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Pump Selection Centrifugal - low P (<3.5 MPa), low viscosity, high flow rates Rotary positive displacement - medium P (<20 MPa), medium viscosity, medium.

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Presentation on theme: "Pump Selection Centrifugal - low P (<3.5 MPa), low viscosity, high flow rates Rotary positive displacement - medium P (<20 MPa), medium viscosity, medium."— Presentation transcript:

1 Pump Selection Centrifugal - low P (<3.5 MPa), low viscosity, high flow rates Rotary positive displacement - medium P (<20 MPa), medium viscosity, medium flow rates Reciprocating - high P (<150 MPa), high viscosity, low flow rates Special issues - corrosion and abrasion See Figure 12-3 course pack

2 What determines pump size?
Operating pressure Elevation change Acceleration of fluid Frictional losses

3 Centrifugal Pump Curves
Flowrate Total head Power Efficiency NPSH Impeller size

4 Schematic Pump Curve TDH? units? GPM? %? HP? NPSH? units?
What is in inches?

5 Identify the lines and associated units:

6 Pump NPSH Net Positive Suction Head (NPSH) =
Head required at suction of pump in excess of the bubble pressure of the fluid at the pump temperature Why does this matter?

7 Pump costing Based on power Affected by Adjust for… Materials
Operating pressure Type of pump Adjust for…

8 Pumps FBM is a function of material and pressure factors.

9

10 Suction pressure? Discharge pressure?


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