r<br />
21. 1248 . 2.5&FP 21<br />
3 .^ t +<br />
- :22 1248 . 66FP 21 r2,9;y .!'.i't,. ?^ +7. `.F!<br />
23. 1260 . 2-45&-4FP 21 y:y<br />
24.' 1260 r : t '. `.: 'P:,, L•,^^<br />
. 66FP 21<br />
25. 1724 . 3.5&FP 21 :1.<br />
26. 1724.8.4-6-FP21<br />
•' ,: ..<br />
....<br />
27. 1736-3.58FP 21'' 1Z<br />
7 !` ' •SSA w%.<br />
28. 1736 . 8.45FP 2:1<br />
. 29. 1740 . 3."TP 21 ' 24s .y ^ ><br />
f<br />
r<br />
.' ^ i ' :"•Y ^' -. rq^ ;;, ;:<br />
.'. 30. 1748-a46FP 21<br />
1,<br />
.. 31. 1760 . 3S4FP 21 , p , ^ •._ '.<br />
n ♦ x? y !d -y:`<br />
• 32 1760 . 84&FP 21 p><br />
Q i<br />
.:.rte w r.-.::f'6-<br />
7 33. 17M-3S&FP 21<br />
S' C,, .y1: rH. 34 1772 . 8.44-FP 2/ •, g:P 1•: f1<br />
i§^^i<br />
a<br />
r: 1' ^: h . f+i .r. Yx ^ +tt tiyF^ ':'i.<br />
1:<br />
8<br />
7<br />
{ vlscoslTV<br />
r<br />
r`<br />
•.. ,<br />
',<br />
':; *<br />
n-<br />
CORRECRONS<br />
.<br />
:.4<br />
'f Avg Oil<br />
" SSU A B<br />
0 0.83 Wr<br />
3 4 5 6 7 8 910 15 20 40 60 80 100 200<br />
GPM (Oil Through Cooler)<br />
rral.MHn rererveeew b.W walawNe Mdpr wwJ neat<br />
46 COPYr^l 02004 MrrlCan hWueeW Heal TnMlw. W. am allure lid zit a am W 1047) M-toot lac 1047) MI .1010 enrw eTaa.e<br />
.,<br />
"' 3,. 7 Attachment 9<br />
Cale. No.: 145579 V-004<br />
t-<br />
Rev. No.: 1<br />
Sheet 6 of 10<br />
. ' y f100 4.00 1.53<br />
2<br />
.•^ `<br />
AS-03