# US 9,518,329 B2 · Method for electrochemically converting carbon dioxide > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 9,518,329 B2 - Document ID: US9518329B2 - Status: Granted - Kind: B2 - Application number: 13/567,169 - Filed: 2012-08-06 - Published: 2013-06-13 - Granted: 2016-12-13 - Earliest claimed: 2011-12-12 - Assignees: Tsinghua University; Hon Hai Precision Industry Co., Ltd. - Applicants: Cheng Wang; Chen-Chen Zhao; Zhi-Xiang Liu; Jian-Wei Guo; Xiang-Ming He - Inventors: Cheng Wang; Chen-Chen Zhao; Zhi-Xiang Liu; Jian-Wei Guo; Xiang-Ming He - Web page: https://patentgrep.com/patent/US9518329B2 ## CPC - C25B 3/25: Reduction - C25B 1/02: Hydrogen or oxygen - C25B 3/07: Oxygen containing compounds - C25B 3/26: of carbon dioxide - C25B 9/19: with diaphragms - C25B 9/40: Cells or assemblies of cells comprising electrodes made of particles; Assemblies of constructional parts thereof - C25B 15/08: Supplying or removing reactants or electrolytes; Regeneration of electrolytes - C25B 15/087: {Recycling of electrolyte to electrochemical cell} - H01M 16/003: {of fuel cells with other electrochemical devices, e.g. capacitors, electrolysers} - Y02E 60/36: Hydrogen production from non-carbon containing sources, e.g. by water electrolysis - Y02E 60/50: Fuel cells - C25B: ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR (anodic or cathodic protection C23F13/00; single-crystal growth C30B) - H01M: PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY - Y02E: REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION ## Abstract A method for electrochemically converting a carbon dioxide gas into expected products includes using a member reactor. In the method, a membrane reactor includes a cavity, a solid electrolyte membrane separator, a cathode, an anode, and a fuel cell is provided. A cathode electrolyte and the carbon dioxide gas are passed through the cathode, and an anode electrolyte and an anode active material are passed through the anode chamber at the same time. An electrolytic voltage is applied to decompose the carbon dioxide gas into expected products. The expected products include a hydrogen gas and an oxygen gas which are fed back to the fuel cell to generate electric power. ## Claims ### Claim 1 A method for electrochemically converting carbon dioxide gas, the method comprising the following steps: providing a membrane reactor comprising a fuel cell, a cavity, a solid electrolyte membrane separator disposed in the cavity and dividing the cavity into a cathode chamber and an anode chamber, a cathode disposed in the cathode chamber, and an anode disposed in the anode chamber, the cathode being a trickle bed consisting of a porous conductive layer and a plurality of cathode catalyst particles disposed on the porous conductive layer; feeding a cathode electrolyte and the carbon dioxide gas into the cathode chamber and continuously feeding an anode electrolyte and an anode active material into the anode chamber simultaneously, wherein the cathode electrolyte is fed as liquid drops trickled through the plurality of cathode catalyst particles and the carbon dioxide gas is fed by continuously passing through the plurality of cathode catalyst particles simultaneously, the cathode electrolyte trickled through the plurality of cathode catalyst particles appears as a film and flows on surfaces of the plurality of cathode catalyst particles; decomposing the carbon dioxide gas by applying an electrolytic voltage between the cathode and the anode by the fuel cell, the carbon dioxide gas is decomposed to form hydrogen and oxygen; and feeding the hydrogen and the oxygen back to the fuel cell to generate electric power; wherein the porous conductive layer comprises a plurality of through holes, the plurality of through holes extend from one side to another side along a thickness direction of the porous conductive layer in a curvy manner, a porosity of the porous conductive layer is about 60%, and the cathode catalyst particles is deposited in the plurality of through holes, all of the plurality of cathode catalyst particles are deposited on inner walls of the through holes; and the cathode electrolyte and the carbon dioxide gas are fed through the plurality of through holes. ### Claim 2 (depends on 1) The method of claim 1 further comprises boosting the carbon dioxide gas before feeding the carbon dioxide gas into the cathode chamber. ### Claim 3 (depends on 1) The method of claim 1, wherein the electrolytic voltage is applied in a range from about 2 volts to about 5 volts. ### Claim 4 (depends on 1) The method of claim 1, wherein the carbon dioxide gas is decomposed to form at least one of formic acid and formate salts. ### Claim 5 (depends on 1) The method of claim 1 further comprising collecting and feeding the cathode electrolyte which is unreacted back to the cathode chamber for a cycling use. ### Claim 6 (depends on 1) The method of claim 1 further comprising collecting and feeding the anode electrolyte which is unreacted back to the anode chamber. ### Claim 7 (depends on 1) The method of claim 1 further comprising supplying water produced in the fuel cell to at least one of the cathode electrolyte and the anode electrolyte. ### Claim 8 (depends on 1) The method of claim 1, wherein a temperature in the cathode chamber is in a range from about 20 degrees to about 90 degrees. ### Claim 9 (depends on 1) The method of claim 1, wherein a pH value of the cathode electrolyte is greater than 7. ### Claim 10 (depends on 1) The method of claim 1, further comprising depositing the plurality of cathode catalyst particles on inner walls of the plurality of holes.