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LPG and Propane Drying and Treating
Gas Treatment & Drying

LPG and Propane Drying and Treating

Drying and sulphur removal from liquefied petroleum gas (LPG), propane, and butane streams using 3A molecular sieve and impregnated activated carbon to meet pipeline and storage specifications.

The Challenge
Liquefied petroleum gas above the pipeline water limit forms hydrates and ice in storage tanks and distribution piping. Trace mercaptans cause odour problems and corrode downstream equipment. The drying bed must work without coadsorbing the C3 and C4 product hydrocarbons.
Quick Answer

LPG drying removes water and trace sulphur from liquefied petroleum gas, propane, and butane streams using 3A molecular sieve in a TSA cycle. The 3 Å pore size excludes the C3 and C4 hydrocarbons from the sieve, eliminating coke laydown and giving long media life. Optional impregnated activated carbon polishing handles trace mercaptans.

LPG and Propane Drying and Treating

Why LPG Dehydration Needs 3A Specifically

Liquefied petroleum gas (LPG) and its components propane (C3) and butane (C4) are the world’s most widely distributed cooking and heating fuels. Pipeline and storage specifications limit water to single digit ppm to prevent hydrate formation and ice accumulation. The drying sieve must remove the water without coadsorbing the C3 and C4 hydrocarbons; SorbiTech 3A molecular sieve with its 3 Å pore is the only sieve that meets this requirement.

3A Excludes Propane and Butane by Pore Geometry

Propane (4.3 Å) and butane (4.7 Å) both exceed the 3 Å pore opening of 3A and cannot enter the crystal. Water (2.6 Å) enters freely and is captured at the surface and inside the cages. The bed holds water alone; the regeneration off gas contains only the released water with minimal hydrocarbon loss. A 4A bed would adsorb both water and propane, lose propane to the regeneration vent, and laydown coke in the crystal during regeneration.

LPG and Propane Drying and Treating process equipment

Optional Mercaptan Polishing

Where the LPG carries trace mercaptans (typically 5 to 50 ppm at the wellhead), a downstream impregnated activated carbon polishing layer removes the sulphur to below the storage and distribution specification. The combined train delivers pipeline ready LPG without a separate sulphur removal unit.

Delivery as Media or Complete Package

SorbiTech supplies LPG drying as a SorbiTech 3A media supply contract for an existing dryer or as a complete twin tower TSA dehydration package engineered by SorbiTech. Sector coverage is oil and gas and petrochemicals and refining.

Selection Guidance

3A molecular sieve excludes propane and butane from the pore; water is captured alone. Impregnated activated carbon polishing layer for mercaptan removal. TSA cycle at the LPG handling pressure.

A Specified, Verified Solution

Define the duty

We capture your process conditions: flow, composition, pressure, temperature, and the target outlet specification.

Select media & configuration

Our engineers recommend the adsorbent grade and system type that meet the duty with margin.

Size & engineer

Bed sizing, vessel design, and cycle parameters are engineered to your case and documented for approval.

Commission & verify

We support loading, start up, and performance verification against the guarantee.

Specify a Solution for This Application

Provide your process conditions and our team will recommend the grade, configuration, and sizing.