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Positive Displacement Pumps

Reference data and engineering information about positive displacement pumps for pumps applications.

positivedisplacementpumps

Overview

Engineering reference data for Positive Displacement Pumps in pumps.

Key Formulas

Pump Power

P=QHρgηP = \frac{Q \cdot H \cdot \rho \cdot g}{\eta}

Hydraulic power / efficiency.

NPSH Available

NPSHa=Psρg+vs22gPvρgNPSH_a = \frac{P_s}{\rho g} + \frac{v_s^2}{2g} - \frac{P_v}{\rho g}

Net Positive Suction Head available.

Affinity Laws

Qn,Hn2,Pn3Q \propto n, \quad H \propto n^2, \quad P \propto n^3

Flow, head, power vs speed.

Variables

SymbolDescriptionUnit
PPPowerW
QQFlow ratem³/s
HHHeadm
η\etaEfficiency
nnRotational speedRPM

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

7 rows
Speed correction for reciprocating pumps based on liquid viscosity
Liquid Viscosity(SSU)
Speed Reduction(%)
2500
5004
100011
200020
300026
400030
500035

Source: engineeringtoolbox.com

7 rows
Speed correction for reciprocating pumps based on water temperature
Water Temperature(°C)
Speed Reduction(%)
210
279
3818
5225
6629
9334
12138

Source: engineeringtoolbox.com

Rotary Pump Speed Correction Table

9 rows
Speed correction for rotary pumps based on liquid viscosity
Liquid Viscosity(SSU)
Speed Reduction(%)
6002
8006
100010
150012
200014
400020
600030
800040
1000050

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.

Interactive Charts

Horsepower Required to Pump Water

Pump - Temperature Rise vs. Volume Flow

Pumps - Parallel vs. Serial Arrangement

References