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

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5.8 Q-H characteristic<br />

diagram<br />

Be<strong>for</strong>e designing a pump, it is important to ascertain <strong>the</strong> characteristic curve <strong>of</strong> <strong>the</strong> plant<br />

that allows you to select <strong>the</strong> right pump by help <strong>of</strong> <strong>the</strong> pump characteristic curve<br />

The operating per<strong>for</strong>mance <strong>of</strong> centrifugal pumps is rarely represented in <strong>the</strong> <strong>for</strong>m <strong>of</strong> tables,<br />

but mainly in <strong>the</strong> <strong>for</strong>m <strong>of</strong> characteristic curves (Fig. 15). These pump characteristic curves are<br />

measured at line machines at constant speed <strong>and</strong> show <strong>the</strong> flow rate (Q in m 3/h) <strong>and</strong> <strong>the</strong> flow<br />

head (liquid column in m) <strong>of</strong> <strong>the</strong> pump. The flow head H <strong>of</strong> a pump is <strong>the</strong> effective mechanical<br />

energy transferred by <strong>the</strong> pump to <strong>the</strong> pumped liquid, as a function <strong>of</strong> <strong>the</strong> weight <strong>for</strong>ce<br />

<strong>of</strong> <strong>the</strong> pumped liquid (in m liquid column). It is independent <strong>of</strong> <strong>the</strong> density (r) <strong>of</strong> <strong>the</strong> pumped<br />

liquid; that means a centrifugal pump transfers liquids regardless <strong>of</strong> <strong>the</strong> density up to <strong>the</strong><br />

same flow head. However, <strong>the</strong> density must be taken into account <strong>for</strong> <strong>the</strong> determination <strong>of</strong><br />

<strong>the</strong> power consumption P <strong>of</strong> a pump.<br />

The actual flow head <strong>of</strong> <strong>the</strong> pump is determined by <strong>the</strong> flow rate H A <strong>of</strong> <strong>the</strong> plant, which<br />

consists <strong>of</strong> <strong>the</strong> following components:<br />

0<br />

HA = Hgeo +<br />

pa ρ<br />

-<br />

x<br />

pe g<br />

+<br />

v 2<br />

a - v 2<br />

e<br />

2g<br />

+ Σ Hv H geo<br />

pa - pe ρ x g<br />

0<br />

v a 2 - v e 2<br />

Σ H v<br />

2g<br />

geodetic flow head = <strong>the</strong> difference in height to overcome between <strong>the</strong> liquid<br />

level <strong>of</strong> <strong>the</strong> suction <strong>and</strong> <strong>the</strong> delivery side<br />

difference <strong>of</strong> pressure heights between liquid level <strong>of</strong> <strong>the</strong> suction <strong>and</strong><br />

delivery side with closed tanks<br />

speed difference (can be neglected in practice)<br />

sum <strong>of</strong> pressure drops (pipe resistances, resistance in fittings <strong>and</strong> <strong>for</strong>med parts in<br />

suction <strong>and</strong> delivery pipes)<br />

20<br />

<strong>GEA</strong> Tuchenhagen

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