SYSTEM AND METHOD FOR CARBON DIOXIDE REACTOR CONTROL
A system optionally including a carbon oxide reactor. A method for carbon oxide reactor control, optionally including selecting carbon oxide reactor aspects based on a desired output composition, running a carbon oxide reactor under controlled process conditions to produce a desired output composition, and/or altering the process conditions to alter the output composition.
1 . A system for producing one or more chemical compounds, the system comprising:
(a) a carbon dioxide capture unit configured to capture carbon dioxide from an impure carbon dioxide source and output carbon dioxide at a concentration greater than the concentration of carbon dioxide in the impure carbon dioxide source;
(b) a carbon dioxide reduction electrolyzer comprising a membrane electrode assembly, which comprises one or more ion conductive polymer layers and a cathode catalyst for facilitating chemical reduction of the carbon dioxide to a carbon-containing reaction product; and
(c) a heat transfer unit configured to transfer excess heat generated by the carbon dioxide reduction electrolyzer to the carbon dioxide capture unit and facilitate carbon dioxide capture and/or carbon dioxide release by the carbon dioxide capture unit,
wherein the system is configured to provide carbon dioxide from the carbon dioxide capture unit to the carbon dioxide reduction electrolyzer.
2 . The system of claim 1 , wherein the carbon dioxide reduction electrolyzer is configured to produce, during operation, humidity, and wherein the system is configured to deliver the humidity produced by the carbon dioxide reduction electrolyzer to the carbon dioxide capture unit, and wherein the carbon dioxide capture unit is configured to release captured carbon dioxide upon exposure to the humidity.
3 . The system of claim 1 , wherein the system is further configured to transport excess carbon dioxide from the carbon dioxide reduction reactor to the carbon dioxide capture unit where the excess carbon dioxide is purified.
4 . The system of claim 1 , wherein the impure carbon dioxide source is air.
5 . The system of claim 1 , wherein the heat transfer unit comprises a heat exchanger configured to receive the excess heat generated by the carbon dioxide reduction electrolyzer.
6 . The system of claim 1 , wherein the carbon dioxide capture unit comprises a sorbent bed configured to capture carbon dioxide at a first temperature and release carbon dioxide at a second temperature, wherein the second temperature is higher than the first temperature.
7 . The system of claim 1 , wherein the system is configured to transport anode water from an outlet of the carbon dioxide capture unit to the heat transfer unit.
8 . The system of claim 7 , wherein the system is further configured to recycle the anode water from the heat transfer unit to the carbon dioxide reduction electrolyzer.
9 . The system of claim 1 , wherein the system is configured to transport a gas stream comprising the carbon-containing reaction product from an outlet of the carbon dioxide capture unit to the heat transfer unit.
10 . The system of claim 9 , wherein the system is further configured to transport anode water from an outlet of the carbon dioxide capture unit to a second heat transfer unit configured to transfer heat to the carbon dioxide capture unit.
11 . The system of claim 1 , wherein the carbon-containing reaction product comprises carbon monoxide and wherein the system is configured to combine hydrogen with the carbon monoxide and produce syngas.
12 . The system of claim 11 , further comprising a water electrolyzer configured to produce the hydrogen.
13 . The system of claim 11 , further comprising a Fischer-Tropsch reactor configured to receive the syngas.
14 . The system of claim 13 , further comprising a second heat transfer unit configured to transfer excess heat generated by the Fischer-Tropsch reactor to the carbon dioxide capture unit and facilitate carbon dioxide capture and/or carbon dioxide release by the carbon dioxide capture unit.
15 . The system of claim 11 , further comprising a methanol synthesis reactor configured to receive the syngas.
16 . The system of claim 15 , further comprising a second heat transfer unit configured to transfer excess heat generated by the methanol synthesis reactor to the carbon dioxide capture unit and facilitate carbon dioxide capture and/or carbon dioxide release by the carbon dioxide capture unit.
17 . A method comprising:
(a) reducing carbon dioxide to a carbon containing product in a carbon dioxide reduction electrolyzer comprising a membrane electrode assembly, which comprises one or more ion conductive polymer layers and a cathode catalyst for facilitating chemical reduction of carbon dioxide to the carbon containing product;
(b) transferring excess heat generated by the carbon dioxide reduction electrolyzer to a carbon dioxide capture unit configured to capture carbon dioxide from an impure carbon dioxide source and output carbon dioxide at a concentration greater than the concentration of carbon dioxide from the impure carbon dioxide source; and
(c) transferring the output carbon dioxide to the carbon dioxide reduction electrolyzer.
18 . The method of claim 17 , further comprising:
producing humidity while reducing carbon dioxide at the carbon dioxide reduction electrolyzer, and
delivering the humidity to the carbon dioxide capture unit and facilitating release of captured carbon dioxide upon exposure to the humidity.
19 . The method of claim 17 , further comprising transporting excess carbon dioxide from the carbon dioxide reduction reactor to the carbon dioxide capture unit where the excess carbon dioxide is purified.
20 . The method of claim 17 , wherein the impure carbon dioxide source is air.
21 . The method of claim 17 , wherein transferring excess heat generated by the carbon dioxide reduction electrolyzer to the carbon dioxide capture unit comprises transferring the excess heat to a heat exchanger.
22 . The method of claim 17 , wherein the carbon dioxide capture unit comprises a sorbent bed that captures carbon dioxide at a first temperature and releases carbon dioxide at a second temperature, wherein the second temperature is higher than the first temperature.
23 . The method of claim 17 , wherein transferring excess heat generated by the carbon dioxide reduction electrolyzer to the carbon dioxide capture unit comprises transporting anode water from an outlet of the carbon dioxide capture unit to the carbon dioxide capture unit.
24 . The method of claim 23 , further comprising recycling the anode water from the carbon dioxide capture unit to the carbon dioxide reduction electrolyzer.
25 . The method of claim 17 , wherein transferring excess heat generated by the carbon dioxide reduction electrolyzer to the carbon dioxide capture unit comprises transporting a gas stream comprising the carbon-containing reaction product from an outlet of the carbon dioxide capture unit to the carbon dioxide capture unit.
26 . The method of claim 25 , wherein transferring excess heat generated by the carbon dioxide reduction electrolyzer to the carbon dioxide capture unit further comprises transporting anode water from an outlet of the carbon dioxide capture unit to the carbon dioxide capture unit.
27 . The method of claim 17 , wherein the carbon-containing reaction product comprises carbon monoxide and wherein the method further comprises combining hydrogen with the carbon monoxide and producing syngas.
28 . The method of claim 27 , further comprising electrolyzing water to produce the hydrogen.
29 . The method of claim 27 , further comprising providing the syngas to a Fischer-Tropsch reactor.
30 . The method of claim 29 , further comprising transferring excess heat generated by the Fischer-Tropsch reactor to the carbon dioxide capture unit.
31 . The method of claim 27 , further comprising providing the syngas to a methanol synthesis reactor.
32 . The method of claim 31 , further comprising transferring excess heat generated by the methanol synthesis reactor to the carbon dioxide capture unit.
33 . A system comprising:
(a) a carbon dioxide reduction electrolyzer comprising a membrane electrode assembly, which comprises one or more ion conductive polymer layers and a cathode catalyst for facilitating chemical reduction of carbon dioxide to a carbon containing compound;
(b) one or more reactors configured to receive the carbon containing compound produced by the carbon dioxide reduction electrolyzer or a derivative of the carbon containing compound, and produce one or more product chemicals; and
(c) a heat accepting unit configured to receive excess heat generated by the carbon dioxide reduction electrolyzer and facilitate production of the one or more product chemicals.
34 .- 48 . (canceled)
49 . A system for producing methanol from carbon dioxide, the system comprising:
(a) a carbon dioxide reduction electrolyzer comprising a membrane electrode assembly, which comprises one or more ion conductive polymer layers and a cathode catalyst for facilitating chemical reduction of carbon dioxide to carbon monoxide;
(b) a methanol synthesis reactor configured to produce methanol from the carbon monoxide and hydrogen, wherein the system is configured to transport the carbon monoxide from the carbon dioxide reduction electrolyzer to the methanol synthesis reactor; and
(c) a heat transfer unit configured to transfer excess heat generated by the methanol synthesis reactor to an auxiliary component of the system.
50 .- 62 . (canceled)
63 . A system for producing liquid hydrocarbons from carbon dioxide, the system comprising:
(a) a carbon dioxide reduction electrolyzer comprising a membrane electrode assembly, which comprises one or more ion conductive polymer layers and a cathode catalyst for facilitating chemical reduction of carbon dioxide to carbon monoxide;
(b) a Fischer-Tropsch reactor configured to produce a liquid hydrocarbon mixture from the carbon monoxide and hydrogen, wherein the system is configured to transport the carbon monoxide from the carbon dioxide reduction electrolyzer to the Fischer-Tropsch reactor; and
(c) a heat transfer unit configured to transfer excess heat generated by the Fischer-Tropsch reactor to an auxiliary component of the system.
64 .- 78 . (canceled)