This invention relates to a system and method for improving sulfur recovery from a Claus unit. More specifically, this invention provides a sorption based SO.sub.2 selective crosslinked polyionic liquid system and method for treating acid gas streams and minimizing sulfur dioxide emissions therefrom.

A resource recovery system for reducing carbon dioxide emissions is revealed. Salt is delivered to a first plasma decomposition unit and decomposed into sodium and chlorine. The sodium is sent to a hydrolysis unit and mixed with water to get pure hydrogen and sodium hydroxide which are respectively sent to a power generation unit for power generation and a carbon dioxide absorption unit to react with carbon dioxide from air and produce a mixture of sodium carbonate and sodium bicarbonate. Then the mixture is delivered to an electric heating unit and broken into carbon dioxide and sodium hydroxide. The carbon dioxide is sent to a second plasma decomposition unit and decomposed into carbon and oxygen gas which is delivered to the power generation unit for generating power. Thereby catalysts, power required, and coproducts are obtained during operation of the system. Therefore, the system offers energy, environmental, and economic benefits.

Provided is the use of a carboxylate compound as an absorbent for capturing carbon dioxide and/or in the preparation of an absorbent for capturing carbon dioxide. In the carboxylate compound, the carboxylate anion is a carboxylate radical with a carbon chain having a carbon atom number of more than 3, or a branched-chain carboxylate radical having a carbon atom number of more than 6; and the cation is a substituted quaternary ammonium ion, quaternary phosphorus ion, pyridinium ion, pyrrolium ion, piperidinium ion, imidazolium ion or metal ion. In the present invention, a method which can capture carbon dioxide in an efficient and energy-saving manner by using a carboxylate compound and has water stability is involved, and the method comprises the following step: putting an aqueous solution of a carboxylate compound in a carbon dioxide atmosphere to absorb carbon dioxide, thereby obtaining a carboxylate and carbon dioxide conjugate precipitated from water.

The plant according to the invention includes a reactor including a combustion chamber in which a fuel is fired with an oxidant to form a carbon dioxide-containing flue gas stream. The plant also includes a waste heat recovery unit in fluid connection with the combustion chamber, configured to capture heat from the flue gas stream. The plant also includes a flue gas compression unit in fluid connection with the waste heat recovery unit, configured to increase the pressure of the flue gas stream. The plant also includes a scrubber in fluid connection with the flue gas compression unit, configured to remove sulphur oxides and/or nitrogen oxides from the flue gas stream and to cool flue gas stream by means of the scrubbing medium. The plant also includes an absorption unit in fluid connection with the scrubber, configured to absorb carbon dioxide from the flue gas stream.

A method of recovering ammonia bicarbonate from a biogas and digestate liquor uses an arrangement of equipment in an operational arrangement that requires relatively modest capital investment and that operates with simplicity to provide solid ammonia bicarbonate. In a specific form the method achieves this by upgrading of biogas to produce a rejected stream having a high mole fraction of CO.sub.2 at an elevated pressure that eliminates the need for further compression when using the CO.sub.2 for recovery of ammonia bicarbonate. The method operates can operate at a high pH produced inherently in a digestate stripper by concurrently stripping dissolved CO.sub.2 from solution to improve the simplicity of solid AB recovery.

The present disclosure is related to systems and methods for the biological processing of hydrocarbon-containing substances. In particular embodiments, the systems and methods herein relate to pre-digestion of hydrocarbon containing substances and further processing of the same to produce hydrocarbon fuels, fertilizer, and other products.

The present disclosure relates to systems and methods for separation of sulfurous material(s) from a multi-component feed stream. The systems and methods can comprise contacting the multi-component feed stream with a solvent in a contacting column so that at least a portion of the sulfurous material(s) is transferred from the multi-component feed stream to the solvent. A stream of a substantially purified gas can thus be provided along with a liquid stream comprising at least a majority of the sulfurous material. In particular, the solvent can comprise liquid carbon dioxide, which can be particularly beneficial for removing sulfurous materials from multi-component feed streams.

A method that can efficiently dissolve a water-soluble component contained in a gas with smaller energy consumption is provided. A mist is produced from a liquid. The mist and carrier air is mixed to produce mist-containing air. A solution gas and the mist-containing air are supplied to a static mixer. The solution gas and the mist-containing are mixed by using the static mixer. The liquid mist is brought in contact with the solution gas to dissolve a water-soluble component that is contained in the solution gas into the liquid mist. The liquid mist that contains the water-soluble component dissolved aggregates and produces a solution that contains the water-soluble component dissolved.

An efficient low-energy carbon dioxide removal system comprises an automated air mover equipped with sensing devices to measure flow rate, volume, level, pressure, temperature and concentration. Packing materials and air-liquid distributors are used in a multi-stage catalytic reactor. The multi-stage catalytic reactor processes ambient air and generates pure carbon dioxide gas and generates exhausted gas released to ambient air. In operation, air contacts the base solution in the presence of a catalyst via the air mover, distributor, and packing materials. The air reacts with the base solution thereby generating a base solution having carbon dioxide and generating exhaust (absorption reaction). Next, the exhaust is released from the reactor. Next, a catalyst is added, heat is applied to the base solution having carbon dioxide thereby generating carbon dioxide and generating a base solution without carbon dioxide (desorption reaction).

Multi-stage ammonia-based decarbonization, characterized in that ammonia is used as an absorbent to absorb CO.sub.2 in a process gas in an absorber, and the absorber may include four or more stages of absorption, where a first-stage absorption, a second-stage absorption, a third-stage absorption, a fourth-stage absorption, and higher-stage absorptions may be sequentially arranged along the flow direction of the process gas; and the temperature of the process gas in the second and third-stage absorptions may be controlled not to be lower than the temperature of the process gas in the first-stage absorption, and the temperature of the process gas in the fourth and any higher-stage absorptions may be controlled to be lower than the temperature of the process gas in the first-stage absorption.