Technical Specification and Selection Guide of Control Valve

Created on 10.21

I. Applicable Standards

Standard Type
Standard No. and Title
International Standard
ASME B16.34
Valves — Flanged, Threaded, and Welding End
International Standard
ASME B16.104
Control Valve Seat Leakage
International Standard
IEC 60534-2-4, IEC 60534-3-1 — Control valve flow capacity and face-to-face dimensions
Domestic Standard
GB/T 4213
Pneumatic Control Valves
Test Standard
API 598, ISO 5208 — Valve inspection and pressure testing
Reference Standard
GB/T 17213.2
Industrial-process control valves — Flow capacity — Sizing equations for fluid flow under installed conditions
Note: JB/T 5296-1991 Test Methods for Flow Coefficient of General Valves was withdrawn in 2017 and is no longer listed.

II. Structural Principle

The eccentric rotary control valve consists of an eccentric rotary valve body throttling assembly and a pneumatic actuator.
Working Principle: The spherical plug and the valve shaft are designed with an eccentricity. When the valve shaft rotates, the plug moves eccentrically along a cam trajectory. When the valve closes, the flexible arm of the plug undergoes elastic deformation and tightly contacts the seat to form a seal. The 50° angular travel provides opening and closing with inherent shearing and anti-jamming capability, making it suitable for fibrous, particulate, and high-viscosity media. It is therefore also called a camflex valve.
Actuator Selection
Model
Structural Type
Applicable Service
PDR
Spring-return rolling diaphragm type
Conventional service, fail-safe applications
PCR
Double-acting piston type
Large diameter, high differential pressure, severe service

Core Design Advantages

Design Feature
Technical Advantage
Straight-through body flow passage
Low flow resistance, high flow capacity
50° angular travel
Fast open/close response, good control linearity
Integral body and bonnet
Reduced external leakage points
Involute spline
Good centering, high torque transmission capability
Symmetrical window design
Air-to-open / air-to-close freely interchangeable on site
Eccentric shearing structure
Anti-jamming by particles, suitable for viscous media
Compact and lightweight
Can be installed at any angle, easy maintenance

III. Three Sealing Structures and Allowable Pressure Drop

1. Sealing Structure Definitions

Sealing Type
Structural Definition
Abbreviation
TS
O-ring embedded in seat, soft-seated structure
Soft Seal
SS
Local Stellite hardfacing overlay on plug and seat
Partial Hard Seal
SF
Full Stellite hardfacing overlay on plug and seat
Full Hard Seal
As described above, TS indicates an O-ring clamped in the seat; SS indicates Stellite hardfacing applied to the sealing areas of the plug and seat (partial overlay); SF indicates full Stellite hardfacing on both plug and seat (full overlay).
2. Performance Comparison
Sealing Type
Leakage Class
Applicable Temperature
Wear and Erosion Resistance
Applicable Media / Scenarios
Advantages and Disadvantages
TS Soft Seal
ASME B16.104 Class VI (bubble-tight zero leakage)
-45 to 230°C
Moderate; not resistant to particle erosion
Clean gas, clean water, non-corrosive clean media
Best sealing performance, low cost; low temperature limit, prone to aging
SS Partial Hard Seal
ASME B16.104 Class IV
-195 to 400°C
Moderate; resistant to slight particulate
Ordinary oil products, steam, mildly corrosive media
Good cost-effectiveness; balanced sealing and wear resistance
SF Full Hard Seal
ASME B16.104 Class IV
-195 to 400°C
Excellent; resistant to erosion, crystallization, and particles
Media containing fibers, particles, high viscosity, high temperature, severe corrosion
Longest service life, widest service adaptability; relatively high cost
Leakage Class Notes: Class VI is bubble-tight sealing with extremely low leakage. Class IV is the normal achievable level for metal-seated valves; the leakage is 0.01% of rated Cv and is not zero leakage. Metal hard seals are not intended to achieve bubble-tight sealing; Class IV is a reasonable expectation for metal-to-metal sealing.

3. Allowable Pressure Drop Rules

Sealing Type
Differential Pressure Capability
Air Supply / Actuator Selection Constraints
TS Soft Seal
Lowest; more than 30% lower than hard seal at the same size
Suitable for conventional PDR spring actuators; high differential pressure and particulate service strictly prohibited
SS Hard Seal
Moderate; sufficient differential pressure margin
PDR or PCR both acceptable; general medium-high differential pressure service
SF Full Hard Seal
Highest; best differential pressure resistance
Large diameter preferably with PCR piston actuator; first choice for high differential pressure and erosion service
Key Constraints:
  • Actual shutoff differential pressure must not exceed the manufacturer's catalog table value.
  • Inlet pressure must not exceed the body ANSI class temperature-pressure rating.
  • Allowable differential pressure for gas media is greater than that for liquid media.

IV. Main Technical Performance Parameters

Item
Technical Specification
Size Range
1″ to 12″ (DN25 to DN300)
Pressure Class
ANSI 150 / 300 / 600 LB
Applicable Temperature
Depends on sealing type: TS soft seal -45 to 230°C; SS/SF hard seal -195 to 400°C
Basic Error (with positioner)
±2% (reference GB/T 4213; refer to manufacturer's catalog for details)
Basic Error (without positioner)
±5%
Hysteresis (with positioner)
1%
Hysteresis (without positioner)
3%
Dead Band (with positioner)
1%
Dead Band (without positioner)
5%
Rangeability
100:1 (refer to specific manufacturer's catalog; some models 50:1)
Inherent Flow Characteristic
Linear
Connection Type
Wafer type (recommended), flanged type
Coating
Carbon steel: PLA9006 silver-white; stainless steel: unpainted

V. Design Calculation

1. Rated Cv Flow Coefficient Table

Size (in)
Full Cv
60% Stroke Cv
40% Stroke Cv
20% Stroke Cv (Metal Seat Only)
1
14
8.4
5.6
2.8
1-1/2
30
18
12
6.0
2
50
30
20
10
3
135
81
54
—
4
230
138
92
—
6
500
300
200
—
8
850
510
340
—
10
1300
780
520
—
12
1750
1050
700
—
The Cv values in the table are typical product data. Products of the same size from different manufacturers may differ; the manufacturer's catalog shall govern during selection.

2. Service Cv Calculation

Liquid Media (non-choked flow, no flashing/cavitation):
​
Where:
Q = volumetric flow rate (m³/h)
ρ = relative density (relative to water, dimensionless)
ΔP = pressure drop across the valve (bar)
Applicable Premise: This simplified formula is applicable to non-choked flow with Newtonian fluids. If flashing or cavitation exists, the pressure recovery factor FLFL​ and critical pressure drop must be introduced for correction in accordance with IEC 60534-2-1 (GB/T 17213.2); this formula cannot be applied directly.
Gas Media: Calculate according to the dedicated formulas for low-pressure or high-pressure compressed gas, with correction for operating temperature and pressure. For the discrimination between low-pressure gas (ΔP<0.5P1ΔP<0.5P1​) and choked flow, as well as the values of expansion factor YY and pressure drop ratio factor XTXT​, refer to IEC 60534-2-1 or GB/T 17213.2.

3. Cv Selection Principles

Selection Range
Service Suitability
40%–60% stroke
Optimal control range; good linearity, no oscillation
< 10%
Small opening prone to oscillation and inaccurate control; selection must not fall within this range
> 80%
Large opening with flow saturation; insufficient load control margin

4. Allowable Pressure Drop Verification

Verification Dimension
Verification Content
Structural Type
Metal seat / soft seat; carbon steel / stainless steel body
Actuator
PDR spring-return / PCR double-acting piston
Service Conditions
Air supply pressure, flow-to-open / flow-to-close, gas / liquid medium
Boundary Limits
Actual differential pressure ≤ manufacturer's catalog table value; inlet pressure not exceeding body rated pressure

5. Valve Body Material Temperature-Pressure Applicability

Body Material
Applicable Temperature
Applicable Pressure Class
Notes
WCB Carbon Steel
-29 to 425°C
150 / 300 / 600 LB
Above 425°C prone to graphitization
CF8 (304)
-195 to 400°C
All classes
Mild corrosion, low-temperature service
CF8M (316)
-195 to 400°C
All classes
Acid/alkali, severe corrosion service

6. Packing Temperature and Pressure Limits

Packing Type
Applicable Temperature Range
Applicable Service
Reinforced PTFE
-45 to 230°C
Ambient temperature, no high-temperature service
Flexible Graphite
-196 to 538°C
High/low temperature, steam, corrosive service

VI. Standard Material Combinations

Body Material
Plug / Seat Configuration
Stem Material
Applicable Service
WCB
304SS / SS / SF / TS
304 nitrided
Water, steam, ordinary oil products
CF8
CF8M / SS / SF
316SS / 17-4PH
Mild corrosion, low-temperature media
CF8M
CF8M / SS / SF / TS
316SS
Acid/alkali, severe corrosion, high temperature

VII. Common Faults, Causes, and Remedies

Fault Phenomenon
Fault Cause
Remedial Measure
Poor control accuracy, large flow fluctuation
Positioner improperly calibrated; air supply pressure fluctuation; long-term operation at small opening; medium impurities causing jamming
Recalibrate zero and span; install air supply pressure regulator; recalculate Cv and reselect; disassemble and clean foreign matter from plug
Excessive internal leakage
TS seal ring aging; SS/SF sealing surface erosion and wear; plug flexible arm fatigue; debris stuck on sealing surface
Replace O-ring soft seal; lap or upgrade to full hard seal SF; replace plug assembly; install upstream filter
Slow action, sticking
Packing over-tightened; stem corrosion; connecting rod coaxiality deviation; actuator diaphragm/piston wear
Moderately loosen packing gland; polish stem and apply anti-corrosion treatment; align transmission linkage; replace actuator seals and diaphragm
Actuator air leakage, loss of position
Diaphragm aging or damaged; joint seal failure; spring fatigue; water/oil contamination in air supply
Replace diaphragm and gaskets; reseal piping connections; replace spring assembly; install air supply dryer/filter
Air-to-open / air-to-close switching failure
Incorrect assembly of body symmetrical windows; directional deviation of rocker arm linkage
Reassemble linkage according to OEM structure; re-switch air-to-open / air-to-close mode on site
High operating noise
Excessive differential pressure; flow velocity over limit; throttling vortex
Use multi-stage pressure reduction; appropriately increase valve size; optimize piping flow pattern

VIII. Routine Maintenance and Servicing Schedule

Maintenance Interval
Maintenance Content
Daily Inspection
Check air supply pressure, valve stroke, external leakage, and abnormal operating noise
Every Six Months
Positioner calibration, air supply filter cleaning, packing tightening, bolt re-tightening
Annual Maintenance
Disassembly inspection of plug and seat wear, actuator seal replacement, full-stroke calibration
Spare Parts Stocking
O-rings, packing, diaphragm, positioner filter element, seat seal assembly
Warranty Period
18 months after shipment or 12 months after installation, whichever comes first; free repair or replacement for manufacturing defects

IX. Summary of Selection and Application Points

The core selection logic for eccentric rotary control valves can be summarized in three points:
First, select the sealing type according to the medium.
  • For clean media requiring bubble-tight sealing, select
TS soft seal.
  • For ordinary oil products, steam, and media with slight particulate, select
SS partial hard seal.
  • For media containing fibers, particles, high viscosity, high temperature, and severe corrosion, select
SF full hard seal.
Second, select the actuator according to differential pressure.
  • Soft seals have the lowest differential pressure capability and are strictly prohibited for high differential pressure service.
  • SF full hard seals have the strongest differential pressure resistance; for large diameter and high differential pressure, prioritize
PCR double-acting piston actuators.
Third, determine the material according to service conditions.
  • WCB
is suitable for water, steam, and ordinary oil products.
  • CF8
is suitable for mild corrosion and low-temperature service.
  • CF8M
is suitable for acid/alkali, severe corrosion, and high-temperature service.
  • For packing,
Ambient temperature applications use reinforced PTFE, while high/low temperature, steam, and corrosive services use flexible graphite.
In field operation, the most critical concern is long-term operation at small opening—this not only results in poor control accuracy but also accelerates erosion of the plug and seat. If the valve is found to operate below 10% opening for extended periods, it indicates that the Cv is oversized and the selection should be recalculated. In addition, if there is a risk of flashing or cavitation in liquid media, the simplified formula cannot be used directly for Cv calculation; choked flow verification must be performed in accordance with IEC 60534-2-1.
Eccentric rotary control valve with pneumatic diaphragm actuator installed in a petrochemical plant pipeline
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