Method for drying a wet CO2 rich gas stream from an oxy-combustion process
A method for drying a wet CO 2 rich gas stream from an oxy-combustion process that includes: compressing the wet CO 2 rich gas stream to a drying process operating pressure, cooling the wet CO 2 rich gas stream in at least one cooler, alternately drying the wet CO 2 rich gas stream in at least one dryer which contains at least one desiccant bed and regenerating the desiccant bed by conducting a heated regenerating gas through the dryer in opposite direction to the flow direction of the wet CO 2 rich gas stream, separating the dried CO 2 rich gas stream in a purification process to a purified CO 2 gas stream and a waste gas stream rich in nitrogen and oxygen, whereby the waste gas stream rich in nitrogen and oxygen is used as regenerating gas, and subsequently to the regeneration the dryer is purged at least once by a pressurized CO 2 rich gas stream conducted from the compressor, and whereby the dryer is charged up to the drying process operating pressure with a pressurized CO 2 rich gas stream conducted from the compressor before each drying process.
1. A method for drying a wet CO 2 rich gas stream from an oxy-combustion process, the method comprising:
compressing the wet CO 2 rich gas stream to a drying process operating pressure,
cooling the wet CO 2 rich gas stream in at least one cooler,
alternately drying the wet CO 2 rich gas stream in at least one dryer which contains at least one desiccant bed and regenerating the desiccant bed by conducting a heated regenerating gas through the dryer in opposite direction to the flow direction of the wet CO 2 rich gas stream,
separating the dried CO 2 rich gas stream in a purification process to a purified CO 2 gas stream and a waste gas stream rich in nitrogen and oxygen,
whereby the waste gas stream rich in nitrogen and oxygen is used as regenerating gas,
and subsequently to the regeneration the dryer is purged at least once by a pressurized CO 2 rich gas stream conducted from a compressor,
and whereby the dryer is charged up to the drying process operating pressure with the pressurized CO 2 rich gas stream conducted from the compressor before each drying process.
2. The method according to claim 1 , wherein the drying process operating pressure is between 10 to 60 bar.
3. The method according to claim 1 , wherein the pressure of the regenerating gas during the regenerating process lies below the drying process operating pressure.
4. The method according to claim 1 , wherein the pressurized CO 2 rich gas stream for purging the dryer is taken directly downstream from the compressor and fed directly to the dryer.
5. The method according to claim 1 , wherein the pressurized CO 2 rich gas stream for charging the dryer before each drying process is taken directly downstream from the compressor and fed directly to the dryer.
6. The method according to claim 1 , wherein Hg and/or SOx and/or dust contained in the wet CO 2 rich gas stream is removed by a flue gas treatment device located upstream of the dryer.
7. The method according to claim 1 , wherein a portion of vapour contained in the wet CO 2 rich gas stream is condensed and discharged by a vapour liquid separator located upstream of the dryer.
8. The method according to claim 1 , wherein the regenerating gas stream is heated by a heater to a temperature of 160 to 300° C.
9. The method according to claim 1 , wherein for drying the wet CO 2 rich gas stream two or more dryers are used and arranged in parallel to each other and whereby one dryer is in drying mode and the other(s) is/are in regeneration mode or in stand-by mode.