Oil & Gas×Control Valves

Control Valves for Oil & Gas

Control valves in oil & gas facilities regulate flow, pressure, temperature, and liquid level across every process unit — from wellhead production chokes and separator level control to refinery feed ratio control and compressor surge control. Vajra Industrial Solutions supplies globe, rotary, and cage-guided control valves per ANSI/ISA-75 and API 553, in NACE MR0175 compliant materials for upstream and refinery applications, with positioners, I/P converters, and HART communication for DCS integration.

Key Applications — Control Valves in Oil & Gas

Wellhead Production Choke (Flow Control)

High-pressure choke valves for wellhead flow control — reducing reservoir pressure (1,000–15,000 psi) to separator operating pressure. Positive-choke and adjustable-choke designs for erosive sand-bearing well fluids. Tungsten carbide trim for sand erosion resistance. NACE MR0175 body and trim. API 6A design for wellhead service.

DN25–DN100, Class 1500–10000 (WP), Inconel trim, WC trim, API 6A, NACE MR0175

Separator Level Control Valve

Control valves for three-phase separator oil and water level control — regulating flow of produced oil to export line and produced water to disposal or injection. Cage-guided globe valve for stable control of liquid level (inherently noisy, flashing service). NACE MR0175 for sour produced fluids.

DN25–DN100, Class 150–600, WCB / CF8M, cage-guided trim, ANSI/ISA-75, NACE

Gas Pressure Control — Compressor Suction/Discharge

Control valves for gas pressure regulation on compressor suction scrubbers, inter-stage separators, and discharge pressure reduction stations. Anti-surge valve for centrifugal compressor protection — fast-acting (under 1 second) with linear characteristic. Carbon steel body with SS 316 trim for sweet gas; duplex trim for sour or wet gas.

DN50–DN300, Class 150–600, WCB / CF8M, ANSI/ISA-75, fast-acting, anti-surge trim

Refinery Feed and Product Flow Control

Globe and rotary control valves for crude distillation unit feed, product draw-off flow control, and reflux control at atmospheric and vacuum distillation columns. High-temperature alloy (WC6/WC9) for furnace outlet and hot product lines. Top-guided single-seat or cage-guided design for stable throttling in high-flash, high-vapour-pressure streams.

DN25–DN200, Class 150–600, WCB / WC6 / CF8M, ISA-75, ASME B16.34, high-temp packing

Required Certifications

ANSI/ISA-75 — Control Valve Sizing and Capacity EquationsAPI 553 — Refinery Control Valves (installation and maintenance)NACE MR0175 / ISO 15156 — Sour serviceAPI 607 — Fire-safe testingEN 10204 3.1 MTCsSIL (IEC 61511) — Safety Instrumented System applicationsATEX / IECEx — Electrical equipment in hazardous areas (positioners)

Recommended Materials

A216 WCB — sweet crude, gas, and general refinery service
A351 CF8M (SS 316 cast) — sour, CO₂, and corrosive service
A217 WC6 (1.25Cr-0.5Mo) — high-temperature refinery >340°C
A182 F51 Duplex 2205 — wet sour gas and offshore applications
Tungsten carbide trim — wellhead choke, erosive sand service
Inconel 625 trim — high-temperature, corrosive, erosive service

Selection Factors

Sizing: Cv calculation per ISA-75.01 — account for flashing, cavitation (FL factor), and noise (Fd factor)
Trim characteristic: Equal-percentage for pressure/temperature control; linear for flow control; quick-opening for on/off
NACE: Sour service requires MR0175 compliant body, trim, bonnet, and packing follower
Noise: High-pressure drop gas service generates high noise — use multi-stage trim or downstream diffuser
Actuator: Pneumatic spring-and-diaphragm for most; piston actuator for large valves or high differential pressure
Positioner: HART or FOUNDATION Fieldbus positioner for DCS integration and valve diagnostics
Fail position: Fail-closed (FTC) for feed and product control; fail-open (FTO) for cooling water and compressor anti-surge

Technical FAQs

What is the difference between a control valve and a choke valve in oil & gas?
A choke valve is a specific type of control valve designed for wellhead service — handling the extreme pressure drops (from reservoir pressure to separator pressure), sand-bearing fluids, and erosive conditions at the wellhead. Choke valves are designed to API 6A (wellhead equipment) and use highly erosion-resistant trim (tungsten carbide, ceramic). Standard control valves are designed to ISA-75 for process facilities (separators, compressor stations, refineries) and use SS, duplex, or alloy trim without the extreme erosion-resistance features of choke valves.
What causes cavitation in oil & gas control valves and how is it prevented?
Cavitation occurs when a liquid control valve's pressure drops below the fluid's vapour pressure, causing vapour bubbles to form, then collapse violently as pressure recovers downstream. In oil & gas, cavitation is most common on separator level control valves handling pressurised liquid (high-pressure separator to low-pressure vessel). Prevention: use a multi-stage (cascade) trim that reduces pressure in steps, each below the vapitation threshold; select valve with high FL (liquid pressure recovery factor); or use a downstream back-pressure regulator to raise downstream pressure above vapour pressure.

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