Pump Head Pressure
Reference data and engineering information about pump head pressure for fluid mechanics applications.
Overview
Engineering reference data for Pump Head Pressure in fluid mechanics.
Key Formulas
Reynolds Number
Ratio of inertial to viscous forces — determines flow regime.
Bernoulli's Equation
Conservation of energy for steady, inviscid, incompressible flow.
Continuity Equation
Conservation of mass for incompressible flow.
Darcy-Weisbach
Pressure drop due to friction in a pipe.
Variables
| Symbol | Description | Unit |
|---|---|---|
| Reynolds number | — | |
| Fluid density | kg/m³ | |
| Flow velocity | m/s | |
| Characteristic dimension | m | |
| Dynamic viscosity | Pa·s | |
| Pressure | Pa | |
| Darcy friction factor | — |
Head vs. Pressure Data Table
For water (SG = 1.0 at 62°F / 17°C), the relationship between pump head in feet and pressure in psi is provided below.
Head(ft) | Pressure(psi) |
|---|---|
| 1 | 0.43 |
| 2 | 0.87 |
| 3 | 1.30 |
| 4 | 1.73 |
| 5 | 2.17 |
| 6 | 2.60 |
| 7 | 3.03 |
| 8 | 3.46 |
| 9 | 3.90 |
| 10 | 4.33 |
| 20 | 8.66 |
| 30 | 13.0 |
| 40 | 17.3 |
| 50 | 21.7 |
| 60 | 26.0 |
| 70 | 30.3 |
| 80 | 34.7 |
| 90 | 39.0 |
| 100 | 43.3 |
| 120 | 52.0 |
| 140 | 60.6 |
| 160 | 69.3 |
| 180 | 78.0 |
| 200 | 86.6 |
| 250 | 108 |
| 300 | 130 |
| 350 | 152 |
| 400 | 173 |
| 500 | 217 |
| 600 | 260 |
| 700 | 303 |
| 800 | 346 |
| 900 | 390 |
| 1000 | 433 |
Source: engineeringtoolbox.com
Head and Pressure for Different Liquids
The pressure developed by a pump depends on the fluid's specific gravity (SG), even if the developed head (ft) is identical. The following table illustrates this for a head of 100 ft.
Liquid | Specific Gravity(SG) | Head(ft) | Pressure(psi) |
|---|---|---|---|
| Water | 1.0 | 100 | 43.3 |
| Kerosene | 0.8 | 100 | 36.6 |
| Sulphuric Acid | 1.8 | 100 | 77.9 |
Source: engineeringtoolbox.com
Key Insight: Head vs. Pressure
Identical pumps running at the same speed will develop the same head regardless of the fluid being pumped. However, the discharge pressure will vary significantly because pressure is a function of both the head and the fluid's density (specific gravity). This is why pump performance curves are typically plotted in terms of head (feet or meters) rather than pressure (psi or bar). Using head makes the curve universally applicable to any fluid, simplifying system design and pump selection.