product guide cr-h, crn-h, cre-h, crne-h
product guide cr-h, crn-h, cre-h, crne-h
product guide cr-h, crn-h, cre-h, crne-h
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Selection and sizing<br />
CR-H, CRN-H, CRE-H, CRNE-H<br />
Selection of pumps<br />
Selection of pumps should be based on:<br />
• duty point of the pump<br />
• sizing data such as pressure loss as a result of<br />
height differences, friction loss in the pipework,<br />
pump efficiency etc.<br />
• pump materials<br />
• piping dimensions<br />
• shaft seal<br />
• inlet pressure and operating pressure.<br />
Duty point of the pump<br />
From a duty point it is possible to select a pump on the<br />
basis of the curve charts in the section Curve charts/<br />
technical data starting on page 24.<br />
H<br />
[m]<br />
280<br />
260<br />
2 0<br />
220<br />
200<br />
180<br />
160<br />
1 0<br />
120<br />
100<br />
80<br />
60<br />
0<br />
20<br />
0<br />
H<br />
[ft]<br />
950<br />
900<br />
850<br />
800<br />
750<br />
700<br />
650<br />
600<br />
550<br />
500<br />
50<br />
00<br />
350<br />
300<br />
250<br />
200<br />
150<br />
100<br />
50<br />
-10<br />
-9<br />
-8<br />
-7<br />
-6<br />
-5<br />
-<br />
-3<br />
2 E)<br />
2-2<br />
1-1 (E)<br />
-11-2<br />
-10-2<br />
9-2<br />
8-2<br />
7-2<br />
6-2<br />
5-2<br />
- -2<br />
3-2 (E)<br />
2-1<br />
1 E)<br />
0<br />
0 20 0 60 80 100 120 1 0 160 180 200 Q [US GPM]<br />
0 5 10 15 20 25 30 35 0 5 Q [m³/h]<br />
P2 P2<br />
Eff<br />
[kW] [hp]<br />
[%]<br />
P2 1/1 80<br />
3<br />
P2 2/3 60<br />
2<br />
E f<br />
2<br />
0<br />
1<br />
1<br />
20<br />
0 0<br />
0<br />
0 20 0 60 80 100 120 1 0 160 180 200 Q [US GPM]<br />
H NPSH<br />
H<br />
[m] [ft]<br />
[ft]<br />
30<br />
30<br />
8<br />
20<br />
20<br />
10<br />
NPSHR<br />
10<br />
0 0<br />
0<br />
0 20 0 60 80 100 120 1 0 160 180 200 Q [US GPM]<br />
Fig. 23 Example of a curve chart<br />
CR(E) 32 H<br />
2-pole, 60 Hz<br />
Sizing data<br />
When sizing a pump the following must be taken into<br />
account.<br />
• Required flow and pressure at the point of use.<br />
• Pressure loss as a result of height differences<br />
(H geo ).<br />
• Friction loss in the pipework (H f ).<br />
It may be necessary to account for pressure loss in<br />
connection with long pipes, bends or valves, etc.<br />
• Best efficiency at the estimated duty point.<br />
• NPSH value.<br />
For calculation of the NPSH value, see Minimum<br />
inlet pressure - NPSHA on page 22.<br />
H<br />
[ft]<br />
950<br />
900<br />
850<br />
800<br />
750<br />
700<br />
650<br />
600<br />
550<br />
500<br />
350<br />
300<br />
250<br />
200<br />
150<br />
100<br />
50<br />
0<br />
50<br />
00<br />
TM04 4551 1609<br />
H geo<br />
Hf<br />
Pb<br />
Fig. 24 Sizing data<br />
Hv<br />
NPSHR<br />
Efficiency<br />
Before determining the point of best efficiency, the<br />
operating pattern of the pump must be identified. If the<br />
pump is expected to operate in the same duty point,<br />
then select a CR(E)-H, CRN(E)-H pump which is<br />
operating in a duty point corresponding to the best<br />
efficiency of the pump.<br />
H<br />
[m]<br />
280<br />
260<br />
2 0<br />
220<br />
200<br />
180<br />
160<br />
1 0<br />
120<br />
100<br />
80<br />
60<br />
0<br />
20<br />
0<br />
H<br />
[ft]<br />
950<br />
900<br />
850<br />
800<br />
750<br />
700<br />
650<br />
600<br />
550<br />
500<br />
50<br />
00<br />
350<br />
300<br />
250<br />
200<br />
150<br />
100<br />
50<br />
10<br />
-9<br />
-8<br />
-7<br />
-6<br />
-5<br />
-<br />
-3<br />
-2 (E)<br />
-2 2<br />
-1-1 E)<br />
-11-2<br />
-10-2<br />
-9-2<br />
-8-2<br />
-7-2<br />
-6-2<br />
-5-2<br />
- -2<br />
-3-2 (E)<br />
-2-1<br />
-1 (E)<br />
CR(E) 32 H<br />
2-pole, 60 Hz<br />
0<br />
0 20 0 60 80 100 120 1 0 160 18 200 Q [US GPM]<br />
0 5 10 15 20 25 30 35 0 5 Q [m³/h]<br />
P2 P2<br />
Eff<br />
[kW] [hp]<br />
[%]<br />
P2 1/1 80<br />
3<br />
P2 2/3 60<br />
2<br />
Eff<br />
2<br />
0<br />
1<br />
1<br />
20<br />
0 0<br />
0<br />
0 20 0 60 80 100 120 1 0 160 180 200 Q [US GPM]<br />
H NPSH<br />
H<br />
[m] [ft]<br />
[ft]<br />
30<br />
30<br />
8<br />
20<br />
20<br />
10<br />
NPSHR<br />
10<br />
0 0<br />
0<br />
0 20 0 60 80 100 120 1 0 160 180 200 Q [US GPM]<br />
Fig. 25 Example of a CR(E)-H, CRN(E)-H pump’s duty<br />
point<br />
H<br />
[ft]<br />
950<br />
900<br />
850<br />
800<br />
750<br />
700<br />
650<br />
600<br />
550<br />
500<br />
350<br />
300<br />
250<br />
200<br />
150<br />
100<br />
50<br />
0<br />
50<br />
00<br />
Duty<br />
point<br />
Best<br />
efficiency<br />
TM04 3689 4804<br />
TM02 0039 1303<br />
19