Assembly of a porous metal diffusion substrate and a polymeric separator membrane
US-2015064606-A1 · Mar 5, 2015 · US
US2018073155A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2018073155-A1 |
| Application number | US-201615558861-A |
| Country | US |
| Kind code | A1 |
| Filing date | Mar 18, 2016 |
| Priority date | Mar 18, 2015 |
| Publication date | Mar 15, 2018 |
| Grant date | — |
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The diaphragm for alkaline water electrolysis according to the present invention comprises a porous polymer membrane, the porous polymer membrane comprising a polymer resin and hydrophilic inorganic particles. A porosity of the porous polymer membrane is 30% or more and 60% or less, average pore sizes at both surfaces of the porous polymer membrane is 0.5 μm or more and 2.0 μm or less, and a ratio of a mode particle size of the hydrophilic inorganic particles to the average pore size of the porous polymer membrane (mode particle size/average pore size) is 2.0 or more.
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1 . A diaphragm for alkaline water electrolysis, comprising a porous polymer membrane, the porous polymer membrane comprising a polymer resin and hydrophilic inorganic particles, wherein a porosity of the porous polymer membrane is 30% or more and 60% or less, average pore sizes at both surfaces of the porous polymer membrane are 0.5 μm or more and 2.0 μm or less, and a ratio of a mode particle size of the hydrophilic inorganic particles to the average pore size of the porous polymer membrane (mode particle size/average pore size) is 2.0 or more. 2 . A diaphragm for alkaline water electrolysis, comprising a porous polymer membrane, the porous polymer membrane comprising a polymer resin and hydrophilic inorganic particles, wherein a porosity of the porous polymer membrane is 30% or more and 60% or less, and bubble points of the porous polymer membrane before and after a cavitation test employing ultrasonic cleaning at a frequency of 40 kHz and a sound pressure of 190 db for 60 minutes as measured at 90° C. are 100 kPa or more. 3 . The diaphragm for alkaline water electrolysis according to claim 2 , wherein average pore sizes at both surfaces of the porous polymer membrane are 0.5 μm or more and 2.0 μm or less, and a ratio of a mode particle size of the hydrophilic inorganic particles to the average pore size of the porous polymer membrane (mode particle size/average pore size) is 2.0 or more. 4 . The diaphragm for alkaline water electrolysis according to claim 2 or 3 , wherein abundances of the hydrophilic inorganic particles as calculated by particle analysis are 10% or more at both surfaces of the porous polymer membrane before and after the cavitation test. 5 . The diaphragm for alkaline water electrolysis according to claim 2 or 3 , wherein abundances of the hydrophilic inorganic particles as calculated by particle analysis are 10% or more at a cross-section of the porous polymer membrane before and after the cavitation test. 6 . The diaphragm for alkaline water electrolysis according to claim 4 , wherein a ratio of decrease, caused by the cavitation test, in the abundances of the hydrophilic inorganic particles at both surfaces or a cross-section of the porous polymer membrane is less than 0.20. 7 . The diaphragm for alkaline water electrolysis according to claim 1 or 2 , wherein the polymer resin comprises at least one selected from the group consisting of polysulfone, polyethersulfone, and polyphenylsulfone. 8 . The diaphragm for alkaline water electrolysis according to claim 1 or 2 , wherein a thickness of the porous polymer membrane is 300 μm or more and 600 μm or less. 9 . The diaphragm for alkaline water electrolysis according to claim 1 or 2 , wherein the hydrophilic inorganic particles comprise zirconium oxide. 10 . The diaphragm for alkaline water electrolysis according to claim 1 or 2 , further comprising a porous support. 11 . The diaphragm for alkaline water electrolysis according to claim 10 , wherein the porous support is any one selected from the group consisting of a mesh, a non-woven fabric, a woven fabric, and a composite fabric comprising a non-woven fabric and a woven fabric enclosed in the non-woven fabric. 12 . The diaphragm for alkaline water electrolysis according to claim 11 , wherein the porous support comprises polyphenylene sulfide. 13 . An alkaline water electrolysis device comprising: an anode; a cathode; and the diaphragm for alkaline water electrolysis according to claim 1 or 2 , the diaphragm being placed between the anode and the cathode. 14 . A method for producing hydrogen, comprising the step of electrolyzing alkaline water by applying a voltage to the alkaline water electrolysis device according to claim 13 using a variable power supply. 15 . A method for producing the diaphragm for alkaline water electrolysis according to claim 1 or 2 , comprising the steps of: (A) preparing a solution containing the polymer resin, a solvent capable of dissolving the polymer resin, and the hydrophilic inorganic particles; (B) applying the solution to a substrate to form a coating on the substrate; (C) exposing a surface of the coating, said surface being located opposite from the substrate, to a gas containing vapor of a poor solvent for the polymer resin; and (D) immersing the coating on the substrate in a coagulation bath containing a poor solvent for the polymer resin to form a porous polymer membrane. 16 . The method for producing the diaphragm for alkaline water electrolysis according to claim 15 , wherein the poor solvent in the coagulation bath further comprises the solvent. 17 . The method for producing the diaphragm for alkaline water electrolysis according to claim 16 , wherein a concentration of the solvent in the coagulation bath is from 30 to 70 mass %. 18 . The method for producing the diaphragm for alkaline water electrolysis according to claim 17 , wherein the solvent comprises N-methyl-2-pyrrolidone. 19 . A method for producing the diaphragm for alkaline water electrolysis according to claim 1 or 2 , comprising the steps of: (E) mixing the polymer resin, a solvent capable of dissolving the polymer resin, and the hydrophilic inorganic particles to obtain a homogeneous dispersion, at a temperature higher than a phase separation temperature of the dispersion to be obtained; (F) extruding the dispersion at a temperature higher than the phase separation temperature of the dispersion to obtain an extrudate; (G) cooling the extrudate obtained in the step (F) to a temperature equal to or lower than the phase separation temperature of the dispersion to coagulate the extrudate; and (H) extracting the solvent from the extrudate obtained in the step (G) to obtain a porous polymer membrane. 20 . The method for producing the diaphragm for alkaline water electrolysis according to claim 19 , further comprising a stretching step. 21 . A method for producing the diaphragm for alkaline water electrolysis according to claim 1 or 2 , comprising the steps of: (I) paste-extruding a mixture containing a polymer resin and hydrophilic inorganic particles; (J) rolling the extruded paste to obtain a sheet-shaped porous membrane; and (K) stretching the obtained sheet-shaped porous membrane in a longitudinal direction and/or a transverse direction.
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