# US 6,720,106 B2 · Membrane electrode assembly for fuel and process for producing the same > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 6,720,106 B2 - Document ID: US6720106B2 - Status: Granted - Kind: B2 - Application number: 09/942,123 - Filed: 2001-08-30 - Published: 2002-05-09 - Granted: 2004-04-13 - Earliest claimed: 2000-09-01 - Assignees: Honda Giken Kogyo Kabushiki Kaisha - Inventors: Kaoru Fukuda; Masaaki Nanaumi; Nobuhiro Saito; Yoichi Asano; Nagayuki Kanaoka - Web page: https://patentgrep.com/patent/US6720106B2 ## CPC - H01M 4/8605: {Porous electrodes} - H01M 4/881: {Electrolytic membranes} - H01M 4/8828: {Coating with slurry or ink} - H01M 4/8882: {Heat treatment, e.g. drying, baking} - H01M 4/8896: {Pressing, rolling, calendering (membrane electrode assemblies H01M8/1004)} - H01M 8/1004: characterised by membrane-electrode assemblies [MEA] (H01M8/12 takes precedence) - Y02E 60/50: Fuel cells - Y10T 29/4911: including sealing - Y10T 29/49115: including coating or impregnating - Y10T 29/53135: Storage cell or battery - Y10T 29/53204: Electrode - 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 - Y10T: TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION ## Abstract An membrane electrode assembly for a fuel cell composed of a pair of electrode catalyst layers and an electrolyte membrane sandwiched between the electrode catalyst layers is configured so that the catalyst of at least one surface of the electrode catalyst layers enters in the electrolyte membrane whereby the electrode catalyst layer and the electrolyte membrane are unified with each other. In this configuration, no exfoliation occurs at the interface between the electrode catalyst layer and the electrolyte membrane, and the durability of the membrane electrode assembly can be increased even during the course of heat cycles. ## Claims ### Claim 1 An membrane electrode assembly for a fuel cell composed of a pair of electrode catalyst layers and an electrolyte membrane sandwiched between the electrode catalyst layers which is configured so that the catalyst of at least one surface of the electrode catalyst layers enters in the electrolyte membrane whereby the electrode catalyst layer and the electrolyte membrane are unified with each other. ### Claim 2 (depends on 1) The membrane electrode assembly for a fuel cell as claimed in claim 1, wherein an ion exchange density gradient coefficient calculated by the following equation (1): Coefficient=(A−B)/(C−D) (1) wherein A is an ion exchange capacity of the electrolyte membrane, B is an ion exchange capacity of the electrode catalyst layer, C is a thickness in μm of the electrolyte membrane before heating under a pressure, and D is a thickness in μm of the electrolyte membrane after heating under a pressure at a portion no catalyst enters therein, is not greater than 3.5×103 meq/g/cm. ### Claim 3 (depends on 2) The membrane electrode assembly for a fuel cell as claimed in claim 2, wherein the depth of the catalyst entering in the electrode is in the range of from 5 μm to 20 μm. ### Claim 4 (depends on 3) The membrane electrode assembly for a fuel cell as claimed in claim 3, which is produced by dissolving the catalyst in a polar solvent and then dispersing the catalyst in an ion conductive polymer solution to prepare a slurry, directly applying the slurry onto at least one surface of the electrolyte membrane, followed by heating under a pressure to form the electrode catalyst layer or layers and to allow at least parts of the catalysts for entering in said electrolyte membrane during the heating under a pressure whereby said electrode catalyst layer and said electrolyte membrane are unified with each other. ### Claim 5 (depends on 3) The membrane electrode assembly for a fuel cell as claimed in claim 3, which is produced by dispersing the catalyst in an organic solvent soluble in said electrolyte membrane to prepare a slurry of the catalyst dispersed in the organic solvent, directly applying the slurry onto at least one surface of the electrolyte membrane, followed by heating under a pressure to form the electrode catalyst layer or layers and to allow at least parts of the catalysts for entering in said electrolyte membrane during the heating under a pressure whereby said electrode catalyst layer and said electrolyte membrane are unified with each other. ### Claim 6 (depends on 3) The membrane electrode assembly for a fuel cell as claimed in claim 3, which is produced by dissolving the catalyst in a polar solvent and then dispersing the catalyst in an ion conductive polymer solution to prepare a slurry, directly applying the slurry onto at least one surface of a diffusion layers to be laminated on both sides of said membrane electrode assembly for a fuel cell, applying the applied surface of said slurry onto the surface of said electrolyte membrane, followed by heating under a pressure to form the electrode catalyst layer or layers and to allow at least parts of the catalysts for entering in said electrolyte membrane during the heating under a pressure whereby said electrode catalyst layer and said electrolyte membrane are unified with each other. ### Claim 7 (depends on 2) The membrane electrode assembly for a fuel cell as claimed in claim 2, which is produced by dissolving the catalyst in a polar solvent and then dispersing the catalyst in an ion conductive polymer solution to prepare a slurry, directly applying the slurry onto at least one surface of the electrolyte membrane, followed by heating under a pressure to form the electrode catalyst layer or layers and to allow at least parts of the catalysts for entering in said electrolyte membrane during the heating under a pressure whereby said electrode catalyst layer and said electrolyte membrane are unified with each other. ### Claim 8 (depends on 2) The membrane electrode assembly for a fuel cell as claimed in claim 2, which is produced by dispersing the catalyst in an organic solvent soluble in said electrolyte membrane to prepare a slurry of the catalyst dispersed in the organic solvent, directly applying the slurry onto at least one surface of the electrolyte membrane, followed by heating under a pressure to form the electrode catalyst layer or layers and to allow at least parts of the catalysts for entering in said electrolyte membrane during the heating under a pressure whereby said electrode catalyst layer and said electrolyte membrane are unified with each other. ### Claim 9 (depends on 2) The membrane electrode assembly for a fuel cell as claimed in claim 2, which is produced by dissolving the catalyst in a polar solvent and then dispersing the catalyst in an ion conductive polymer solution to prepare a slurry, directly applying the slurry onto at least one surface of a diffusion layers to be laminated on both sides of said membrane electrode assembly for a fuel cell, applying the applied surface of said slurry onto the surface of said electrolyte membrane, followed by heating under a pressure to form the electrode catalyst layer or layers and to allow at least parts of the catalysts for entering in said electrolyte membrane during the heating under a pressure whereby said electrode catalyst layer and said electrolyte membrane are unified with each other. ### Claim 10 (depends on 1) The membrane electrode assembly for a fuel cell as claimed in claim 1, wherein the depth of the catalyst entering in the electrode is in the range of from 5 μm to 20 μm. ### Claim 11 (depends on 10) The membrane electrode assembly for a fuel cell as claimed in claim 10, which is produced by dissolving the catalyst in a polar solvent and then dispersing the catalyst in an ion conductive polymer solution to prepare a slurry, directly applying the slurry onto at least one surface of the electrolyte membrane, followed by heating under a pressure to form the electrode catalyst layer or layers and to allow at least parts of the catalysts for entering in said electrolyte membrane during the heating under a pressure whereby said electrode catalyst layer and said electrolyte membrane are unified with each other. ### Claim 12 (depends on 10) The membrane electrode assembly for a fuel cell as claimed in claim 10, which is produced by dispersing the catalyst in an organic solvent soluble in said electrolyte membrane to prepare a slurry of the catalyst dispersed in the organic solvent, directly applying the slurry onto at least one surface of the electrolyte membrane, followed by heating under a pressure to form the electrode catalyst layer or layers and to allow at least parts of the catalysts for entering in said electrolyte membrane during the heating under a pressure whereby said electrode catalyst layer and said electrolyte membrane are unified with each other. ### Claim 13 (depends on 10) The membrane electrode assembly for a fuel cell as claimed in claim 10, which is produced by dissolving the catalyst in a polar solvent and then dispersing the catalyst in an ion conductive polymer solution to prepare a slurry, directly applying the slurry onto at least one surface of a diffusion layers to be laminated on both sides of said membrane electrode assembly for a fuel cell, applying the applied surface of said slurry onto the surface of said electrolyte membrane, followed by heating under a pressure to form the electrode catalyst layer or layers and to allow at least parts of the catalysts for entering in said electrolyte membrane during the heating under a pressure whereby said electrode catalyst layer and said electrolyte membrane are unified with each other. ### Claim 14 (depends on 1) The membrane electrode assembly for a fuel cell as claimed in claim 1, which is produced by dissolving the catalyst in a polar solvent and then dispersing the catalyst in an ion conductive polymer solution to prepare a slurry, directly applying the slurry onto at least one surface of the electrolyte membrane, followed by heating under a pressure to form the electrode catalyst layer or layers and to allow at least parts of the catalysts for entering in said electrolyte membrane during the heating under a pressure whereby said electrode catalyst layer and said electrolyte membrane are unified with each other. ### Claim 15 (depends on 1) The membrane electrode assembly for a fuel cell as claimed in claim 1, which is produced by dispersing the catalyst in an organic solvent soluble in said electrolyte membrane to prepare a slurry of the catalyst dispersed in the organic solvent, directly applying the slurry onto at least one surface of the electrolyte membrane, followed by heating under a pressure to form the electrode catalyst layer or layers and to allow at least parts of the catalysts for entering in said electrolyte membrane during the heating under a pressure whereby said electrode catalyst layer and said electrolyte membrane are unified with each other. ### Claim 16 (depends on 1) The membrane electrode assembly for a fuel cell as claimed in claim 1, which is produced by dissolving the catalyst in a polar solvent and then dispersing the catalyst in an ion conductive polymer solution to prepare a slurry, directly applying the slurry onto at least one surface of a diffusion layers to be laminated on both sides of said membrane electrode assembly for a fuel cell, applying the applied surface of said slurry onto the surface of said electrolyte membrane, followed by heating under a pressure to form the electrode catalyst layer or layers and to allow at least parts of the catalysts for entering in said electrolyte membrane during the heating under a pressure whereby said electrode catalyst layer and said electrolyte membrane are unified with each other. ### Claim 17 A process for an membrane electrode assembly for a fuel cell composed of a pair of electrode catalyst layers and an electrolyte membrane sandwiched between the electrode catalyst layers configured so that the catalyst of at least one surface of the electrode catalyst layers enters in the electrolyte membrane whereby the electrode catalyst layer and the electrolyte membrane are unified with each other, which comprises: dissolving the catalyst making up the electrode catalyst layer in a polar solvent and then dispersing the catalyst in an ion conductive polymer solution to prepare a slurry having a viscosity of from 5,000 to 25,000 mPa.s, directly applying the resulting slurry onto at least one surface of the electrolyte membrane, followed by heating under a pressure to form the electrode catalyst layer or layers, and heating the slurry under a pressure to allow at least parts of the catalysts for entering in said electrolyte membrane during the heating under a pressure whereby said electrode catalyst layer and said electrolyte membrane are unified with each other. ### Claim 18 (depends on 17) The process for an membrane electrode assembly for a fuel cell as claimed in claim 17, wherein the heating under a pressure is carried out in a state where the polar solvent remaining in the slurry directly applied onto the electrolyte membrane is in amount of from 20 mg/cm2 to 100 mg/cm2 to allow the catalysts for entering in said electrolyte membrane. ### Claim 19 A process for an membrane electrode assembly for a fuel cell composed of a pair of electrode catalyst layers and an electrolyte membrane sandwiched between the electrode catalyst layers configured so that the catalyst of at least one surface of the electrode catalyst layers enters in the electrolyte membrane whereby the electrode catalyst layer and the electrolyte membrane are unified with each other, which comprises: dispersing the catalyst making up the electrode catalyst layer in an organic solvent soluble in the electrolyte membrane to prepare a slurry of the catalyst dispersed in the organic solvent having a viscosity of from 5,000 to 25,000 mPa.s, directly applying the resulting slurry onto at least one surface of the electrolyte membrane, followed by heating under a pressure to form the electrode catalyst layer or layers, and heating the slurry under a pressure to allow at least parts of the catalysts for entering in said electrolyte membrane during the heating under a pressure whereby said electrode catalyst layer and said electrolyte membrane are unified with each other. ### Claim 20 (depends on 19) The process for an membrane electrode assembly for a fuel cell as claimed in claim 19, wherein the heating under a pressure is carried out in a state where the polar solvent remaining in the slurry directly applied onto the electrolyte membrane is in amount of from 20 mg/cm2 to 100 mg/cm2 to allow the catalysts for entering in said electrolyte membrane. ### Claim 21 A process for an membrane electrode assembly for a fuel cell composed of a pair of electrode catalyst layers and an electrolyte membrane sandwiched between the electrode catalyst layers is configured so that the catalyst of at least one surface of the electrode catalyst layers enters in the electrolyte membrane whereby the electrode catalyst layer and the electrolyte membrane are unified with each other, which comprises: dissolving the catalyst making up the electrode catalyst layer in a polar solvent and then dispersing the catalyst in an ion conductive polymer solution to prepare a slurry having a viscosity of from 5,000 to 25,000 mPa.s, directly applying the resulting slurry onto at least one surface the diffusion layer laminated on both sides of the membrane electrode assembly, applying the electrolyte membrane onto the applied surface of the slurry, followed by heating under a pressure to form the electrode catalyst layer or layers, and heating the slurry under a pressure to allow at least parts of the catalysts for entering in said electrolyte membrane during the heating under a pressure whereby said electrode catalyst layer and said electrolyte membrane are unified with each other. ### Claim 22 (depends on 21) The process for an membrane electrode assembly for a fuel cell as claimed in claim 21, wherein the heating under a pressure is carried out in a state where the polar solvent remaining in the slurry directly applied onto the electrolyte membrane is in amount of from 20 mg/cm2 to 100 mg/cm2 to allow the catalysts for entering in said electrolyte membrane.