Valve Cv (Flow Coefficient) Table & Calculator

Complete Cv reference for Gate, Globe, Ball, Butterfly & Check valves from DN 15 to DN 600 (NPS ½" to 24"). Use the interactive calculator and sizing formulas below for accurate valve selection.

Last updated: March 2026 • Data per ISA/IEC 60534, API 598 & manufacturer test reports

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Typical Valve Cv Values — DN 15 to 600

Valve Flow Coefficient (Cv) Table for Gate, Globe, Ball, Butterfly, and Check Valves from DN 15 to DN 600
DN (mm) NPS (inch) Valve Type Cv Kv (m³/hr) Flow Rate
(m³/hr @ 1 bar)
% Full Bore Typical Application

Engineering Note: Cv values shown are typical full-open values for standard-port designs and may vary ±15% based on manufacturer, trim design, and seat configuration. Always verify against the manufacturer's certified Cv data sheet for critical sizing. Reduced-port valves will have lower Cv values.

Cv is measured per ISA-75.02 / IEC 60534-2-3. Flow rates assume water at 15°C (60°F), SG = 1.0, ΔP = 1 bar.

Cv vs. DN by Valve Type

Ball and Butterfly valves provide the highest Cv (least flow restriction) for any given DN. Globe valves offer the lowest Cv due to their tortuous flow path, making them ideal for throttling applications where pressure drop control is desired.

Flow Rate Calculator

Enter known parameters to calculate flow rate or required Cv. Supports liquids and gases.

Liquid Flow Rate from Cv

Required Cv from Flow Rate

Cv Sizing Formulas

Industry-standard equations per ISA-75.01 / IEC 60534-2-1 for valve sizing across different fluid types.

Liquids (Incompressible)

Q = Cv × √(ΔP / SG)
Q
Flow rate in US GPM
Cv
Flow coefficient
ΔP
Pressure drop across valve (psi)
SG
Specific gravity (water = 1.0)

Gas / Air (Subcritical)

Q = 963 × Cv × N × √(ΔP × (P1+P2) / (T × SG))
Q
Flow rate in SCFH
P1, P2
Upstream / downstream pressure (psia)
T
Absolute temperature (°R = °F + 460)
SG
Gas specific gravity (air = 1.0)
N
Numerical constant (varies by units)

Steam

W = 63.3 × Cv × √(ΔP × γ)
W
Mass flow rate in lb/hr
ΔP
Pressure drop across valve (psi)
γ
Steam density at inlet (lb/ft³)
Cv
Flow coefficient

For superheated steam, use degree of superheat correction factor.

Cv / Kv Conversion Reference

Cv → Kv

Kv = 0.865 × Cv

Kv is the metric flow coefficient (m³/hr of water at ΔP = 1 bar)

Kv → Cv

Cv = 1.156 × Kv

Used when converting European valve data to ANSI/ISA standards

Cv → Flow Rate

Q (m³/hr) = Kv × √(ΔP / SG)

Where ΔP is in bar and SG relative to water

Quick Cv to Kv conversion lookup table
CvKv (m³/hr)CvKv (m³/hr)CvKv (m³/hr)
10.875043.31000865
54.3310086.520001730
108.6520017350004325
1513.0300260100008650
2521.65004332000017300

Valve Type Comparison for Engineers

Selecting the right valve type depends on your application requirements. This comparison covers key engineering parameters.

Engineering comparison of Gate, Globe, Ball, Butterfly, and Check valve characteristics
Parameter Gate Globe Ball Butterfly Check (Swing)
Relative Cv (same DN) High Low Highest High Medium
Throttling Ability Poor Excellent Fair (V-port: Good) Fair Not applicable
Shut-off (Leakage Class) Class IV–V Class IV–V Class VI (zero leakage) Class IV–VI Class II–IV
Pressure Drop (full open) Very Low High Very Low Low Medium
Operating Torque High (multi-turn) Medium (multi-turn) Low (quarter-turn) Low (quarter-turn) N/A (self-acting)
Actuator Suitability Electric, Pneumatic Electric, Pneumatic, Diaphragm Pneumatic, Electric Pneumatic, Electric N/A
Flow Characteristic Quick opening Linear / Equal % Modified equal % Equal percentage N/A
Max Temperature Up to 650°C Up to 650°C Up to 350°C (soft seat) / 550°C (metal seat) Up to 300°C (rubber) / 600°C (metal) Up to 550°C
Best For On/off isolation, pipelines Throttling, flow control Quick shut-off, tight sealing Large-diameter isolation Backflow prevention
Key Standard API 600, BS 1414 API 623, BS 1873 API 608, BS 5351 API 609, BS EN 593 API 594, BS 1868

Valve Selection Guide

Use this decision framework to select the optimal valve type for your process conditions.

On/Off Isolation

Recommended: Gate Valve (small bore), Butterfly Valve (large bore), Ball Valve (critical sealing)

Prioritize low ΔP and high Cv. Avoid globe valves for isolation-only service.

Flow Throttling & Control

Recommended: Globe Valve (best), V-port Ball Valve, Butterfly with positioner

Globe valve's linear/equal-% characteristic offers the most predictable control. Check rangeability (≥50:1 for globe).

High Flow / Low ΔP

Recommended: Full-bore Ball Valve, Butterfly Valve

Maximum Cv with minimal flow restriction. Ball valves offer near-zero pressure drop when fully open.

Critical / Severe Service

Recommended: Metal-seated Ball Valve, Bellow-seal Globe Valve

For high temperature, high pressure, toxic, or fugitive emissions control. Consider API 624 / ISO 15848 certified valves.

Engineering FAQs

Cv is the flow coefficient that represents the volume of water (in US GPM) at 60°F that will flow through a valve with a pressure drop of 1 psi. A higher Cv means a larger flow capacity and less resistance to flow. It is the most critical parameter for valve sizing and is standardized by ISA-75.01 and IEC 60534.

Kv = 0.865 × Cv. Kv is the metric equivalent of Cv and represents the flow of water in m³/hr at a pressure drop of 1 bar. Conversely, Cv = 1.156 × Kv. European and Asian manufacturers often publish Kv values while North American manufacturers use Cv.

Full-bore ball valves typically offer the highest Cv values for a given pipe size because they provide an unobstructed, straight-through flow path. Butterfly valves also offer high Cv in a compact design. Globe valves have the lowest Cv because their tortuous S-shaped flow path creates the most resistance.

A full-bore (full-port) valve has an internal bore diameter equal to the pipe ID, yielding maximum Cv. A reduced-bore valve has a smaller opening (typically one pipe size down), resulting in Cv values that are 60–75% of the equivalent full-bore valve. Reduced-bore valves are lighter, cheaper, and often acceptable for non-critical applications where some pressure drop is tolerable.

If the pressure at the vena contracta drops below the liquid's vapor pressure, cavitation occurs — causing noise, vibration, and rapid erosion of valve internals. When sizing for cavitation-prone service, the actual ΔP used in the Cv formula must be limited to the allowable ΔP (ΔP_allowed = FL² × (P1 - FF × Pv)), where FL is the liquid pressure recovery factor and Pv is the vapor pressure. Anti-cavitation trim designs (multi-stage, caged) effectively reduce FL and allow higher pressure drops.

Industry best practice recommends selecting a valve where the required Cv falls between 60–80% of the valve's rated Cv at full open. This provides a safety margin for process upsets and allows the valve to operate in the most controllable portion of its travel. An oversized valve (operating <20% open) causes poor control, increased wear, and potential instability.

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