Control Valve Seat Leakage Classes (ANSI/FCI 70-2) Explained: 6 Critical Grades That Prevent Dangerous Failures

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Control Valve Seat Leakage Classes (ANSI/FCI 70-2) Explained

A control valve that passes its factory leak test can still fail badly in the field.

The difference usually comes down to whether the right leakage class was specified in the first place.

Class I to VI Explained Live Class V Calculator Real FCI Test Data

Control valve seat leakage classes under ANSI/FCI 70-2 define exactly how much fluid a valve is allowed to leak once it's fully closed, using six standardized grades from loose to bubble tight.

Every control valve leaks a little when closed. That's simply a mechanical fact, since a moving plug can never seal as perfectly as a solid wall.

control-valve-seat-leakage-classes

ANSI/FCI 70-2 exists to put a number on that leakage. It's the standard almost every manufacturer, EPC, and end user references when specifying shutoff performance.

The standard defines six classes, labeled I through VI. Each one sets a maximum allowable leakage rate, tested a specific way, for a specific type of valve construction.

Fisher EH series high pressure control valve rated for Class V seat leakage
Image credit: Emerson (Fisher EH Series Control Valve, rated for Class V shutoff)
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The 6 ANSI/FCI 70-2 Control Valve Seat Leakage Classes

Here are all six classes, in order from loosest to tightest.

I

Class I: No Required Test

Same design intent as Class II, III, or IV, but no shop leak test is performed by agreement between user and supplier.

II

Class II: 0.5% of Rated Capacity

Typical of commercial double seat valves or balanced single seat valves with a piston ring seal.

III

Class III: 0.1% of Rated Capacity

Same basic construction as Class II, but built to a tighter seat and seal tolerance.

IV

Class IV: 0.01% of Rated Capacity

The standard for most metal seated single seat control valves in general industrial service.

V

Class V: A Precise Volumetric Limit

Set as 0.0005 mL of water per minute, per inch of port diameter, per psi of differential pressure. Needs lapped metal seats.

VI

Class VI: Bubble Tight, Soft Seated

Measured in bubbles per minute using air or nitrogen. Requires a resilient seat material like PTFE.

Metal Seated vs Soft Seated: Which Classes Apply

Not every valve construction can reach every class. The seat material draws a hard line partway through the list.

Metal Seated Valves

Can reach Class II through Class V. Class V needs hardfaced, precision lapped seats to hold that volumetric limit.

High temperature, high pressure service
💧

Soft Seated Valves

Reach Class VI using PTFE, RTFE, PEEK, or elastomer seating. Not suited to very high temperatures.

Toxic and hazardous gas isolation
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Why Actuator Thrust Decides Whether a Valve Actually Meets Its Class

A valve rated Class V on paper still needs real mechanical force to achieve that rating in the field.

The plug has to be driven hard into the seat to crush any microscopic gap. That force comes entirely from the actuator.

Undersized actuator: valve throttles fine, but seat leakage is worse than rated
Correctly sized actuator: seating force matches the manufacturer's requirement
Tight shutoff mode: positioner dumps air fully below a threshold to maximize seating force

A valve engineered for Class V will perform like a Class IV, or worse, if the actuator's final seating thrust is undersized. The leakage class on the datasheet means nothing without the force to back it up.

Common commissioning finding on tight shutoff service

Class V Leakage Formula and Worked Example

Class V is defined by an exact formula, not a percentage of flow capacity.

Class V Maximum Allowable Leakage
Q = 0.0005 x D x ΔP
Where Q = leakage in mL of water per minute
D = port diameter in inches
ΔP = differential pressure in psi across the closed valve

Example: D = 4 inches, ΔP = 500 psi
Q = 0.0005 x 4 x 500
Q = 1.0 mL per minute

Control Valve Seat Leakage Class Comparison Table

Here's how all six classes compare side by side, including the test method used for each.

ClassMax LeakageTest MediumTypical Seat Type
INo test requiredN/ASame as II, III, or IV
II0.5% of rated CvAir or water, 45 to 60 psiMetal to metal
III0.1% of rated CvAir or water, 45 to 60 psiMetal to metal
IV0.01% of rated CvAir or water, 45 to 60 psiMetal to metal
V0.0005 mL/min per inch per psiWater at max operating dPLapped metal seat
VIBubbles per minute by port sizeAir or nitrogen, up to 50 psiSoft seat (PTFE, elastomer)

Class VI Bubble Rate by Port Diameter

Class VI leakage scales with valve size. A bigger port is allowed more bubbles per minute.

Nominal Port SizeMax Bubbles per Minute
1 inch or smaller1
1.5 to 2 inch2 to 3
3 inch6
4 inch11
6 inch27
8 inch45
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Live Class V Seat Leakage Calculator

Enter port diameter and differential pressure to calculate the maximum allowable Class V leakage rate.

🧮 Class V Leakage Calculator
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Max Leakage (mL/min)

Where Each Leakage Class Gets Specified

💧

Class II/III

General utility water, air, and steam services where minor leakage is acceptable.

🏭

Class IV

Standard modulating loops: temperature, pressure, and flow control.

🔥

Class V

High pressure steam letdown and boiler feedwater level control.

Class VI

Toxic gas, hazardous chemical, and ESD valve isolation service.

Refining

Hydrocarbon processing units needing tight shutoff on shutdown.

🏭

Power Generation

Steam turbine bypass and drain valve applications.

ANSI/FCI 70-2 vs API 598: Not the Same Standard

Engineers sometimes specify FCI 70-2 classes on gate or globe isolation valves. That's a mistake worth avoiding.

FCI 70-2 was written specifically for control valves that throttle. API 598 governs on and off valves meant for true isolation.

Mixing the two leads to the wrong test procedure being applied. It can also create a false sense of confidence in a valve's actual shutoff performance.

If a project genuinely needs zero visible leakage, API 598 is the correct standard to call out, not FCI 70-2.

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Do's and Don'ts When Specifying Seat Leakage Class

✓ Do

  • Match the class to the actual process risk, not the tightest option available
  • Size the actuator's final seating thrust to the manufacturer's stated requirement
  • Install a dedicated block valve if true isolation, not just control, is needed
  • Specify Class V for high differential pressure steam and boiler feedwater service

✗ Don't

  • Default to Class VI everywhere regardless of temperature limits
  • Assume a control valve can replace a proper isolation valve for LOTO
  • Ignore actuator sizing when specifying a tight shutoff class
  • Confuse ANSI/FCI 70-2 with API 598, which governs isolation valves instead

Reference Materials on Control Valve Seat Leakage

PDF
ANSI/FCI 70-2 Informational Sheet
Fluid Controls Institute: official summary of the leakage standard
PDF
Fisher ET, EAT, and ETR Control Valve Bulletin
Emerson: shutoff classifications per ANSI/FCI 70-2 and IEC 60534-4

FAQs on Control Valve Seat Leakage Classes

What is the most common seat leakage class for control valves?
Class IV is the default for most metal seated control valves in general industrial service, allowing 0.01% of rated capacity as maximum leakage.
Can a metal seated valve achieve Class VI?
Not reliably. Class VI is built around the elasticity of a soft seat material, and bare metal seats develop microscopic imperfections that let gas escape over repeated cycles.
Does a higher class number always mean a tighter seal?
Generally yes from II through VI, but Class V and Class VI use different units, volumetric leakage versus bubble rate, so they aren't directly comparable number for number across all valve sizes.
Why do control valves need a separate leakage standard from isolation valves?
A control valve's plug must move freely for throttling, which makes a perfect seal mechanically difficult, so ANSI/FCI 70-2 defines an accepted leakage allowance instead of the near zero leakage that API 598 demands from isolation valves.
Can a control valve replace a manual block valve for maintenance isolation?
No. Even a Class VI control valve should never be relied on alone for lockout tagout isolation, since a dedicated upstream block valve is the correct way to secure a line for maintenance.
Why does Class IV leakage damage high pressure steam valves?
At high differential pressure, even 0.01% leakage can accelerate through the tiny gap at near sonic velocity, wire drawing and eroding the seat, which is exactly why high pressure steam service upgrades to Class V.

External References

What we learn today

  • ANSI/FCI 70-2 defines 6 control valve seat leakage classes, from Class I with no test to Class VI, bubble tight.
  • Classes II, III, and IV use a percentage of rated valve capacity, while Class V uses an exact volumetric formula and Class VI uses bubbles per minute.
  • Metal seats reach up to Class V, while Class VI needs a soft seat material like PTFE.
  • Actuator seating thrust is what actually delivers the rated leakage class in the field, not the seat design alone.
  • ANSI/FCI 70-2 applies to control valves specifically, not isolation valves, which instead follow standards like API 598.
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