SYSTEM AND METHOD FOR CARBON DIOXIDE REACTOR CONTROL

1 . A system comprising:

a carbon dioxide electrolyzer comprising an inlet configured to receive carbon dioxide and a cathode configured electrochemically reduce the carbon dioxide;

a first carbon dioxide absorption unit comprising (i) a first CO 2 absorption unit having a first carbon dioxide sorbent and (ii) an inlet for receiving a first stream of impure carbon dioxide;

a second carbon dioxide absorption unit comprising (i) a second CO 2 absorption unit having a second carbon dioxide sorbent and (ii) an inlet for receiving a second stream of impure carbon dioxide; and

a desorption unit configured to receive the first carbon dioxide sorbent from the first carbon dioxide absorption unit and the second carbon dioxide sorbent from the second carbon dioxide absorption unit, wherein the desorption unit is further configured to desorb purified carbon dioxide for reaction at the cathode of the carbon dioxide electrolyzer.

2 . The system of claim 1 , wherein the first stream of impure carbon dioxide comprises unreacted carbon dioxide from the cathode of the carbon dioxide electrolyzer.

3 . The system of claim 1 , wherein the second stream of impure carbon dioxide comprises a feedstock of carbon dioxide to the system.

4 . The system of claim 3 , wherein the feedstock of carbon dioxide comprises air or a flue gas.

5 . The system of claim 1 , wherein the second stream of impure carbon dioxide comprises carbon monoxide and/or hydrogen produced by a reformer.

6 . The system of claim 1 , wherein the system is configured to transfer heat generated by the carbon dioxide electrolyzer to the desorption unit.

7 . The system of claim 1 , wherein the first sorbent and/or the second sorbent comprises an amine.

8 . The system of claim 1 , further comprising a downstream reactor configured to receive a carbon-containing reaction product generated at the cathode of the carbon dioxide electrolyzer, or a derivative of the carbon-containing reaction product, and react said carbon-containing reaction product or derivative thereof in an exothermic chemical reaction, wherein this system is configured to transfer heat from the exothermic chemical reaction to the carbon dioxide desorption unit.

9 . The system of claim 8 , wherein the downstream reactor is a liquid hydrocarbon synthesis reactor.

10 . The system of claim 1 , wherein the carbon dioxide electrolyzer comprises a membrane electrode assembly.

11 . A method comprising:

electrochemically reducing carbon dioxide at a cathode of a carbon dioxide electrolyzer;

receiving a first stream of impure carbon dioxide at a first CO 2 absorption unit having a first carbon dioxide sorbent;

receiving a second stream of impure at a second CO 2 absorption unit having a second carbon dioxide sorbent;

receiving the first carbon dioxide sorbent and the second carbon dioxide sorbent at a desorption unit;

desorbing purified carbon dioxide at the desorption unit; and

providing the purified carbon dioxide for reaction at the cathode of the carbon dioxide electrolyzer.

12 .- 20 . (canceled)

21 . A system comprising:

a carbon dioxide electrolyzer comprising an inlet configured to receive carbon dioxide and a cathode configured electrochemically reduce the carbon dioxide to produce carbon monoxide;

a carbon dioxide purification unit configured to perform a pressure-mediated separation of carbon dioxide from an impure carbon dioxide inlet stream; and

a liquid hydrocarbon synthesis reactor configured to react carbon monoxide produced by the carbon dioxide electrolyzer and produce a mixture of liquid hydrocarbons and a tail gas comprising one or more volatile hydrocarbons,

wherein the system is configured to provide tail gas produced by the liquid hydrocarbon production reactor to the carbon dioxide purification unit to thereby facilitate purification of carbon dioxide from the impure carbon dioxide stream, and

wherein the system is further configured to provide purified carbon dioxide from the carbon dioxide purification unit to the inlet of the carbon dioxide electrolyzer.

22 . The system of claim 21 , wherein the liquid hydrocarbon synthesis reactor is a Fischer-Tropsch reactor.

23 . The system of claim 21 , wherein the carbon dioxide purification unit is configured to perform a pressure swing carbon dioxide purification process in which carbon dioxide is absorbed from the impure carbon dioxide inlet stream at a first pressure and carbon dioxide is released during exposure to the tail gas at a second pressure, and wherein the second pressure is greater than the first pressure.

24 . The system of claim 23 , wherein the carbon dioxide purification unit comprises a sorbent.

25 . The system of claim 21 , wherein the impure carbon dioxide inlet stream comprises an output gas stream from the cathode of the carbon dioxide electrolyzer.

26 . The system of claim 21 , wherein the impure carbon dioxide inlet stream comprises air or a flue gas.

27 . The system of claim 21 , further comprising a source of hydrogen configured to produce hydrogen that mixes with the carbon monoxide produced by the carbon dioxide electrolyzer for input to the liquid hydrocarbon production reactor.

28 . The system of claim 27 , wherein the source of hydrogen is a water electrolyzer.

29 . The system of claim 21 , wherein the carbon dioxide electrolyzer comprises a membrane electrode assembly.

30 . The system of claim 29 , wherein the membrane electrode assembly comprises a bipolar membrane.

31 . A method comprising:

electrochemically reducing carbon dioxide to carbon monoxide at a cathode of a carbon dioxide electrolyzer;

reacting the carbon monoxide to produce a mixture of liquid hydrocarbons and a tail gas comprising one or more volatile hydrocarbons;

using the tail gas to facilitate purification of an impure carbon dioxide stream by performing a pressure-mediated separation of carbon dioxide from the impure carbon dioxide stream and producing purified carbon dioxide; and

providing the purified carbon dioxide to the cathode of the carbon dioxide electrolyzer.

32 .- 60 . (canceled)