Positive Displacement Pumps
Reference data and engineering information about positive displacement pumps for pumps applications.
Overview
Engineering reference data for Positive Displacement Pumps in pumps.
Key Formulas
Pump Power
Hydraulic power / efficiency.
NPSH Available
Net Positive Suction Head available.
Affinity Laws
Flow, head, power vs speed.
Variables
| Symbol | Description | Unit |
|---|---|---|
| Power | W | |
| Flow rate | m³/s | |
| Head | m | |
| Efficiency | — | |
| Rotational speed | RPM |
Pump Classification
Positive displacement pumps are divided into two main classes:
- Reciprocating pumps: plunger pumps, diaphragm pumps, piston pumps
- Rotary pumps: gear pumps, lobe pumps, vane pumps, progressive cavity pumps, peripheral pumps, screw pumps
Operating Characteristics
A positive displacement pump operates with an expanding cavity on the suction side and a decreasing cavity on the discharge side. Liquid flows into the pump as the suction cavity expands, and flows out as the discharge cavity collapses.
Key operational properties:
- Constant volume delivery: Each cycle displaces a fixed volume regardless of discharge pressure
- No shut-off head: Unlike centrifugal pumps, positive displacement pumps cannot operate against closed discharge valves — this will cause pressure buildup until line failure or pump damage
- Relief valve required: A safety/relief valve on the discharge side is mandatory. External relief valves with return lines to the suction side or supply tank are highly recommended; internal valves should serve only as backup safety devices
Reciprocating Pump Operation
Plunger pumps use a cylinder with a reciprocating plunger. During the suction stroke, the plunger retracts and the suction valve opens. During the forward stroke, the plunger pushes fluid out through the discharge valve.
Single-cylinder plunger pumps produce pulsating flow — maximum flow during mid-stroke and zero flow at end positions. This causes energy waste, vibration, and potential water hammer effects. Multi-cylinder configurations with offset phasing compensate for these issues.
Diaphragm pumps use pressurized hydraulic oil to flex a diaphragm, making them suitable for pumping hazardous and toxic fluids.
Reciprocating Pump Speed Correction Tables
Liquid Viscosity(SSU) | Speed Reduction(%) |
|---|---|
| 250 | 0 |
| 500 | 4 |
| 1000 | 11 |
| 2000 | 20 |
| 3000 | 26 |
| 4000 | 30 |
| 5000 | 35 |
Source: engineeringtoolbox.com
Water Temperature(°C) | Speed Reduction(%) |
|---|---|
| 21 | 0 |
| 27 | 9 |
| 38 | 18 |
| 52 | 25 |
| 66 | 29 |
| 93 | 34 |
| 121 | 38 |
Source: engineeringtoolbox.com
Rotary Pump Speed Correction Table
Liquid Viscosity(SSU) | Speed Reduction(%) |
|---|---|
| 600 | 2 |
| 800 | 6 |
| 1000 | 10 |
| 1500 | 12 |
| 2000 | 14 |
| 4000 | 20 |
| 6000 | 30 |
| 8000 | 40 |
| 10000 | 50 |
Source: engineeringtoolbox.com
Viscosity Correction Example
Fuel oil No. 2 at 20°C has a viscosity of approximately 150 SSU, requiring no speed reduction. Fuel oil Type 5 at 100°C has a viscosity of approximately 4000 SSU, requiring approximately 30% speed reduction for a reciprocating pump.