Differential Pressure Calculator

Compute pressure differences for flows and fluid columns. Switch units, compare methods, quickly export results. Designed for quick checks and accurate reporting every time.

Pick the model that matches your measurement setup.
Typical range: 0.6–1.0 depending on geometry.
If you have only one velocity, keep v1 = 0.
Used for the fluid-column method. Default is standard gravity.
Result appears above the form after submission.

Formula used

Notes: Real systems add losses from fittings, roughness, compressibility, and elevation changes. Use the method that matches your instrument and assumptions.

How to use this calculator

  1. Select a calculation method matching your setup.
  2. Enter values and choose their units in each field.
  3. Set the output unit you want for reporting.
  4. Click the calculate button to display the result.
  5. Use the CSV or PDF buttons to export your run.

Example data table

Scenario Inputs Computed ΔP
Direct difference P1 = 120 kPa, P2 = 95 kPa 25 kPa
Fluid column ρ = 1000 kg/m³, g = 9.80665 m/s², Δh = 0.35 m 3432 Pa
Dynamic / Pitot ρ = 1.225 kg/m³, v2 = 25 m/s, v1 = 0 m/s 383 Pa
Restriction estimate ρ = 998 kg/m³, Q = 0.006 m³/s, A = 0.00025 m², Cd = 0.62 ~ 1.85×106 Pa
Example values are illustrative. Use measured geometry and coefficients for design work.

Differential pressure in practical measurements

1) What differential pressure represents

Differential pressure (ΔP) is the pressure difference between two points in a system. In piping and ducts, it is commonly used to infer flow, detect filter loading, or quantify losses across equipment. Because ΔP can be positive or negative, always define a clear “high” and “low” side before recording data.

2) Typical unit ranges you may encounter

Instrumentation spans wide ranges. HVAC work often uses inches of water (inH2O) or Pascals, where 0.5 inH2O ≈ 125 Pa. Process piping frequently reports kPa or bar, and restriction devices can reach hundreds of kPa under high flow. This calculator supports common reporting units for quick comparison.

3) Fluid-column method and manometer data

For a static fluid column, ΔP = ρ g Δh. With water at ρ ≈ 1000 kg/m³ and g ≈ 9.80665 m/s², each 1 cm height difference corresponds to about 98.1 Pa. For mercury (ρ ≈ 13,595 kg/m³), 1 mm corresponds to roughly 133 Pa, matching the mmHg convention.

4) Dynamic pressure and Pitot-style readings

In gases and liquids, a Pitot tube relates velocity to dynamic pressure: ΔP = ½ ρ v². For air at ρ = 1.225 kg/m³ and v = 25 m/s, dynamic pressure is about 383 Pa. If you compare two velocities, the calculator uses ½ρ(v2² − v1²) to isolate the change.

5) Restriction estimates from flow and geometry

When you know flow rate Q, an effective flow area A, and a discharge coefficient Cd, the estimate ΔP = (ρ/2)(Q/(Cd·A))² provides a fast check. Small areas make ΔP rise sharply because velocity scales as Q/A. Use realistic Cd values (often 0.6–1.0) to avoid overestimating.

6) Interpreting sign, direction, and reference points

Direct subtraction uses ΔP = P1 − P2, so the sign depends on which pressure you place in P1. For hydrostatic setups, the sign depends on how you define Δh. In reporting, document the tap locations and elevation direction so results are reproducible.

7) Data quality, uncertainty, and calibration

Accuracy depends on sensor range and resolution. A ±0.5% full-scale transmitter on a 10 kPa range yields ±50 Pa uncertainty, which is significant for low-pressure air systems but minor for high-pressure liquid lines. Zeroing, temperature effects, and impulse line condition can dominate errors.

8) Choosing the right method for your scenario

Use the direct method for two known pressures, the fluid-column method for manometers, the dynamic method for velocity-related measurements, and the restriction estimate for quick engineering checks. For design-critical work, validate with standards and include additional losses from fittings and roughness.

FAQs

1) Can ΔP be negative?

Yes. A negative value simply means the “low” side is higher than the “high” side based on your input order. Swap P1 and P2 if you want a positive convention.

2) Which method should I use for a U-tube manometer?

Use the fluid-column method (ρ g Δh). Enter the manometer fluid density and the measured height difference, then select your preferred output unit for reporting.

3) Why does the restriction method sometimes give very large values?

ΔP grows with the square of velocity. If area A is small, Q/(Cd·A) becomes large, producing a large ΔP. Double-check geometry, Cd, and that Q is in the correct unit.

4) How do I use the Pitot option?

Enter fluid density and velocity. If you have a baseline velocity, enter it as v1; otherwise keep v1 at zero. The result represents the dynamic pressure change.

5) Does this include friction losses in pipes?

No. The calculator focuses on core ΔP relationships and simple estimates. For pipe friction and minor losses, use a dedicated head-loss model and sum losses across components.

6) What density should I use for gases?

Use density at operating conditions. For air, 1.225 kg/m³ is a common sea-level reference, but temperature, humidity, and pressure can change density and therefore ΔP predictions.

7) Why do my readings drift near zero?

Near-zero ΔP is sensitive to sensor zero offset, temperature changes, and vibration. Re-zero the transmitter, inspect impulse lines, and ensure the selected range gives adequate resolution.

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Important Note: All the Calculators listed in this site are for educational purpose only and we do not guarentee the accuracy of results. Please do consult with other sources as well.