Control Valves

The Final Control Element in Process Automation

A control valve is not simply a valve with an actuator bolted on. It is an engineered system—the final control element that executes the commands of the plant control system (DCS, PLC, or SCADA) to regulate pressure, flow, level, or temperature in a process. While manual and on/off actuated valves isolate and direct flow, the control valve modulates it continuously, positioning its closure member at any point between fully open and fully closed to maintain a precise process setpoint.

In oil and gas operations, control valves are found in every process unit: controlling feed to distillation columns, regulating steam to reboilers, managing pressure in separator gas outlets, adjusting fuel gas to fired heaters, and protecting compressors from surge. A poorly selected or undersized control valve degrades process performance, wastes energy, and in the worst case, causes trips and shutdowns.

Hoger Sanat Pars supplies complete control valve packages—body, trim, actuator, positioner, and all accessories—from qualified global manufacturers. Every package is supplied with full material certification, hydrostatic and seat leakage test records, actuator bench-set data, positioner calibration certificates, and functional test documentation.


How a Control Valve Works

The control loop operates as follows:

  1. sensor (pressure transmitter, temperature element, flow meter, level transmitter) measures the process variable.
  2. The controller (DCS or PLC) compares the measured value to the desired setpoint and calculates the required corrective action.
  3. The controller sends a signal (typically 4-20 mA or digital via HART/Fieldbus/Profibus) to the control valve.
  4. The positioner receives the signal, compares it to the actual stem position, and adjusts the pneumatic output to the actuator.
  5. The actuator moves the valve stem, changing the position of the closure member (plug, ball, disc).
  6. The flow through the valve changes, bringing the process variable back to setpoint.

Control Valve Components

ComponentFunctionKey Specifications
Valve BodyPressure-containing envelope. Houses trimASME B16.34, API 6D, material per process conditions
Trim (Plug, Seat, Cage)Modulates flow. Primary wearing componentsMaterial, characteristic, tight shutoff class
BonnetPressure boundary between body and actuator. Houses packingStandard, extension (cryogenic/high temp), bellows seal
PackingSeals around moving stemPTFE, Graphite, live-loaded
ActuatorProvides force to move the stemPneumatic diaphragm, pneumatic piston, electric, electro-hydraulic
PositionerEnsures stem position matches control signalPneumatic, electro-pneumatic, smart/digital
AccessoriesEnhance functionality and safetyLimit switches, solenoid valves, air filter regulators, volume boosters, handwheels

1. Globe-Style Control Valves

The traditional and most widely used control valve configuration. A linear-motion plug moves vertically within a seat ring or cage to modulate flow.

Body Types

TypeDescriptionApplication
Single-Port, UnbalancedOne plug, one seat. Simple, tight shutoffClean service, moderate pressure drop. Most common
Single-Port, Pressure-BalancedPlug has balance holes or balance chamberHigh pressure drop where actuator force would be excessive
Cage-GuidedPlug guided within a cylindrical cage. Cage can have characterized holesVersatile. Trim easily changed. Reduced noise and cavitation options
Double-PortedTwo plugs, two seats. Forces partially balancedHigh capacity. Less common now (higher leakage)
Angle BodyInlet and outlet at 90°. Combines valve + elbowErosive fluids, flashing, high pressure drop with solids
Three-WayThree connections. Mixing or diverting serviceTemperature control, bypass, combining streams

Flow Characteristics (Trim Profiles)

CharacteristicPlug ShapeFlow vs. TravelApplication
LinearCylindrical or conicalFlow directly proportional to travelLevel control, constant ΔP
Equal PercentageCurved, flaredEqual increments of travel produce equal percentage change in flowMost common. Pressure, flow, temperature control where ΔP varies
Quick OpeningFlat disc or beveled edgeLarge flow change for small initial travelOn/off, relief, bypass

2. Rotary Control Valves

Use a rotating closure member (ball, disc, plug) rather than a linear plug. Offer higher capacity, smaller size, lighter weight, and lower cost than globe valves for equivalent flow.

TypeDescriptionBest For
V-Ball (Segmented Ball)Ball with V-shaped or parabolic notch. Equal percentage characteristicSlurries, viscous fluids, fibrous materials. High capacity
Eccentric Plug (Camflex)Plug rotates eccentrically. Contacts seat only at final closureSlurries, flashing fluids, abrasive service
High-Performance ButterflyDouble or triple offset disc. Metal seated availableLarge diameter. Gas, steam, high temperature
Concentric ButterflyResilient-seated disc. Low costWater, non-critical, moderate temperature

3. Severe Service Control Valves

Applications where standard trims fail rapidly due to cavitation, flashing, high noise, or extreme erosion.

Service ConditionProblemSolution
Cavitation (Liquids)Vapor bubbles form and collapse, eroding trim and bodyAnti-cavitation trim. Multi-stage pressure reduction. Hardened materials
Flashing (Liquids to Vapor)Liquid flashes to vapor across valve. High velocity, erosionAngle body. Hardened trim. Larger body outlet to accommodate expanded vapor volume
High Noise (Gas)Aerodynamic noise >85 dBA. Vibration damage to piping and instrumentsLow-noise cage. Multi-stage trim. Diffuser plates. Acoustic insulation
Erosive Solids (Sand, Catalyst)Particles erode plug, seat, and bodyTungsten carbide trim. Ceramic trim. Stellite hardfacing. Angle body

4. Control Valve Actuators

The actuator provides the force or torque to move the valve closure member against process pressure, packing friction, and seat loading.

TypePower SourceFail ModeApplication
Pneumatic Spring & DiaphragmInstrument air (3-15 psi or 6-30 psi)Spring drives to fail position (FO, FC, FL)Most common. Reliable, simple, cost-effective
Pneumatic PistonInstrument air to double-acting cylinderFail position requires air receiver or spring-returnHigh thrust. Large valves. Long stroke
Electric (Smart)24 VDC, 110/220 VACProgrammable. Battery backup optionalRemote locations. No instrument air available
Electro-HydraulicElectric signal controls hydraulic power unitProgrammable. Accumulator for fail-safeSubsea. High force. Remote
Manual (Handwheel)OperatorN/AManual override. Maintenance bypass

Fail Modes

DesignationDescriptionExample Application
Fail-Open (FO)Valve opens on loss of signal/air/powerCooling water supply, compressor recycle
Fail-Closed (FC)Valve closes on loss of signal/air/powerFuel gas supply, hydrocarbon isolation
Fail-Last / Fail-in-Place (FL)Valve holds last position on loss of signalWhere sudden open or closed is equally undesirable. Locks in position

5. Positioners & Accessories

Positioners

TypeSignalFeatures
Pneumatic (P/P)3-15 psi input to 3-15 psi outputSimple, no electricity required
Electro-Pneumatic (I/P)4-20 mA input to pneumatic outputStandard for DCS/PLC control loops
Smart / Digital4-20 mA + HART, Fieldbus, Profibus PAAuto-calibration, diagnostics, partial stroke testing, valve signature, predictive maintenance

Accessories

ComponentFunction
Filter RegulatorProvides clean, regulated air to positioner and actuator
Solenoid ValveElectrically vents actuator to force fail position on ESD signal
Limit SwitchesOpen/closed position confirmation to control system
Volume BoosterAmplifies pneumatic output for faster stroking speed on large actuators
Position Transmitter4-20 mA feedback of actual stem position
HandwheelManual override for maintenance or emergency operation

6. Control Valve Sizing & Selection

Control valve sizing is an engineering discipline governed by the ISA-75 and IEC 60534 standards. It is fundamentally different from on/off valve sizing. A correctly sized control valve operates typically between 20% and 80% of its travel, providing adequate rangeability without hunting at low opening or saturating at high opening.

Key Sizing Parameters

ParameterSymbolUnitDescription
Flow CoefficientCv or KvUS or metricFlow capacity of the valve at full open with 1 psi (or 1 bar) pressure drop
Pressure DropΔPpsi, barDifference between inlet and outlet pressure at rated flow
Inlet PressureP1psia, baraAbsolute pressure upstream of valve
Vapor PressurePvpsia, baraLiquid vapor pressure at flowing temperature. Critical for cavitation/flashing analysis
Critical PressurePcpsia, baraFluid critical pressure
Specific GravitySg or ρ— or kg/m³Fluid density relative to water or absolute
ViscosityμcPAffects Reynolds number correction for Cv
Pressure Recovery FactorFLInherent valve characteristic. Low FL = high recovery = prone to cavitation

Sizing Steps (Simplified)

  1. Define required flow rate (min, normal, max)
  2. Calculate required Cv for each flow condition
  3. Select valve body size (typically one size smaller than line size for globe, equal for rotary)
  4. Verify that all flow conditions fall within 20-80% of valve travel
  5. Check for cavitation (liquid), noise (gas), and choked flow conditions
  6. Specify actuator sizing based on required force/torque at maximum shutoff ΔP
  7. Document all selections in an ISA data sheet

Control Valve Standards

StandardScope
ISA-75.01.01Flow equations for sizing control valves
ISA-75.02.01Control valve capacity test procedures
ISA-75.05.01Control valve terminology
ISA-75.08.01Face-to-face dimensions for integral flanged globe-style control valves
ISA-75.11.01Inherent flow characteristic and rangeability
ISA-75.17Control valve aerodynamic noise prediction
ISA-75.25.01Control valve hydrodynamic noise prediction
IEC 60534 SeriesInternational equivalent of ISA-75
API 6DPipeline valves (when control valve is in pipeline service)
ASME B16.34Valves – flanged, threaded, and welding end
NACE MR0175 / ISO 15156Sour service materials
SIL (IEC 61508 / IEC 61511)Safety integrity level for valves in safety instrumented functions

Integration with the Rest of Your Site

The control valves page cross-references:

SectionRelationship
Valves (Manual & On/Off)Manual gate/globe/ball valves for isolation. Control valves for modulation
Instrument Valves & ManifoldsInstrument isolation and calibration valves connected to control valve positioners
Instrument Tubing & FittingsPneumatic tubing from positioner to actuator. Instrument air supply lines
Junction Boxes & EnclosuresHousing for solenoid valves, limit switches, and smart positioner electronics
Rotating EquipmentAnti-surge control valves on compressors. Minimum flow bypass on pumps
Wellhead & Downhole EquipmentChoke valves (specialized control valves for wellhead pressure management)

How We Supply Control Valves

  • Complete Package: Valve body + trim + actuator + positioner + solenoid + limit switches, assembled, calibrated, and tested as a unit
  • ISA Data Sheet Review: We review your process data and control philosophy to flag undersized trims, incorrect materials, or missing noise/cavitation analysis
  • Documentation: Full MTRs, hydrostatic test records, seat leakage test (FCI 70-2 Class IV, V, or VI), actuator bench set, positioner calibration certificate
  • Aftermarket: Trim kits, packing kits, actuator seals, positioner upgrades