Natural Gas Compression

Flare Gas Recovery

Lubricants for flare gas recovery compressors recover gas from flare headers and return it to a fuel gas system, a process unit, or, where treatment and specifications permit, a sales-gas system.

Flare-header composition varies with connected processes. Recovered gas contains light and heavier hydrocarbons, water vapor, CO₂ (carbon dioxide), H₂S (hydrogen sulfide), and frequently hydrogen and nitrogen. Where this gas contacts the lubricant, dissolved gas and hydrocarbon condensate reduce its operating viscosity.

NEXT Lubricants supplies PAO (polyalphaolefin), PAG (polyalkylene glycol), PAG-WS (water-soluble polyalkylene glycol), and PEG (polyethylene glycol) formulations for gas-contact lubrication in flare gas recovery compressors. Selection depends on the complete gas composition, pressure, temperature, compressor design, and water exposure across the operating envelope.

For technical background on rich wellsite gas and lubricant dilution, see [Associated Gas and Flare Gas Capture: Compressor Lubricants for Rich Wellsite Gas].

Key Takeaways
01

Flare gas recovery captures gas that would otherwise be burned and returns it to a fuel, process, or suitable sales-gas system. Refinery, gas-processing, and production headers carry different gas compositions and operating profiles, which determine the lubrication requirements.

02

Oil-injected compressors and lubricated cylinders expose the lubricant directly to recovered gas. Dissolved gas can reduce its operating viscosity. Bearings, gearboxes, and drives isolated from the process gas require lubricants selected for their own equipment requirements.

03

Gas composition, pressure, and lubricant temperature act together to determine dilution. Heavier hydrocarbons can substantially reduce viscosity, but hydrocarbon content alone does not establish severity. Selection must consider the conditions at the actual lubrication point.

04

Select for the most demanding credible combinations of composition and conditions within the recovery compressor’s operating envelope. An average gas analysis can hide significant changes. Include normal operation, load changes, and relevant shutdown and restart conditions.

05

Flare gas recovery can operate continuously or intermittently. Some systems recover sustained routine flows; others cycle with gas availability. Where lubricant remains exposed to gas during shutdown, retained pressure, temperature, and contact time can affect its condition at restart.

06

Gas analysis and dilution calculations support lubricant selection, while used-oil analysis tracks its condition in service. Dissolved gas can escape during sampling, so laboratory viscosity may be higher than operating viscosity. Interpret the results alongside the actual compressor conditions.

products

Recommended NEXT Flare Gas Recovery Compressor Lubricants

NEXT GPL PAG

Light–Medium Hydrocarbon / Dilution-Prone Recovery

Base Oil: PAG

ISO Range: 32 – 680

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NEXT GPL PAG-WS

Medium–Heavy Hydrocarbon / Higher-Dilution Recovery

Base Oil: PAG-WS

ISO Range: 32 – 460

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NEXT GPL PAG-EO

Heavy Hydrocarbon / Lowest Hydrocarbon Dilution

Base Oil: PEG

ISO Range: 32 – 220

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NEXT GPL PAO

Light Hydrocarbon / Lower-Dilution Recovery

Base Oil: PAO

ISO Range: 32 – 320

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PROCESS, APPLICATION & COMPRESSOR

How Flare Gas Recovery Works and the Compressor's Role

Flare gas recovery units draw gas from the flare collection system and compress it for reuse. Depending on gas quality and treatment requirements, recovered gas returns to a fuel gas, process, or sales-gas system. Recovery reduces routine flaring while the flare remains available for excess flows, recovery-system outages, and emergency releases.

A typical installation includes a recovery connection to the flare header, liquid separation, compression, cooling, and downstream separation or treatment. Pressure controls and the flare-system arrangement maintain the required header conditions and preserve the relief path to the flare. The recovery unit operates within its designed flow, pressure, and gas-composition limits.

Recovery compressors run continuously, under variable load, or intermittently. Liquid-ring, oil-injected and dry screw, reciprocating, and sliding-vane compressors serve different combinations of gas composition, capacity, pressure ratio, and package requirements.

Lubrication requirements vary with compressor design. Oil-injected compression chambers and lubricated cylinders expose the lubricant to process gas — where viscosity after dilution determines component protection. Separately lubricated bearings and drives follow their own manufacturer requirements, and in liquid-ring compressors, the ring's service liquid is selected independently of bearing and drive lubrication.

Refinery Flare Systems

Recovery from refinery flare headers for return to fuel gas or process systems, with treatment where required.

Gas Plants & Processing Facilities

Flare-header recovery at natural gas processing, NGL (natural gas liquids) recovery, and gas-treating facilities.

Production Facilities & Offshore

Recovery of gas routed to flare systems at oil and gas production facilities, including offshore installations.

LNG & Storage Terminals

Recovery from designated flare systems at liquefaction, regasification, and storage facilities.

LUBRICANT SELECTION FACTORS

Factors affecting lubricant selection

Vapor recovery combines hydrocarbon-rich vapor, low suction pressure, variable flow and the possibility of condensation. The following factors determine the lubricant chemistry and viscosity required.

Process

What NEXT needs to recommend a lubricant

A lubricant recommendation is based on the information below. Provide whatever information is available; NEXT will identify whether any additional details are required.

Benefits

Operational Benefits of Correct Lubricant Selection

Selecting the lubricant according to the compressor, gas composition and operating conditions can provide several operational benefits.

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TECHNICAL SUPPORT

Lubricant Selection, Technical Support and Compatibility Documentation

NEXT combines application knowledge, laboratory data and an extensive internal cross-reference database to support lubricant selection, conversions and compressor troubleshooting.

Depending on the application, we can provide:

Frequently Asked questions

Lubricant chemistry is determined by duty, not application name. For gas-contact lubrication, the range extends from mineral and PAO base stocks for leaner, drier headers, through PAG and water-soluble PAG, to PEG as the recovered stream becomes richer. Selection is based on dissolved-gas behavior, operating viscosity, water exposure, and compatibility. Separately lubricated bearings and drives have their own requirements. NEXT provides a conclusive recommendation for a specific header, machine, and lubrication point.

Where gas contacts the lubricant, soluble components dissolve into it and reduce its viscosity—heavier hydrocarbons far more readily than lighter ones. Hydrocarbon condensate also adds a liquid contamination path. The severity depends on composition, chemistry, pressure, and temperature: rich, wet headers dilute fast; lean, dry ones barely at all.

Neither alone. Selection uses the most demanding credible combination of composition and conditions within the compressor’s intended envelope. The average day understates the duty, and the richest composition by itself is not the whole answer either: pressure and lubricant temperature influence dilution as much as richness does. Emergency releases routed directly to the flare are outside the recovery compressor’s duty and do not factor into its sizing.

The collection source. Vapor recovery units collect vapors from storage tanks, loading operations, and production equipment; flare gas recovery units recover gas from the flare collection system. The lubricant mechanics—low suction pressure, condensable gas, variable composition—are shared, which is why the duties share a chemistry range. Compositions are site-specific, so selections are too.

Not for the ring itself, as the service liquid is a separate selection. The lubricated bearing and drive end require an oil or grease according to the manufacturer’s design. Where these points are isolated from the process gas, flare-gas dilution is not a selection criterion. The products on this page are for gas-contact lubrication; they do not include liquid-ring service liquids.

No. Suction pressure is one of several inputs. Gas composition, lubricant chemistry, and the pressure and temperature at the actual gas–lubricant contact points determine dissolved-gas behavior, and hydrocarbon condensate contaminates the lubricant regardless of suction pressure. Low suction pressure changes where dilution occurs, not whether it does.

It depends on the isolation arrangement. Lubricant in contact with header gas under retained pressure continues to absorb gas during standstill and starts the next run pre-diluted. An isolated, depressurized sump does not. Shutdown and restart scenarios are evaluated alongside normal operation. Warming at restart drives dissolved gas out over time, not instantly.

This is sometimes possible and worth investigating, as inventory consolidation offers real value. The condition is that the product satisfies each machine’s viscosity, chemistry, and compatibility requirements. A lubricant selected for the most severe stream is not automatically suitable for every lubrication point on site. NEXT reviews all machines together and advises where one product genuinely covers the needs and where separate products are required.

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