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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

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