Accurately select check valve size using flow, pressures, and fluid data today. Get Cv, velocity, pressure loss, and a recommended nominal diameter instantly here.
Meta words: 25/25 Tagline words: 24/24
This tool uses the standard liquid sizing relationship between flow, pressure drop, and valve capacity. For a quick check valve selection, it compares the Cv you need against typical Cv values by nominal size.
Style factor adjusts available Cv to reflect different internal designs and losses.
| Scenario | Flow | SG | Allowable ΔP | Style | Required Cv | Suggested NPS | Velocity (approx) |
|---|---|---|---|---|---|---|---|
| Domestic water riser | 250 gpm | 1.00 | 5 psi | Swing | 111.8 | 3 in | ~7–9 ft/s |
| Chilled water loop | 120 gpm | 1.00 | 3 psi | Dual-plate | 69.3 | 2.5 in | ~5–7 ft/s |
| Process water branch | 40 gpm | 1.05 | 2 psi | Lift | 29.0 | 2 in | ~3–5 ft/s |
Examples are illustrative; confirm with actual valve Cv and project criteria.
Check valves protect building piping by allowing flow in one direction while reducing the chance of backflow, pump reverse rotation, and unwanted drain-down. In domestic water, chilled water, condenser water, and fire protection branches, the most common sizing mistake is selecting a valve only by pipe diameter. A check valve behaves like a flow restriction, so performance depends on the valve’s capacity rating and the allowable pressure loss in your design.
Capacity is commonly expressed as Cv (or Kv in metric). Cv links flow rate and pressure drop, letting you estimate whether the valve will pass the required flow without consuming too much system head. When the valve is undersized, pressure loss rises quickly, reducing delivered flow and increasing pump energy. When the valve is oversized, the disc may chatter, close slowly, or fail to stabilize at low velocity, which can increase wear and noise.
Practical sizing also checks velocity. Higher velocity can increase noise, vibration, and water hammer severity during rapid closure events. Low velocity can reduce self-cleaning and may allow debris to settle at the seat. A balanced selection targets your project’s acceptable ΔP while keeping velocity in a comfortable range for the service, material, and expected solids content.
This calculator estimates the required Cv from your design flow, specific gravity, and allowable pressure drop. It then compares that requirement with typical Cv values by nominal size, adjusted by an internal style factor. Use the result as a screening step, then confirm the final selection against the manufacturer’s published Cv curve for the exact valve model, pattern, and end connections.
Suppose a domestic water riser requires 250 gpm, with SG = 1.00 and allowable ΔP = 5 psi. The required capacity is: Cv = 250 / √(5/1.00) ≈ 111.8. A swing-style valve typically meets this around a 3 in nominal size using representative Cv data. The calculator also reports an approximate line velocity using a typical Schedule 40 inside diameter to support a quick reasonableness check.
For critical systems, also evaluate minimum cracking pressure, installation orientation, accessibility for maintenance, and the risk of slam during pump trips. When surge is a concern, consider faster-closing designs, damped mechanisms, or a detailed transient analysis. In fire protection lines, coordinate valve loss with hydraulic calculations and verify that the selected check valve meets listing requirements, orientation limits, and inspection access needs.
Cv is a capacity rating that relates flow to pressure drop for liquids. Higher Cv means less restriction at a given flow. Always confirm the exact Cv from the chosen manufacturer and model.
Not always. Matching the pipe can work, but it may over- or under-restrict flow. Use allowable pressure drop, expected flow, and stability at low flow to select an appropriate size.
Different designs create different internal losses. Swing valves often have lower losses than lift or piston designs. The style factor in this tool is a simplification to reflect that behavior.
It depends on service, material, and noise limits. Many designs aim for moderate velocities to reduce erosion and water hammer risk. Use your project criteria and local standards for final limits.
You can use it as a rough screen, but gas sizing is more complex because density changes with pressure and temperature. For final selection, use manufacturer gas equations and service conditions.
Cracking pressure is the differential pressure required to start opening the valve. If it is too high, low-flow branches may not open fully. Check published data when flows can be small.
Confirm Cv on the exact model, verify ΔP at design and minimum flow, check installation orientation and maintenance access, and evaluate surge risk. Document the basis and export results for review.
Use engineering judgment and manufacturer data before final selection.
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.