Electrolytic cell
US-9476130-B2 · Oct 25, 2016 · US
US9404191B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9404191-B2 |
| Application number | US-201314439653-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 25, 2013 |
| Priority date | Oct 31, 2012 |
| Publication date | Aug 2, 2016 |
| Grant date | Aug 2, 2016 |
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It is an object of the present invention to provide an anode for a zero-gap brine electrolyzer which through employment of a highly roughened surface at a catalyst layer at an anode for a zero-gap brine electrolyzer makes it possible to achieve sufficient liquid permeability and further reduction in electrolyzing voltage and a brine electrolysis method employing same. The present invention relates to an anode for a zero-gap brine electrolyzer equipped with a liquid-permeable conductive substrate 21 , and with a catalyst layer 22 which is provided on the conductive substrate 21 and which is such that the maximum difference in height of surface irregularities is 55 μm to 70 μm; a zero-gap brine electrolyzer equipped with the anode 20 , a cathode 30 , and an ion-exchange membrane I disposed between and in contact with the anode 20 and the cathode 30 ; and a brine electrolysis method employing same.
Opening claim text (preview).
What is claimed is: 1. An anode for use in a zero-gap brine electrolyzer, comprising: a liquid-permeable conductive substrate; and a catalyst layer that is provided on the conductive substrate and has 55 to 70 μm of maximum difference in height of surface irregularities of the catalyst layer, wherein the catalyst layer has a thickness of 1 to 5 μm and an average surface roughness of 3 to 30 μm. 2. The anode according to claim 1 for use in a zero-gap brine electrolyzer, wherein the conductive substrate is an expanded or punched metal member comprising a valve metal or an alloy of two or more valve metals, and a total thickness of the conductive substrate and the catalyst layer is from 0.5 to 2.0 mm. 3. A zero-gap brine electrolyzer, comprising: an anode comprising a liquid-permeable conductive substrate and a catalyst layer that is provided on the conductive substrate and has 55 to 70 μm of maximum difference in height of surface irregularities of the catalyst layer; a cathode; and an ion-exchange membrane disposed between and in contact with the anode and the cathode, wherein the catalyst layer has a thickness of 1 to 5 m and an average surface roughness of 3 to 30 μm. 4. The zero-gap brine electrolyzer according to claim 3 , wherein the conductive substrate is an expanded or punched metal member comprising a valve metal or an alloy of two or more valve metals, and the total thickness of the conductive substrate and the catalyst layer is from 0.5 to 2.0 mm. 5. The zero-gap brine electrolyzer according to claim 3 , wherein the cathode comprises an expanded metal member of nickel with a rigid structure, a fine mesh-shaped cathode member with a flexible structure, and a conductive elastic material that has an elastic restoring force and is disposed between the expanded metal member and the fine mesh-shaped cathode member, and wherein the conductive elastic material is configured to press the fine mesh-shaped cathode member against the ion-exchange membrane. 6. The zero-gap brine electrolyzer according to claim 5 , wherein the conductive elastic material is in the form of a cushion mat or a spring. 7. A method for zero-gap brine electrolysis, the method comprising electrolyzing a sodium chloride-containing liquid with the zero-gap brine electrolyzer according to claim 3 .
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