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Manual for the Design of Pipe Systems and Pumps - GEA ...

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6.3.3 Reducing <strong>the</strong><br />

impeller size<br />

6.3.4 Operation in<br />

parallel<br />

6.3.5 Operation in<br />

series<br />

Tuchenhagen <strong>of</strong>fers <strong>for</strong> each pump different impeller sizes. It may happen that <strong>the</strong> best<br />

efficiency point <strong>of</strong> <strong>the</strong> impeller is located between two characteristic curves. The impeller will<br />

<strong>the</strong>n be turned to size in order to obtain <strong>the</strong> required diameter.<br />

This is both <strong>the</strong> most simple <strong>and</strong> favourable method.<br />

H<br />

H 1<br />

H 2<br />

Reducing Impeller <strong>the</strong> reduced impeller size<br />

picture 4<br />

Fig. 25 - Reducing <strong>the</strong> impeller size<br />

Two pumps can be operated in parallel, if <strong>the</strong> desired operating point cannot be reached with<br />

only one pump. In such a case <strong>the</strong> flow <strong>of</strong> <strong>the</strong> two pumps are added while <strong>the</strong> flow head<br />

remains unchanged.<br />

Q 1<br />

Q 2<br />

Fig. 26 - Operation in parallel<br />

B 2<br />

If <strong>the</strong> required flow head cannot be achieved by one pump only, two pumps are connected in<br />

series. Thus <strong>the</strong> flow head is doubled at constant flow rate.<br />

P 1 P2<br />

Fig. 27 - Operation in series<br />

P = P 1 + P 2 Q = constant<br />

29<br />

<strong>GEA</strong> Tuchenhagen<br />

B 1<br />

D 2<br />

D 1<br />

Q 2 Q 1 Q<br />

Q = Q 1 + Q 2 P = constant<br />

D 1<br />

D 2<br />

2<br />

Q1 Q2 ≈ ≈<br />

H 1<br />

H 2

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