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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7.3 Example Product data<br />
• Medium: Yeast<br />
• Temperature: t = 10°C<br />
• Viscosity: η = 100 cP<br />
• Density: ρ = 1,000 kg/m3 • Portion <strong>of</strong> particles none<br />
• Particle size none<br />
• Single acting mechanical seal in <strong>the</strong> pairing carbon against stainless steel<br />
Pumping data<br />
• Q = 300 l/min.<br />
• ∆p = 5 bar<br />
• NPSH: 0.4 bar abs.<br />
Selection <strong>of</strong> <strong>the</strong> pump size<br />
The characteristic diagram (Fig. 30) may be used as a first step <strong>for</strong> <strong>the</strong> preliminary<br />
selection <strong>of</strong> <strong>the</strong> pump type in question. For this purpose <strong>the</strong> required flow rate <strong>and</strong> <strong>the</strong><br />
known viscosity <strong>of</strong> <strong>the</strong> product are to be entered. According to this diagram, <strong>the</strong> VPSH 54 is<br />
<strong>the</strong> suit able pump size. Now <strong>the</strong> pump can be examined more closely using <strong>the</strong> detailed<br />
characteristic diagram (Fig. 31) shown on <strong>the</strong> next page.<br />
1.000.000<br />
100.000<br />
10.000<br />
Viscosity cP<br />
1.000<br />
Fig. 30<br />
100<br />
10<br />
1<br />
1 10 100 1.000<br />
Volume flow l/min<br />
33<br />
<strong>GEA</strong> Tuchenhagen<br />
42<br />
52<br />
44<br />
64<br />
62<br />
54<br />
300 l/min