A gas treatment device uses a gas to be treated which contains an acid compound that dissolves into water to produce acid and a treatment liquid which absorbs the acid compound to phase-separate, to separate an acid compound from the gas to be treated. The gas treatment device includes an absorber which brings the gas to be treated into contact with the treatment liquid; a regenerator 14 which heats the treatment liquid contacting the gas to be treated to separate an acid compound; and a liquid feeding portion which feeds the treatment liquid contacting the gas to be treated in the absorber to the regenerator. In the absorber, the treatment liquid contacting the gas to be treated phase-separates into a first phase portion having a high acid compound content and a second phase portion having a low acid compound content. The liquid feeding portion is configured to introduce, into the regenerator, the treatment liquid with the phase-separated first phase portion and second phase portion mixed.

Intensification techniques are described for enhancing biocatalytic CO.sub.2 absorption operations, and may include the use of a rotating packed bed, a rotating disc reactor, a zig-zag reactor or other reactors that utilize process intensification. Carbonic anhydrase can be deployed in the high intensity reactor free in solution, immobilized with respect to particles that flow with the liquid, and/or immobilized to internals, such as packing, that are fixed within the high intensity reactor.

An absorbent liquid which absorbs at least one of CO.sub.2 and H.sub.2S from a gas, including a secondary linear monoamine; a tertiary linear monoamine or a sterically hindered primary monoamine; and a secondary cyclic diamine, wherein a concentration of each of the secondary linear monoamine, the tertiary linear monoamine or the sterically hindered primary monoamine; and the secondary cyclic diamine is less than 30% by weight.

A composite material for gas capture, notably CO.sub.2 capture and storage. The composite material includes a mixture of a solid or liquid reactive filler and a gas-permeable polymer such that the reactive filler forms micron-scale domains in the polymer matrix.

The present disclosure relates to electrochemical target species (e.g., carbon dioxide) capture and release with a redox-active amine. Associated systems and articles are also described.

A system for direct air capture (DAC) of carbon dioxide uses a liquid CO.sub.2-absorbent solvent that enables the hybridization of a cooling tower with CO.sub.2 DAC systems. A liquid solvent such as monoethanolamine (MEA) is added to cooling water to absorb CO.sub.2 from ambient air, the cooling water is used for its original purpose, and CO.sub.2 is recovered from the cooling water in a novel process. Initially, this combination of CO.sub.2 absorbent and cooling water would appear to be undesirable, since liquid CO.sub.2 solvents such as MEA are hygroscopic, and cooling towers reject heat via evaporation. However, an absorbent concentration range was identified where CO.sub.2 could be still absorbed and water evaporated, and a novel process for absorbent solvent regeneration was created.

The invention is in the field of CO.sub.2 capture. In particular the invention relates to a method for capturing CO.sub.2 from a CO.sub.2-containing feed gas stream, wherein the method comprises at least partially removing dissolved transition metal ions by electrodeposition. The invention further relates to a system for the method.

The present invention provides a carbon dioxide absorbent comprising a primary amine and a dialkylene glycol dialkyl ether or trialkylene glycol dialkyl ether. The carbon dioxide absorbent according to the present invention has an excellent carbon dioxide absorptivity, absorption rate and regeneration property.

A carbon dioxide absorbent composition is disclosed. Based on 100 parts by weight of the carbon dioxide absorbent composition, the carbon dioxide absorbent composition includes 5 to 45 parts by weight of sodium 2-[(2-aminoethyl)amino]ethanesulfonate. Moreover, a method for capturing carbon dioxide using the carbon dioxide absorbent composition is disclosed.

Methods for enzyme-enhanced CO.sub.2 capture include contacting a CO.sub.2-containing gas with an aqueous absorption solution at process conditionssuch as high temperature, high pH, and/or using carbonate-based solutionsin the presence of Thermovibrio ammonificans carbonic anhydrase (TACA) or functional derivative thereof for catalyzing the hydration reaction of CO.sub.2 into bicarbonate and hydrogen ions and/or catalyzing the desorption reaction to produce a CO.sub.2 gas. The TACA may be provided to flow with the solution to cycle through a CO.sub.2 capture system that includes an absorber and a stripper.