Abstract: A process for the removal of co2 from a gas comprising the steps of: (a) contacting the gas (1) in an absorber (2) with an aqueous solution of one or more carbonate compounds in the presence of an accelerator, thereby reacting at least part of the co2 to form a bicarbonate compound, under conditions such that at least a part of the bicarbonate compound formed precipitates, forming a bicarbonate slurry; (b) subjecting at least part of the bicarbonate slurry to a concentration step (5) to obtain an aqueous solution (6) and a concentrated bicarbonate slurry (7), wherein the concentrated bicarbonate slurry comprises from 20 to 80 wt % of bicarbonate compounds; (c) returning at least part of the aqueous solution to the absorber; (d) pressurising (8) the concentrated bicarbonate slurry, (e) transferring the pressurized concentrated bicarbonate slurry to a regenerator (12) and applying heat to obtain a co2-rich gas stream (13) and a regenerated carbonate stream (14).

Abstract: Process for the removal of CO2 from a gas comprising CO2, comprising the steps of: (a) contacting the gas in an absorber (102) with an aqueous solution of one or more carbonate compounds in the presence of an accelerator, thereby reacting at least part of the CO2 to form a bicarbonate compound, under conditions such that at least a part of the bicarbonate compound formed precipitates, forming a bicarbonate slurry; (b) subjecting at least part of the bicarbonate slurry to a concentration step (105) to obtain the aqueous solution and a concentrated bicarbonate slurry, wherein the concentrated bicarbonate slurry comprises in the range of from 10 to 60 wt % of bicarbonate compounds; (c) returning at least part of the aqueous solution to the absorber; (d) transferring a first part of the concentrated bicarbonate slurry to a first heat exchanger (110a), wherein the first part of the slurry is being heated against a hot lean solvent of a regenerator (112); (e) transferring a second part of the concentrated bicarbona

Abstract: A process for the removal of CO2 and/or H2S from a gas comprising CO2 and/or H2S. The process comprises contacting the gas in an absorber with an absorbing solution wherein the absorbing solution absorbs at least part of the CO2 and/or H2S so as, to produce a CO2 and/or H2S lean gas and a CO2 and/or H2S rich absorbing solution. At least part of the CO2 and/or H2S rich absorbing solution is heated to produce a heated CO2 and/or H2S rich absorbing solution. At least part of the CO2 and/or H2S is removed from the heated CO2 and/or H2S rich absorbing solution in a regenerator to produce a CO2 and/or H2S rich gas and a CO2 and/or H2S lean absorbing solution. In the process, at least part of the heat for heating the CO2 and/or H2S rich absorbing solution in step b) is obtained in a sequence of multiple heat exchangers.

Abstract: A process for the removal of co2 from a gas comprising the steps of: (a) contacting the gas (1) in an absorber (2) with an aqueous solution of one or more carbonate compounds in the presence of an accelerator, thereby reacting at least part of the co2 to form a bicarbonate compound, under conditions such that at least a part of the bicarbonate compound formed precipitates, forming a bicarbonate slurry; (b) subjecting at least part of the bicarbonate slurry to a concentration step (5) to obtain an aqueous solution (6) and a concentrated bicarbonate slurry (7), wherein the concentrated bicarbonate slurry comprises from 20 to 80 wt % of bicarbonate compounds; (c) returning at least part of the aqueous solution to the absorber; (d) pressurising (8) the concentrated bicarbonate slurry, (e) transferring the pressurised concentrated bicarbonate slurry to a regenerator (12) and applying heat to obtain a co2-rich gas stream (13) and a regenerated carbonate stream (14).

Abstract: A process for the treatment of a high-pressure hydrocarbon gas stream to make a carbon dioxide-rich product stream and a treated hydrocarbon gas product stream by contacting within a contactor the high-pressure hydrocarbon gas stream with a solvent containing aqueous ammonia and, optionally, a reaction product of a liquid ammonia-carbon dioxide-water system. A fat solvent containing precipitated solids is withdrawn from the contactor and is regenerated whereby carbon dioxide is released and the fat solvent and a lean solvent is provided for reuse as the solvent.

Abstract: A method of treating a high-pressure hydrocarbon stream, such as natural or synthetic gas, contaminated with a high concentration of carbon dioxide, by contacting the contaminated high-pressure hydrocarbon stream with a chilled aqueous ammonia solution in an absorber at high pressure to produce a treated gas stream having a substantially reduced carbon dioxide content and a carbon dioxide-rich ammonia solution. The carbon dioxide-rich ammonia solution is regenerated by stripping, thus producing a concentrated carbon dioxide stream at high pressure suitable for sequestration or other uses.