Understanding Polyalkylene Glycols (PAG)

PAG lubricants are a family of synthetic base lubricants used across refrigeration, heat pump, and hydrocarbon gas compression applications. Unlike mineral lubricants, PAGs come in several distinct chemistries — each with different solubility, miscibility, and dilution behaviour with both refrigerants and process gases. Selecting the right type depends on the gas composition, system design, and operating conditions.

 

Common PAG Chemistries Used in Compressor Lubricants

A PAG lubricant is defined by the oxide monomer used to build its backbone. Propylene oxide (PO) produces a less polar, more hydrophobic polymer. Ethylene oxide (EO) produces a polar one. Copolymers sit between the two, with the EO:PO ratio controlling where the final lubricant lands on the polarity spectrum. Polarity is what governs the properties that matter in service: water solubility, refrigerant miscibility, and how much hydrocarbon gas dissolves into the lubricant at pressure.

Technical Background

MONOMER CHEMISTRY AND POLARITY

Key solubility, miscibility and dilution behaviour is mainly driven by base-stock chemistry, while additives tune performance areas such as oxidation control, wear protection, corrosion and foaming. A PO-based backbone gives a lubricant that dissolves readily into hydrocarbon gases but rejects water. An EO-based backbone does the opposite. Copolymers are built to sit somewhere useful between the two. Because polarity is baked into the base stock, additive packages cannot shift these behaviours meaningfully — the backbone decides what the lubricant will do in service.

180–250

Typical PAG viscosity index

< 3%

PEG dilution with pentane (R-601)

15–30%

WI-PAG dilution with butane (R-600)

DILUTION BEHAVIOUR WITH HYDROCARBON GASES

At operating pressure, hydrocarbon gas dissolves into the lubricant in the sump. The more it dissolves, the more in-service viscosity drops below nominal grade. In representative butane/heavy-hydrocarbon cases, WI-PAG can show substantial dilution, WS-PAG typically lower dilution, and PEG very low dilution. Actual values depend on pressure, temperature, gas composition and formulation For medium to heavy hydrocarbon streams at high pressure, dilution is the single most important input into nominal grade selection.

MODELLING IN-SERVICE DILUTION

Predicting how much a PAG will dilute in real service requires solving the thermodynamics of gas solubility in the specific lubricant at the actual operating pressure and temperature. NEXT uses a PVT (pressure–volume–temperature) model calibrated against measured solubility data for each base chemistry — WI-PAG, WS-PAG, and PEG, with PAO and mineral baselines for comparison. The model takes the gas composition in mol % (methane, ethane, propane, butane, pentane, CO₂, H₂S, N₂), the suction and discharge pressure, and the expected sump temperature as inputs, and returns the in-service viscosity at those conditions.

That in-service number is what should drive nominal grade selection. For heavy hydrocarbon streams or high-pressure duty, the gap between nominal and in-service viscosity is typically one to two ISO grades — large enough to move a compressor from correctly lubricated to under-lubricated if selection is made from the data sheet alone. The PVT model removes that gap from the decision.

MISCIBILITY WITH REFRIGERANTS

Certain PAG formulations are highly miscible with ammonia (R717), making them suitable for ammonia DX systems where oil return depends on refrigerant/lubricant circulationWith CO₂ (R-744), miscibility is partial and formulation-specific — dedicated CO₂ PAGs are built to manage this. PAGs are not standard with HFC or HFO refrigerants, where POE is the dominant chemistry.

LUBRICITY AND FILM STRENGTH

PAGs are naturally high-lubricity. The polar backbone adsorbs onto metal surfaces, giving boundary protection that synthetic hydrocarbons cannot match without additive support. Combined with viscosity indices of 180 to 250, a PAG typically outperforms a mineral or PAO of the same nominal grade across a wider temperature range.

CARBON AND VARNISH BEHAVIOUR

PAGs are known for low deposit tendency and clean burn-off behaviour compared with many hydrocarbon-based oils, helping reduce carbon and varnish risk in suitable applications. For high-ratio gas compressors and heat pumps running at elevated discharge temperatures, this behaviour is often the deciding factor over base-stock cost.

Key Factors

Four variables determine whether a given PAG will perform in a given system. They interact — a change in one usually shifts the requirements on the others.

Base Lubricant Chemistry

The monomer type (PO, EO, BO, or copolymer) determines polarity, water solubility, and solubility with both refrigerants and hydrocarbon gases.

Gas Composition

Light hydrocarbons (methane, ethane) cause limited dilution; medium fractions (propane, butane) cause moderate dilution; heavy fractions (pentane+) cause significant viscosity reduction, particularly in WI-PAG.

Operating Pressure

Higher discharge pressures increase gas solubility in the lubricant. This effect is most pronounced with medium and heavy hydrocarbon gases and must be factored into viscosity grade selection.

Operating Viscosity

In-situ viscosity can drop significantly under gas dilution. Nominal grade selection must account for expected dilution across the full range of operating pressures and gas compositions.

Applications

PAG Selection by Application

PAG selection starts with what the compressor is moving. Gas composition and refrigerant chemistry determine which backbone works. Viscosity grade is the second decision, made after the chemistry is fixed.

Hydrocarbon Gas Compression

WS-PAG or PEG for medium-to-heavy streams (propane, butane, pentane) where dilution must be controlled. WI-PAG is acceptable for lighter gas or lower-pressure duty.

CO₂ Refrigeration

Dedicated CO₂ PAGs formulated for partial miscibility. Selection depends on whether the system is transcritical or subcritical.

Immiscible Hydrocarbon Heat Pumps

PEG is the default. The lubricant stays in the sump rather than circulating with the refrigerant, so dilution resistance and thermal stability dominate.

High-Pressure Natural Gas

WS-PAG for streams with significant C3+ content. WI-PAG loses too much viscosity at pressure under these conditions.

Lubrication Considerations

Four practical rules that separate a reliable PAG installation from a problem one.

Match the Backbone to the Gas Stream

Dilution behaviour comes from the base chemistry, not the additive package. A WI-PAG in heavy hydrocarbon service will never hold grade, regardless of the starting viscosity.

Select Viscosity for In-Service Conditions, Not Nominal

Data-sheet viscosity is measured in a beaker, not at pressure. A VG 220 WI-PAG at 25% dilution behaves like a VG 150 in service. Use the NEXT PVT dilution model to calculate in-service viscosity for your actual gas composition and operating envelope, and select the nominal grade that lands on the target in-service value — not above it, not below it.

Never Mix PAG with Mineral, PAO, or POE

Most conventional PAGs should not be mixed with mineral oil, PAO or other lubricant chemistries unless compatibility has been confirmed. Conversions normally require thorough draining and flushing.

Manage Moisture in WS-PAG and PEG

Water solubility is a feature in service but a liability in storage. Keep drums sealed, dedicate transfer equipment, and monitor water content in operation.

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Understanding Polyalkylene Glycols (PAG)

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Frequently Asked Questions

Common questions about gas dilution and its effects on compressor lubrication systems.

It depends on what the compressor is moving. For ammonia refrigeration and heat pumps, WI-PAG is standard because of its high miscibility with ammonia. For medium-to-heavy hydrocarbon gas compression, WS-PAG is the usual choice as it dilutes less than WI-PAG at pressure. For immiscible heat pump systems running on hydrocarbon refrigerants, PEG is the default because dilution is negligible. For CO₂ systems, dedicated CO₂ PAGs are formulated specifically for that refrigerant and should not be substituted with general WI-PAG or WS-PAG.

No. PAG is chemically incompatible with mineral, PAO, and POE lubricants and forms sludge on contact. A proper conversion requires draining the system, flushing with a compatible fluid, and confirming that residual contamination is below 1% before charging the new lubricant. Skipping the flush is the most common cause of premature PAG failure after a base-stock change.

The model is a thermodynamic tool that calculates how much of each gas component dissolves into the lubricant at the system’s actual operating pressure and temperature. It is calibrated against measured solubility data for WI-PAG, WS-PAG, and PEG, with PAO and mineral baselines included for comparison. Inputs are gas composition in mol %, suction and discharge pressure, and expected sump temperature. Outputs are total dilution percentage and the resulting in-service viscosity. For compressors running on hydrocarbon streams or at elevated pressures, this in-service viscosity is the number that matters for grade selection — and it can differ from the nominal data-sheet value by one or more ISO grades. To run your case through the model, use the Request Lubricant Recommendation form or contact the NEXT technical team directly.

They are the same material. PPG is the chemical name for a polymer built entirely from propylene oxide; WI-PAG is the industry designation used in the lubricant market. The terms are used interchangeably in technical literature and in NEXT product documentation.

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