Calculate valve Cv/Kv flow coefficients for liquid and gas flow. Size control valves, determine pressure drop, and compare valve capacities.
The Flow Coefficient Calculator determines the Cv (US) or Kv (metric) value for control valves, which quantifies flow capacity. Cv is defined as the flow of water in US gallons per minute at 60°F through a valve with a 1 psi pressure drop. It is the universal sizing parameter for valves in process control, HVAC, and plumbing systems when you need to size a valve from actual flow conditions.
Proper valve sizing is critical — an oversized valve causes poor control and hunting, while an undersized valve limits flow and creates excessive pressure drop. This calculator handles both liquid and gas flow, accounts for specific gravity and temperature, and helps you select the right valve Cv from manufacturer catalogs.
Enter your process conditions to calculate the required Cv, or enter a valve's Cv to determine the flow rate or pressure drop it will produce. The comparison table shows how different valve sizes and types compare in flow capacity.
Use this calculator when you want a valve size that matches the actual flow and pressure-drop requirement instead of picking from a catalog by guesswork. It is useful for process control, HVAC, and plumbing work where sizing errors lead to poor control, wasted capacity, or unstable control loops. That helps you compare candidate valve sizes against the actual operating point more confidently.
Liquid: Cv = Q × √(SG / ΔP). Gas: Cv = Q / (963 × P₁ × √(ΔP/(P₁ × SG × T))). Where Q = flow rate, SG = specific gravity, ΔP = pressure drop (psi), P₁ = inlet pressure (psia), T = temperature (°R). Kv = 0.865 × Cv.
Result: Cv = 31.6
For 100 GPM of water (SG=1.0) with 10 psi pressure drop: Cv = 100 × √(1.0/10) = 100 × 0.316 = 31.6. A 2" globe valve (Cv ~45) would work well, providing 30% overcapacity for control range.
Ball valves offer the highest Cv per pipe size (full bore): 2" ball valve Cv ≈ 100-180. Globe valves have lower Cv but better control: 2" globe Cv ≈ 30-50. Butterfly valves fall in between: 2" butterfly Cv ≈ 60-80. Gate valves are on/off only, not for flow control: 2" gate Cv ≈ 120. Needle valves for fine control: Cv ≈ 0.01-5. Diaphragm valves for slurry: 2" Cv ≈ 50-70.
Gas flow through valves is more complex than liquid. Below critical pressure drop (ΔP < 0.5 × P₁), flow is subcritical and increases with ΔP. Above critical drop (choked flow), increasing ΔP doesn't increase flow — the valve is at maximum capacity. Always check whether your pressure drop exceeds the critical ratio and use choked flow equations accordingly.
ISA/IEC 60534 is the international standard for control valve sizing. It covers liquid flow with viscosity correction, gas/vapor flow with specific heat ratio, two-phase flow, and noise prediction. Manufacturer catalogs provide Cv tables for each valve model, trim type, and opening percentage. Software tools like Emerson Fisher's Valvelink or Flowserve's Limitorque automate complex sizing calculations.
Cv is the US flow coefficient (GPM of water at 1 psi drop). Kv is the metric equivalent (m³/h of water at 1 bar drop). Convert: Kv = 0.865 × Cv. Both quantify valve flow capacity — Cv is standard in North America, Kv in Europe.
Calculate the required Cv for your maximum flow condition. Select a valve with rated Cv about 25-50% higher than required. This allows the valve to operate in its most controllable range (30-80% open) at normal conditions.
An oversized valve (>2× required Cv) operates nearly closed, causing poor control, noise, and accelerated wear. An undersized valve can't deliver required flow and creates excessive pressure drop. Correct sizing is essential for stable control loops.
Yes, for viscous fluids (>20 centistokes), a viscosity correction factor reduces effective Cv. Very viscous fluids may require larger valve bodies. The ISA/IEC 60534 standard provides correction methods for high-viscosity applications.
Cavitation occurs when local pressure drops below the fluid's vapor pressure, forming vapor bubbles that collapse violently. It damages valve internals and creates noise. Avoid by ensuring ΔP doesn't exceed the valve's allowable ΔP for the given upstream pressure.
Cv varies from near-zero at closed to maximum at full open. The characteristic curve (linear, equal percentage, or quick-opening) determines the shape. Equal percentage valves are most common in control applications because they provide constant % change in flow per % change in opening.