Process and apparatus for separating carbon dioxide from a waste gas of a fluid bed catalytic cracking (FCC) installation
In a process for separating carbon dioxide from a waste gas ( 3 ) of a fluid bed catalytic cracking installation ( 1 ) containing carbon dioxide, nitrogen and possibly carbon monoxide, the waste gas ( 3 ) is separated by adsorption to form a gas enriched in carbon dioxide and depleted in nitrogen ( 29 ) and a gas rich in nitrogen and depleted in carbon dioxide ( 31 ), and at least a portion of the gas enriched in carbon dioxide and depleted in nitrogen is separated in a separation device ( 30 ) by way of separation at a temperature of less than 0° C. by partial condensation and/or by distillation to form a fluid rich in carbon dioxide ( 35 ) and a fluid depleted in carbon dioxide ( 37 ).
1. A process for separating carbon dioxide from a waste gas of a fluid bed catalytic cracking installation containing carbon dioxide, nitrogen and carbon monoxide, wherein:
i) at least a portion of the carbon monoxide of the waste gas is converted into carbon dioxide to form a flow enriched in carbon dioxide,
ii) the waste gas, or the flow enriched in carbon dioxide from step i), is separated by adsorption to form a gas enriched in carbon dioxide and depleted in nitrogen and a gas rich in nitrogen and depleted in carbon dioxide,
the process comprising:
separating at least a portion of the gas enriched in carbon dioxide and depleted in nitrogen in a separation device by separation at a temperature of less than 0° C. by partial condensation and/or by distillation to form a fluid rich in carbon dioxide and a fluid depleted in carbon dioxide,
wherein a portion of the fluid rich in carbon dioxide is sent to step ii) as a rinsing gas.
2. The process according to claim 1 , wherein the waste gas or the flow enriched in carbon dioxide is compressed upstream of step ii) to a pressure of between 2.5 and 10 bar abs.
3. The process according to claim 1 , wherein the gas rich in nitrogen and depleted in carbon dioxide contains less than 5 mol % CO 2 .
4. The process according to claim 1 , wherein the gas enriched in carbon dioxide and depleted in nitrogen contains more than 45 mol % CO 2 .
5. The process according to claim 1 , wherein the fluid depleted in carbon dioxide contains at most 15% CO 2 .
6. The process according to claim 1 , wherein the fluid depleted in carbon dioxide is compressed and mixed with the flow enriched in carbon dioxide sent to step ii).
7. The process according to claim 1 , wherein the gas rich in nitrogen and depleted in carbon dioxide is expanded in a turbine and is sent to the atmosphere.
8. The process according to claim 7 , wherein the gas rich in nitrogen and depleted in carbon dioxide is heated by a fluid originating from the fluid bed catalytic cracking installation or by at least a portion of the gas enriched in carbon dioxide and depleted in nitrogen or by at least a portion of the waste gas, or by at least a portion of the flow enriched in carbon dioxide.
9. The process according to claim 1 , wherein the waste gas is expanded upstream of step i) in a turbine and the flow enriched in carbon dioxide is compressed in a compressor driven by the turbine upstream of step ii).
10. The process according to claim 9 , wherein an electricity generator and/or a motor is mounted on the same shaft or the same speed-increasing gearing as the compressor for the flow enriched in carbon dioxide upstream of step ii) and the turbine for the waste gas.
11. The process according to claim 1 , wherein the fluid depleted in carbon dioxide and/or the gas rich in nitrogen and depleted in carbon dioxide is expanded in a turbine to a temperature of less than 0° C. and greater than −100° C. in a chamber containing the separation device.
12. The process according to claim 1 , wherein at least a portion of the carbon monoxide of the waste gas is converted into carbon dioxide to form a flow enriched in carbon dioxide by combustion of the carbon monoxide in air and in the presence of a fuel.
13. The process according to claim 1 , wherein no part of the gas enriched in carbon dioxide and depleted in nitrogen and/or of the fluid rich in carbon dioxide is sent to the fluid bed catalytic cracking installation.