Manual for the Design of Pipe Systems and Pumps - GEA ...
Manual for the Design of Pipe Systems and Pumps - GEA ...
Manual for the Design of Pipe Systems and Pumps - GEA ...
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6.4 Pumping <strong>of</strong><br />
viscous media<br />
6.4.1 Correction <strong>for</strong><br />
high viscosities<br />
In <strong>the</strong> previous example (Chapter 6.1) water served as pumping medium.<br />
In practice media o<strong>the</strong>r than water are conveyed. In this respect viscosity is a factor that<br />
must be taken into account <strong>for</strong> <strong>the</strong> calculation <strong>and</strong> design <strong>of</strong> <strong>the</strong> pump.<br />
Conveying liquids <strong>of</strong> higher viscosity (ν) at constant speed (n), reduce <strong>the</strong> flow rate (Q), flow<br />
head (H) <strong>and</strong> <strong>the</strong> efficiency (η) <strong>of</strong> <strong>the</strong> pump, while power consumption Pz <strong>of</strong> <strong>the</strong> pump (see<br />
Fig. 28) increases tt <strong>the</strong> same time. According to <strong>the</strong> method <strong>of</strong> approxima-tion, (6.4.2) <strong>the</strong><br />
suitable pump size can be determined, starting from <strong>the</strong> operating point <strong>for</strong> viscous liquids<br />
via <strong>the</strong> operating point <strong>for</strong> water. The pump’s power<br />
consumption depends on <strong>the</strong> efficiency <strong>of</strong> <strong>the</strong> complete<br />
H<br />
unit.<br />
Annexed are tables used <strong>for</strong> <strong>the</strong> determination <strong>of</strong><br />
pressure drops in dependence <strong>of</strong> viscosity <strong>and</strong> pipe<br />
diameter. In this connection it is worthwhile to mention<br />
that <strong>the</strong> pressure drop in dependence <strong>of</strong> viscosity is<br />
irrelevant <strong>for</strong> centrifugal pumps <strong>and</strong> can <strong>the</strong>re<strong>for</strong>e be<br />
neglected. Centrifugal pumps are suitable <strong>for</strong> liquids<br />
up to a viscosity <strong>of</strong> 500 mm2/s. picture 5<br />
If it is <strong>the</strong> question <strong>of</strong> pumping viscous media such as Fig. 28<br />
quarg, butter or syrup, rotary piston pumps will be used due to <strong>the</strong>ir higher<br />
efficiency in this respect.<br />
The following page shows an example that explains <strong>the</strong> calculation <strong>and</strong> design <strong>of</strong> a pump<br />
used <strong>for</strong> viscous media. Decisive in this connection are <strong>the</strong> correction factors <strong>for</strong> <strong>the</strong> flow<br />
head (K H), flow rate (K Q) <strong>and</strong> <strong>the</strong> pump efficiency (K η).<br />
The correction factors are found in <strong>the</strong> diagram on page 31, by proceeding in <strong>the</strong><br />
following steps:<br />
1. Find out <strong>the</strong> kinematic viscosity <strong>of</strong> <strong>the</strong> medium in mm 2/s<br />
2. Determine product <strong>of</strong> Q x √H (m 3/h √m)<br />
3. Set up a vertical at <strong>the</strong> intersection <strong>of</strong> Q x √H with <strong>the</strong> corresponding viscosity<br />
4. Reading <strong>the</strong> intersections with <strong>the</strong> three correction lines at <strong>the</strong> vertical<br />
5. Enter <strong>the</strong>se values into <strong>the</strong> equations <strong>and</strong> calculate <strong>the</strong> corrected value<br />
On <strong>the</strong> basis <strong>of</strong> <strong>the</strong> obtained values, <strong>the</strong> pump can be desigend by means <strong>of</strong> <strong>the</strong> pump<br />
characteristic <strong>for</strong> water, (see Chapter 6.2).<br />
30<br />
<strong>GEA</strong> Tuchenhagen<br />
H z<br />
P z<br />
P<br />
h<br />
h z<br />
Q