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Methods of using microchannel separation systems including absorbents to improve thermal efficiency and reduce parasitic power loss. Energy is typically added to desorb a solute and then energy or heat is removed to absorb a solute using a working solution. The working solution or absorbent may comp

Methods of using microchannel separation systems including absorbents to improve thermal efficiency and reduce parasitic power loss. Energy is typically added to desorb a solute and then energy or heat is removed to absorb a solute using a working solution. The working solution or absorbent may comprise an ionic liquid, or other fluids that demonstrate a difference in affinity between a solute and other gases in a solution.

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1. A method of operating a processing system comprising: providing a first microchannel including a first absorbent inlet, a first absorbent outlet, a feed stream inlet, and a first resultant gas outlet;providing a second microchannel including a second absorbent inlet, a second absorbent outlet, an

1. A method of operating a processing system comprising: providing a first microchannel including a first absorbent inlet, a first absorbent outlet, a feed stream inlet, and a first resultant gas outlet;providing a second microchannel including a second absorbent inlet, a second absorbent outlet, and a second resultant gas outlet, the second microchannel being arranged in a counterflow arrangement relative to the first microchannel;circulating an absorbent through the first microchannel and the second microchannel;receiving a flue gas feed including nitrogen and carbon dioxide through the feed stream inlet;exhausting, from the first resultant gas outlet, a first resultant gas having a higher concentration of nitrogen than the flue gas feed; and,exhausting, from the second resultant gas outlet, a second resultant gas having a higher concentration of carbon dioxide than the flue gas feed;wherein the absorbent has a temperature T1 at the first inlet, a temperature T2 at the first outlet, a temperature T3 at the second inlet, and a temperature T4 at the second outlet; and,wherein at least one of the following conditions is satisfied: T2 is greater than T3 and T1 is greater than T4. 2. A method of operating a processing system comprising: providing a first microchannel including a first absorbent inlet, a first absorbent outlet, a feed stream inlet, and a first resultant gas outlet;providing a second microchannel including a second absorbent inlet, a second absorbent outlet, and a second resultant gas outlet, the second microchannel being arranged in a counter flow arrangement relative to the first microchannel;circulating an absorbent through the first microchannel and the second microchannel;receiving a mixture including at least one hydrocarbon and nitrogen through the feed stream inlet;exhausting, from the first resultant gas outlet, a first resultant gas having a higher concentration of nitrogen than the mixture; and,exhausting, from the second resultant gas outlet, a second resultant gas having a higher concentration of the at least one hydrocarbon than the mixture;wherein the absorbent has a temperature T1 at the first inlet, a temperature T2 and the first outlet, a temperature T3 at the second inlet, and a temperature T4 at the second outlet; and,wherein at least one of the following conditions is satisfied: T2 is greater than T3 and T1 is greater than T4. 3. A method of operating a processing system comprising: providing a first microchannel including a first absorbent inlet, a first absorbent outlet, a feed stream inlet, and a first resultant gas outlet;providing a second microchannel including a second absorbent inlet, a second absorbent outlet, and a second resultant gas outlet, the second microchannel being arranged in a counterflow arrangement relative to the first microchannel; andcirculating an absorbent through the first microchannel and the second microchannel;receiving a mixture including at least one hydrocarbon and at least one contaminant through the feed stream inlet;exhausting, from the first resultant gas outlet, a first resultant gas having a higher concentration of the hydrocarbon than the mixture; andexhausting, from the second resultant gas outlet, a second resultant gas having a higher concentration of the contaminant than the mixture;wherein the absorbent has a temperature T1 at the first inlet, a temperature T2 at the first outlet, a temperature T3 at the second inlet, and a temperature T4 at the second outlet; and,wherein at least one of the following conditions is satisfied: T2 is greater than T3 and T1 is greater than T4. 4. The method of claim 3, wherein the mixture is a natural gas feed and the contaminant is at least one of H2S, a thiol, and another sulfur-containing compound. 5. The method of claim 3, further comprising the act of providing a first Fischer-Tropsch reactor, where the feed stream inlet is coupled to an outlet of the Fischer-Tropsch reactor. 6. The method of 5, further comprising the act of providing a second Fischer-Tropsch reactor, wherein at least one of the first resultant gas outlet and the second resultant gas outlet is coupled to an inlet of the second Fischer-Tropsch reactor. 7. A method of operating a processing system comprising: providing a first microchannel including a first absorbent inlet, a first absorbent outlet, a feed stream inlet, and a first resultant gas outlet;providing a second microchannel including a second absorbent inlet, a second absorbent outlet, and a second resultant gas outlet, the second microchannel being arranged in a counterflow arrangement relative to the first microchannel;circulating an absorbent through the first microchannel and the second microchannel;receiving a mixture including nitrogen and oxygen through the feed stream inlet;exhausting, from the first resultant gas outlet, a first resultant gas having a higher concentration of nitrogen than the mixture; and,exhausting, from the second resultant gas outlet, a second resultant gas having a higher concentration of oxygen than the mixture;wherein the absorbent has a temperature T1 at the first inlet, a temperature T2 at the first outlet, a temperature T3 at the second inlet, and a temperature T4 at the second outlet; and, wherein at least one of the following conditions is satisfied: T3 is greater than T2, T4 is greater than T1, and T2 is greater than T4. 8. A method of operating a processing system comprising: providing a first microchannel including a first absorbent inlet, a first absorbent outlet, a feed stream inlet, and a first resultant gas outlet;providing a second microchannel including a second absorbent inlet, a second absorbent outlet, and a second resultant gas outlet, the second microchannel being arranged in a counterflow arrangement relative to the first microchannel;circulating an absorbent through the first microchannel and the second microchannel;receiving a mixture including at least one hydrocarbon and at least one contaminant through the feed stream inlet;exhausting, from the first resultant gas outlet, a first resultant gas having a higher concentration of the hydrocarbon than the mixture; and,exhausting, from the second resultant gas outlet, a second resultant gas having a higher concentration of the contaminant than the mixture;wherein the absorbent has a temperature T1 at the first inlet, a temperature T2 at the first outlet, a temperature T3 at the second inlet, and a temperature T4 at the second outlet; and,wherein at least one of the following conditions is satisfied: T3 is greater than T2, T4 is greater than T1, and T2 is greater than T4. 9. The method of claim 8, wherein the mixture is a natural gas feed and the contaminant is at least one of H2S, a thiol, and another sulfur-containing compound. 10. The method of claim 8, further comprising the act of providing a first Fischer-Tropsch reactor, where the feed stream inlet is coupled to an outlet of the Fischer-Tropsch reactor. 11. The method of 10, further comprising the act of providing a second Fischer-Tropsch reactor, wherein at least one of the first resultant gas outlet and the second resultant gas outlet is coupled to an inlet of the second Fischer-Tropsch reactor.