초록 ▼

High volumetric-efficiency thermally integrated systems for capturing a target gas from a process gas stream include a monolithic body and a distribution system. The monolithic body includes a first plurality of channels and a second plurality of channels each having sorbent surfaces that reversibly

High volumetric-efficiency thermally integrated systems for capturing a target gas from a process gas stream include a monolithic body and a distribution system. The monolithic body includes a first plurality of channels and a second plurality of channels each having sorbent surfaces that reversibly adsorb the target gas. The channels are in thermal communication such that heat from an exothermic adsorption of target gas in one plurality of channels is used by an endothermic desorption of target gas from the other plurality of channels. Methods for separating a target gas from a process gas stream include switching the high volumetric-efficiency thermally integrated systems between a first state and a second state. In the first state, the first plurality of channels undergoes desorption while the second undergoes adsorption. In the second state, the second plurality of channels undergoes desorption while the first plurality undergoes adsorption.

대표청구항 ▼

1. A method for separating a target gas from a process gas stream, the method comprising: performing a first stage comprising simultaneously: flowing a purge stream through a first plurality of discrete channels of a monolithic body to cause the target gas to desorb endothermically from sorbent surf

1. A method for separating a target gas from a process gas stream, the method comprising: performing a first stage comprising simultaneously: flowing a purge stream through a first plurality of discrete channels of a monolithic body to cause the target gas to desorb endothermically from sorbent surfaces of the first plurality of discrete channels and enter into the flowing purge stream, andflowing the process gas stream through a second plurality of discrete channels of the monolithic body to cause the target gas to adsorb exothermically into sorbent surfaces of the second plurality of discrete channels; andperforming a second stage comprising simultaneously: flowing the process gas stream through the first plurality of discrete channels to cause the target gas to adsorb exothermically into the sorbent surfaces of the first plurality of discrete channels, andflowing the purge stream through the second plurality of discrete channels to cause the target gas to desorb endothermically from the sorbent surfaces of the second plurality of discrete channels and enter into the flowing purge stream; andcollecting at least a portion of the target gas in the flowing purge stream;wherein individual channels of the first plurality of discrete channels are in thermal communication with individual channels of the second plurality of discrete channels, and the first plurality of discrete channels are not in fluidic communication with any of the second plurality of discrete channels. 2. The method of claim 1, wherein the monolithic body comprises a first monolith comprising the first plurality of discrete channels and a second monolith adjacent to the first monolith and comprising the second plurality of discrete channels. 3. The method of claim 1, further comprising switching from the performing the first stage to the performing the second stage by switching at least one valve. 4. The method of claim 1, further comprising switching from the performing the first stage to the performing the second stage by rotating the monolithic body about a rotational axis. 5. The method of claim 1, wherein: during the performing the first stage, adsorption of the target gas into the sorbent surfaces of the second plurality of discrete channels benefits from heat liberated by desorption of the target gas from the sorbent surfaces of the first plurality of discrete channels; andduring the performing the second stage, adsorption of the target gas into the sorbent surfaces of the first plurality of discrete channels benefits from heat liberated by desorption of the target gas from the sorbent surfaces of the second plurality of discrete channels. 6. A method for separating a target gas from a process gas stream, the method comprising: flowing the process gas stream through a first plurality of discrete channels of a first monolith of a monolithic body to cause the target gas to adsorb into sorbent surfaces of the first plurality of discrete channels; andperforming a thermally integrated first stage for a first cycle time, the thermally integrated first stage comprising simultaneously: flowing the process gas stream through a second plurality of discrete channels of a second monolith of the monolithic body to cause the target gas to adsorb exothermically into sorbent surfaces of the second plurality of discrete channels, the second plurality of discrete channels and the first plurality of discrete channels arranged such that individual channels of the second plurality of discrete channels are in thermal communication with individual channels of the first plurality of discrete channels, and the second plurality of discrete channels are not in fluidic communication with any of the first plurality of discrete channels; andpurging the first plurality of discrete channels with a flowing purge stream to cause the target gas to desorb endothermically from the sorbent surfaces of the first plurality of discrete channels and enter into the flowing purge stream. 7. The method of claim 6, wherein each discrete first channel is parallel to a first flow axis of the monolithic body and each discrete second channel is parallel to a second flow axis of the monolithic body. 8. The method of claim 6, further comprising: performing a thermally integrated second stage for a second cycle time, the thermally integrated second stage comprising simultaneously: flowing the process gas stream through the first plurality of discrete channels to cause the target gas to adsorb exothermically into the sorbent surfaces of the first plurality of discrete channels; andpurging the second plurality of discrete channels with the flowing purge stream to cause the target gas to desorb endothermically from the sorbent surfaces of the second plurality of discrete channels and enter into the flowing purge stream. 9. The method of claim 8, wherein: the thermally integrated first stage further comprises exhausting process gas exhaust from the second plurality of discrete channels and purge exhaust from the first plurality of discrete channels; andthe thermally integrated second stage further comprises exhausting process gas exhaust from the first plurality of discrete channels and purge exhaust from the second plurality of discrete channels. 10. The method of claim 9, wherein: the exhausting in the thermally integrated first stage is simultaneous with the flowing of the process gas stream through the second plurality of discrete channels and the purging the first plurality of discrete channels with the flowing purge stream; andthe exhausting in the thermally integrated second stage is simultaneous with the flowing of the process gas stream through the first plurality of discrete channels and the purging the second plurality of discrete channels with the flowing purge stream. 11. The method of claim 8, further comprising: delivering the process gas to the monolithic body from a process gas source in fluidic communication with only the second plurality of discrete channels during the thermally integrated first stage and with only the first plurality of discrete channels during the thermally integrated second stage; anddelivering the purge stream to the monolithic body from a purge source in fluidic communication with only the first plurality of discrete channels during the thermally integrated first stage and with only the second plurality of discrete channels during the thermally integrated second stage. 12. The method of claim 11, further comprising cycling between the thermally integrated first stage and the thermally integrated second stage. 13. The method of claim 12, wherein cycling between the thermally integrated first stage and the thermally integrated second stage comprises in sequence: performing the thermally integrated first stage;rotating the monolithic body about a rotational axis perpendicular to a first flow axis and a second flow axis to place the first plurality of discrete channels in fluidic communication with the process gas source and to place the second plurality of discrete channels in fluidic communication with the purge source;performing the thermally integrated second stage; androtating the monolithic body about the rotational axis to place the second plurality of discrete channels in fluidic communication with the process gas source and to place the first plurality of discrete channels in fluidic communication with the purge source. 14. The method of claim 13, wherein the first flow axis is perpendicular to the second flow axis. 15. The method of claim 8, wherein: the first cycle time is less than a first breakthrough time at which the sorbent surfaces of the second plurality of discrete channels are saturated with the target gas; andthe second cycle time is less than a second breakthrough time at which the sorbent surfaces of the first plurality of discrete channels are saturated with the target gas. 16. The method of claim 6, wherein the process gas stream comprises a process gas concentration of the target gas of up to 50 mol. %, and the purge stream comprises a purge concentration of the target gas of less than 1 mol. %. 17. The method of claim 6, wherein the process gas stream is selected from the group consisting of natural gas, flue gas, air, biogas, a water gas-shift mixture from a hydrogen gas production process, and exhaust gas from a combustion process. 18. The method of claim 6, wherein the target gas is selected from the group consisting of carbon dioxide and hydrogen sulfide. 19. The method of claim 6, wherein the target gas is carbon dioxide.