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Carbon dioxide removal

Eastman AdapT solvents for CO2 removal

Eastman AdapT solvents rely on the chemistry of the different amine-carbon dioxide (CO2) reactions to optimize the performance for each application.

By choosing the type and concentration of various amines, the CO2 removal rate and absorption capacity can be customized. Besides CO2 removal efficiency, factors like system corrosion and operational limitations are also crucial in selecting the appropriate solvent.

A landscape view of a gas treatment facility.
An engineer in PPE performs a site inspection.

Bulk CO2 removal

Solvents for bulk CO2 removal are used for natural gas and syngas plants. Typical treated gas specifications require a high-volume percentage. Thermal regeneration of the solvent is not always essential to meet the specifications but, in most cases, is preferred.

The alternative to thermal regeneration is flash regeneration, which yields to strong reduction in energy consumption. However, this process is less robust against changing gas composition, operating conditions and external contamination.

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Deep CO2 removal

Solvents for deep CO₂ removal are used in liquefied natural gas (LNG) plants and ammonia plants. Achieving effective CO₂ removal requires high reactivity between CO₂ and the solvent, which can be accomplished with Eastman AdapT 200 series solvents.

In addition to solvent reactivity, the residual loading of the lean solvent and absorption conditions are key factors in determining the optimal solvent and plant design. Towers for natural gas treatment with the aim of producing LNG often include extra trays. The regeneration section is expanded with additional heat input and stripping stages to drive the lean solvent loading to challengingly low levels.

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CO2 absorption reaction chemistry

The removal of CO₂ is required in many applications. Eastman AdapT solvents rely on the chemistry of different amine-CO₂ reactions to optimize the performance for each application.

Tertiary amines, such as MDEA, form a bicarbonate with CO₂, which is slowly formed in the amine solution. This is illustrated in the following reaction scheme.

A chart showing how tertiary amines like MDEA form bicarbonate with carbon dioxide in the amine solution. A chart showing how tertiary amines like MDEA form bicarbonate with carbon dioxide in the amine solution.
Chart showing how non-tertiary amines can react with carbon dioxide to free a proton. Chart showing how non-tertiary amines can react with carbon dioxide to free a proton.

Formation of carbamate

Non-tertiary amines can react much faster with CO₂ through formation of a carbamate. The free proton formed in this reaction may protonate a second amine, which is also a fast step but reduces the absorption capacity. This is illustrated in the reaction scheme.

By selecting the type and concentration of various amines, the CO₂ removal rate and absorption capacity can be adapted. Alongside CO₂ removal efficiency, factors like system corrosion and operational limitations are also important in choosing the right solvent.

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