Carbon dioxide recovery
The present techniques are directed to a system and method for recovering carbon dioxide (CO 2 ). The method includes recovering the CO 2 from a gas mixture including the CO 2 via a CO 2 separation system. The CO 2 separation system includes a rotating freezer/melter.
1. A method for recovering carbon dioxide (CO 2 ), comprising:
receiving, in a CO 2 separation system, a gas mixture from a power plant, wherein the gas mixture comprises CO 2 , and the CO 2 separation system comprises:
a rotating freezer/melter having a freezing zone, a melting zone, and a rotor;
a CO 2 separation device downstream of the freezing zone of the rotating freezer/melter; and
a compressor downstream of the CO 2 separation device;
flowing the gas mixture through the rotor while the rotor is in the freezing zone;
capturing solid CO 2 from the gas mixture on the rotor while the rotor is in the freezing zone;
melting the solid CO 2 captured on the rotor while the rotor is in the melting zone, thereby forming liquid CO 2 ;
flowing the liquid CO 2 through the rotor while the rotor is in the melting zone;
maintaining the melting zone at a higher pressure than the freezing zone to preserve the melted CO 2 in a liquid state as it exits the melting zone;
routing the remaining gas mixture out of the freezing zone and into the CO 2 separation device;
recovering residual CO 2 from the remaining gas mixture using the CO 2 separation device;
pressurizing the residual CO 2 using the compressor to produce a pressurized CO 2 vapor stream; and
using the pressurized CO 2 vapor stream to melt the solid CO 2 within the melting zone of the rotating freezer/melter.
2. The method of claim 1 , further comprising pumping at least a portion of the melted CO 2 using a pump disposed downstream of the rotating freezer/melter, thereby generating pressurized liquid CO 2 .
3. The method of claim 2 , further comprising converting the pressurized liquid CO 2 to a vapor CO 2 stream using a refrigeration load.
4. The method of claim 3 , further comprising using the refrigeration load to chill cooling water for the power plant.
5. The method of claim 3 , further comprising using the vapor CO 2 stream in enhanced oil recovery (EOR) operations.
6. The method of claim 1 , further using a dehydration system to remove H 2 O from the gas mixture prior to receiving the gas mixture in the CO 2 separation system.
7. The method of claim 1 , wherein the CO 2 separation system further comprises a heat exchanger and a first expander.
8. The method of claim 7 , further comprising, prior to flowing the gas mixture through the rotor:
cooling the gas mixture using the heat exchanger; and
flowing the gas mixture through the first expander, thereby forming solid CO 2 from at least a portion of the CO 2 in the gas mixture.
9. The method of claim 8 , wherein the gas mixture is cooled via indirect heat exchange.
10. The method of claim 8 , further comprising flowing the remaining gas mixture to the heat exchanger prior to routing the remaining gas mixture to the CO 2 separation device, wherein the heat exchanger cools the gas mixture via indirect exchange with the remaining gas mixture.
11. The method of claim 8 , wherein the first expander lowers the pressure and temperature of the gas mixture thereby freezing at least a portion of CO 2 within the gas mixture to pure solid CO 2 .
12. The method of claim 1 , wherein the CO 2 separation device recovers the residual CO 2 from the remaining gas mixture via a potassium carbonate separation process.
13. The method of claim 1 , further comprising:
recycling a portion of the liquid CO 2 to the melting zone of the rotating freezer/melter; and
using the portion of the liquid CO 2 to melt the solid CO 2 within the melting zone.
14. The method of claim 1 , wherein an exhaust gas from the power plant provides the gas mixture.
15. The method of claim 1 , comprising producing power via the power plant.
16. The method of claim 15 , wherein producing power via the power plant comprises:
providing mechanical energy via an expander turbine using energy extracted from the gas mixture after combustion of the gas mixture in a combustor; and
generating electricity via a generator using the mechanical energy provided by the expander turbine.
17. The method of claim 15 , wherein producing the power via the power plant comprises:
providing mechanical energy via an expander turbine using energy extracted from the gas mixture after combustion of the gas mixture in a combustor;
generating steam via a heat recovery steam generator (HRSG) by heating a boiler with an exhaust stream from the expander turbine;
providing mechanical energy via a steam turbine using energy extracted from the steam generated by the HRSG; and
generating electricity via a generator using the mechanical energy provided by the expander turbine and the steam turbine.
18. The method of claim 1 , further comprising recycling a portion of the gas mixture to the power plant.