# US 9,518,331 B2 · Hydrogen system and method of operation > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 9,518,331 B2 - Document ID: US9518331B2 - Status: Granted - Kind: B2 - Application number: 14/321,123 - Filed: 2014-07-01 - Published: 2015-01-01 - Granted: 2016-12-13 - Earliest claimed: 2013-07-01 - Assignees: Sustainable Innovations, LLC - Applicants: Sustainable Innovations, LLC - Inventors: Joshua S. Preston; Trent M. Molter; Mark E. Dristy; Vyas Krishnamurthy; Gregory Hesler - Web page: https://patentgrep.com/patent/US9518331B2 ## CPC - C25B 15/02: Process control or regulation - B01D 53/326: {in electrochemical cells} - C25B 1/04: by electrolysis of water - C25B 9/05: Pressure cells - C25B 9/73: of the filter-press type - C25B 15/023: Measuring, analysing or testing during electrolytic production - Y02E 60/36: Hydrogen production from non-carbon containing sources, e.g. by water electrolysis - 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) - B01D: SEPARATION (separating solids from solids by wet methods B03B, B03D; by pneumatic jigs or tables B03B; by other dry methods B07; magnetic or electrostatic separation of solid materials from solid materials or fluids, separation by high-voltage electric fields B03C; centrifuges, vortex apparatus B04; presses per se for squeezing-out liquid from liquid-containing material B30B9/02; treatment of water C02F, e.g. softening by ion-exchange C02F1/42; {arrangements of air intake cleaners in gas turbine plants F02C7/05} ; arrangements or mounting of filters in air-conditioning, air-humidification or ventilation F24F13/28) - Y02E: REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION ## Abstract A system is disclosed for providing hydrogen that includes a first PEM electrochemical cell or stack including a membrane electrode assembly that includes an inlet for a first gas that comprises hydrogen in fluid communication with the anode side of the first electrochemical cell or cell stack, and an outlet in fluid communication with the cathode side of the first electrochemical cell or stack. A second electrochemical cell or cell stack includes a water inlet in fluid communication with the anode side of the second electrochemical cell or cell stack, and an outlet in fluid communication with the cathode side of the second electrochemical cell or cell stack. A controller is configured to operate the first electrochemical cell or cell stack as a primary hydrogen source and to controllably operate the second electrochemical cell or cell stack as a secondary hydrogen source. ## Claims ### Claim 1 A system for providing hydrogen, comprising: a first electrochemical cell or cell stack comprising a first membrane electrode assembly comprising a cathode and an anode separated by a proton exchange membrane, an inlet in controllable fluid communication with a variably-available source of a first gas that comprises hydrogen in fluid communication with the anode side of the first electrochemical cell or cell stack, and an outlet in fluid communication with the cathode side of the first membrane electrode assembly; a second electrochemical cell or cell stack comprising a second membrane electrode assembly comprising a cathode and an anode separated by a proton exchange membrane, a water inlet in fluid communication with the second membrane electrode assembly, and an outlet in fluid communication with the cathode side of the second membrane electrode assembly; and a controller in communication with the first and second electrochemical cells or cell stacks, configured to receive a hydrogen demand signal and: (i) when the hydrogen demand signal is greater than zero and the first gas is not available at the first electrochemical cell or cell stack inlet, to operate the second electrochemical cell or cell stack, and (ii) when the hydrogen demand signal is greater than zero and the first gas is available at the first electrochemical cell or cell stack inlet, to operate the first electrochemical cell or cell stack as a primary hydrogen source and to controllably operate the second electrochemical cell or cell stack as a secondary hydrogen source in response to the hydrogen demand signal and/or the hydrogen output of the first electrochemical cell or cell stack. ### Claim 2 (depends on 1) The system of claim 1, wherein the controller is configured to operate the first electrochemical cell or cell stack at a predetermined current when the first gas is available, and to selectively toggle the second electrochemical cell or cell stack between an off state and an on state in response to the hydrogen demand signal and/or the hydrogen output of the first electrochemical cell or cell stack. ### Claim 3 (depends on 1) The system of claim 1, wherein the controller is configured to operate the first electrochemical cell or cell stack at a predetermined current when the first gas is available, and to operate the second electrochemical cell or cell stack at a variable current in response to the hydrogen demand signal and/or the hydrogen output of the first electrochemical cell or cell stack. ### Claim 4 (depends on 1) The system of claim 1, wherein the water inlet of the second electrochemical cell or cell stack is in fluid communication with the anode side of the second membrane electrode assembly, and further comprising a first volume of liquid water in fluid communication with the water inlet of the second electrochemical cell or cell stack and in fluid communication with the anode side of the first electrochemical cell or stack. ### Claim 5 (depends on 4) The system of claim 4, further comprising a second volume of liquid water in fluid communication with the cathode side of the first electrochemical cell or stack and the cathode side of the second electrochemical cell or stack. ### Claim 6 (depends on 1) The system of claim 1, wherein the first and second electrochemical cells or cell stacks are configured to produce hydrogen at a pressure of from greater than 0 psi to 12,000 psi. ### Claim 7 (depends on 1) The system of claim 1, further comprising a compressor having an inlet in fluid communication with the outlets of the first and second electrochemical cells or cell stacks. ### Claim 8 (depends on 1) The system of claim 1, wherein the hydrogen output of the first electrochemical cell or cell stack is represented by gas pressure from the outlet of the first electrochemical cell or cell stack, and the second electrochemical cell or cell stack is controllably operated in response to said gas pressure. ### Claim 9 (depends on 8) The system of claim 8, further comprising a pressure switch or sensor in a hydrogen stream downstream of the first and second electrochemical cell or cell stack outlets and a pressure regulator downstream of the pressure switch or sensor. ### Claim 10 (depends on 1) The system of claim 1, further comprising one or more additional first electrochemical cells or cell stacks having an inlet in controllable fluid communication with a variably-available source of the first gas in fluid communication with an anode side of said one or more additional first electrochemical cells or cell stacks, and an outlet in fluid communication with a cathode side of said one or more first additional electrochemical cells or cell stacks. ### Claim 11 (depends on 1) The system of claim 1, further comprising one or more additional second electrochemical cells or cell stacks having a water inlet in fluid communication with said one or more additional second electrochemical cells or cell stacks, and an outlet in fluid communication with a cathode side of said one or more second additional electrochemical cells or cell stacks. ### Claim 12 (depends on 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, 11) The system of any of claims 1-11, wherein the first gas further comprises at least one gas component other than hydrogen. ### Claim 13 A method of providing hydrogen, comprising receiving a hydrogen demand signal; when the hydrogen demand signal is greater than zero and a first gas comprising hydrogen is available, operating a first electrochemical cell or cell stack comprising a first membrane electrode assembly comprising a cathode and an anode separated by a proton exchange membrane, and an inlet for the first gas in fluid communication with the anode side of the first electrochemical cell or cell stack, to provide hydrogen at an outlet in fluid communication with the cathode side of the first membrane electrode assembly, and controllably operating a second electrochemical cell or cell stack comprising a second membrane electrode assembly comprising a cathode and an anode separated by a proton exchange membrane, and a water inlet in fluid communication with the second membrane electrode assembly, in response to the hydrogen demand signal and/or the hydrogen output of the first electrochemical cell or cell stack to provide hydrogen at an outlet in fluid communication with the cathode side of the second membrane electrode assembly; and when the hydrogen demand signal is greater than zero and the first gas is not available at the first electrochemical cell or cell stack inlet, operating the second electrochemical cell or cell stack to provide hydrogen at the outlet in fluid communication with the cathode side of the second membrane electrode assembly. ### Claim 14 (depends on 13) The method of claim 13, wherein the controller operates the first electrochemical cell or cell stack at a predetermined current when the first gas is available, and to selectively toggle the second electrochemical cell or cell stack between an off state and an on state in response to the hydrogen demand signal and/or the hydrogen output of the first electrochemical cell or cell stack. ### Claim 15 (depends on 13) The method of claim 13, wherein the controller operates the first electrochemical cell or cell stack at a predetermined current when the first gas is available, and to operate the second electrochemical cell or cell stack at a variable current in response to the hydrogen demand signal and/or the hydrogen output of the first electrochemical cell or cell stack. ### Claim 16 (depends on 13) The method of claim 13, wherein the water inlet of the second electrochemical cell or cell stack is in fluid communication with the anode side of the second membrane electrode assembly, and a first volume of liquid water is in fluid communication with the water inlet of the second electrochemical cell or cell stack and in fluid communication with the anode side of the first electrochemical cell or cell stack proton exchange membrane. ### Claim 17 (depends on 16) The method of claim 16, wherein a second volume of liquid water is in fluid communication with the cathode side of the first electrochemical cell or cell stack proton exchange membrane and the cathode side of the second electrochemical cell or cell stack proton exchange membrane. ### Claim 18 (depends on 13) The method of claim 13, wherein the first and second electrochemical cells or cell stacks are operated to produce hydrogen at a pressure of from greater than 0 psi to 12,000 psi. ### Claim 19 (depends on 13) The method of claim 13, further comprising compressing hydrogen from the outlets of the first and second electrochemical cells or cell stacks. ### Claim 20 (depends on 13) The method of claim 13, further comprising determining the hydrogen output of the first electrochemical cell or cell stack from gas pressure from the outlet of the first electrochemical cell or cell stack, and wherein the second electrochemical cell or cell stack is controllably operated in response to said gas pressure. ### Claim 21 (depends on 13) The method of claim 13, further comprising operating one or more additional first electrochemical cells or cell stacks having an inlet for the first gas in fluid communication with an anode side of said one or more additional first electrochemical cells or cell stacks, and an outlet in fluid communication with a cathode side of said one or more first additional electrochemical cells or cell stacks. ### Claim 22 (depends on 13) The method of claim 13, further comprising operating one or more additional second electrochemical cells or cell stacks having a water inlet in fluid communication with said one or more additional second electrochemical cells or cell stacks, and an outlet in fluid communication with a cathode side of said one or more second additional electrochemical cells or cell stacks. ### Claim 23 A system for providing hydrogen, comprising: a first electrochemical cell or cell stack comprising a first membrane electrode assembly comprising a cathode and an anode separated by a proton exchange membrane, an inlet in controllable fluid communication with a variably-available source of a first gas that comprises hydrogen in fluid communication with the anode side of the first electrochemical cell or cell stack, and an outlet in fluid communication with the cathode side of the first membrane electrode assembly; a second electrochemical cell or cell stack comprising a second membrane electrode assembly comprising a cathode and an anode separated by a proton exchange membrane, a water inlet in fluid communication with the anode side of the second membrane electrode assembly, and an outlet in fluid communication with the cathode side of the second membrane electrode assembly; and a first volume of liquid water in fluid communication with the water inlet of the second electrochemical cell or cell stack and in fluid communication with the anode side of the first electrochemical cell or cell stack proton exchange membrane, or a second volume of liquid water in fluid communication with the cathode side of the first membrane electrode assembly and the cathode side of the second electrochemical membrane electrode assembly. ### Claim 24 (depends on 23) The system of claim 23, comprising said first volume of liquid water. ### Claim 25 (depends on 23) The system of claim 23, comprising said second volume of liquid water. ### Claim 26 (depends on 23) The system of claim 23, comprising said first volume of liquid water and said second volume of liquid water.