ELECTROCHEMICAL WATER GAS SHIFT REACTOR AND METHOD OF USE
Herein discussed is an electrochemical reactor comprising an ionically conducting membrane, wherein the reactor performs the water gas shift reactions electrochemically without electricity input, wherein electrochemical water gas shift reactions involve the exchange of an ion through the membrane and include forward water gas shift reactions, or reverse water gas shift reactions, or both. Also discussed herein is a reactor comprising: a bi-functional layer and a mixed conducting membrane; wherein the bi-functional layer and the mixed conducting membrane are in contact with each other, and wherein the bi-functional layer catalyzes reverse-water-gas-shift (RWGS) reaction and functions as an anode in an electrochemical reaction.
1 . An electrochemical reactor comprising an ionically conducting membrane, wherein the reactor performs the water gas shift reactions electrochemically without electricity input, wherein electrochemical water gas shift reactions involve the exchange of an ion through the membrane and include forward water gas shift reactions, or reverse water gas shift reactions, or both.
2 . The reactor of claim 1 comprising porous electrodes that comprise metallic phase and ceramic phase, wherein the metallic phase is electronically conductive, and wherein the ceramic phase is ionically conductive.
3 . The reactor of claim 2 , wherein the electrodes are separated by the membrane and are both exposed to a reducing environment.
4 . The reactor of claim 2 , wherein the electrodes comprise Ni or NiO and a material selected from the group consisting of YSZ, CGO, SDC, SSZ, LSGM, and combinations thereof.
5 . The reactor of claim 1 , wherein the ionically conducting membrane is impermeable to fluid flow.
6 . The reactor of claim 1 , wherein the ionically conducting membrane also conducts electrons and wherein the reactor comprises no interconnect.
7 . The reactor of claim 1 , wherein the membrane comprises CGO.
8 . The reactor of claim 1 , wherein the membrane comprises CoCGO.
9 . The reactor of claim 1 comprising a catalyst that promotes chemical reverse water gas shift (RWGS) reactions.
10 . The reactor of claim 1 , wherein the reactor also performs chemical water gas shift reactions.
11 . A reactor comprising: a bi-functional layer and a mixed conducting membrane; wherein the bi-functional layer and the mixed conducting membrane are in contact with each other, and wherein the bi-functional layer catalyzes reverse-water-gas-shift (RWGS) reaction and functions as an anode in an electrochemical reaction.
12 . The reactor of claim 11 , wherein the bi-functional layer as the anode is exposed to a reducing environment and the electrochemical reaction taking place in the bi-functional layer is oxidation.
13 . The reactor of claim 11 , wherein no current collector is attached to the bi-functional layer.
14 . The reactor of claim 11 , wherein the reactor comprises no interconnect, and wherein the reactor does not receive or produce electricity.
15 . The reactor of claim 11 , wherein the bi-functional layer comprises Ni or NiO and a material selected from the group consisting of YSZ, CGO, SDC, SSZ, LSGM, and combinations thereof.
16 . The reactor of claim 11 comprising a catalyst that promotes chemical reverse water gas shift (RWGS) reactions.
17 . The reactor of claim 16 wherein the catalyst is a high temperature RWGS catalyst.
18 . The reactor of claim 16 , wherein said catalyst is part of the bi-functional layer.
19 . The reactor of claim 16 , wherein said catalyst is configured to be outside of the bi-functional layer.
20 . The reactor of claim 16 , wherein the catalyst comprises Ni, Cu, Fe, Pt-group metals, or combinations thereof.