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Gas Sweetening (H₂S and CO₂ Removal)
Gas Treatment & Drying

Gas Sweetening (H₂S and CO₂ Removal)

Removing hydrogen sulphide and carbon dioxide from natural gas and refinery streams using 13X molecular sieve TSA or impregnated activated carbon to meet pipeline and LNG specifications.

The Challenge
Sour natural gas with H₂S above 4 ppmv fails pipeline specification, corrodes pipeline steel, and is a safety hazard at the wellhead; CO₂ above pipeline limit lowers heating value and causes ice formation in cryogenic processes.
Quick Answer

Gas sweetening removes hydrogen sulphide (H₂S), carbon dioxide (CO₂), and mercaptans from natural gas, associated gas, and refinery gas streams. SorbiTech delivers the duty using 13X molecular sieve in a TSA cycle (small to medium scale) or impregnated activated carbon guard beds downstream of amine contactors (large scale). Outlet meets GPA 2140 pipeline H₂S limit of 4 ppmv.

Gas Sweetening (H₂S and CO₂ Removal)

Sour Gas Specifications Drive the Duty

Gas sweetening is the removal of acid gases, hydrogen sulphide and carbon dioxide, and mercaptans from natural gas, associated gas from oil production, refinery gas streams, and biogas. Pipeline specifications (GPA 2140 in North America, equivalent in other jurisdictions) limit H₂S to 4 ppmv and CO₂ to 2 to 4 mol percent. LNG feed preparation tightens these further: H₂S below 4 ppmv, CO₂ below 50 ppmv to prevent cold box freezing. Refinery gas streams require similar treatment ahead of catalytic units that are sulphur sensitive.

Molecular Sieve TSA at Small to Medium Scale

Below about 60 MMSCFD a gas sweetening unit using SorbiTech 13X molecular sieve in a TSA cycle delivers combined drying and sweetening in a single bed. The 13X grade is preferred over 4A because the 10 Å pore admits H₂S, CO₂, and mercaptans alongside water; a single bed delivers both pipeline H₂S and pipeline dew point. The regeneration off gas is routed to a flare, an incinerator, or a Claus sulphur recovery unit depending on the H₂S load.

Gas Sweetening (H₂S and CO₂ Removal) process equipment

Amine Plus Polishing at Large Scale

Above 60 MMSCFD the economics favour an amine contactor (typically MDEA or formulated solvent) for the bulk H₂S and CO₂ removal, followed by molecular sieve polishing for the residual water and trace sulphur. The combined train delivers the pipeline or LNG specification at lower capital and operating cost than molecular sieve alone at large scale.

Sour Service Engineering and Delivery

All SorbiTech sweetening equipment is built to NACE MR0175 / ISO 15156 for hardness control in H₂S service, with mandatory post weld heat treatment and full material traceability. SorbiTech runs the fabrication; SorbiTech delivers the turnkey package where the project includes civil and electrical scope. Sector coverage is oil and gas and petrochemicals and refining.

Selection Guidance

Below 60 MMSCFD: 13X molecular sieve TSA gives combined drying and sweetening in one bed. Above 60 MMSCFD: amine contactor (MDEA) followed by molecular sieve polishing. For mercaptans add impregnated activated carbon polishing layer.

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.