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Ion exchange membrane, method for producing ion exchange membrane, and electrolytic cell

An ion exchange membrane and manufacturing method technology, applied in the electrolysis process, electrolysis components, diaphragms, etc., can solve the problems of increasing electrolysis voltage, decreasing current efficiency, increasing alkali impurity concentration, etc., and achieve the effect of stable electrolysis performance and small impact.

Pending Publication Date: 2020-12-18
ASAHI KASEI KK
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0006] In addition, if there are impurities such as metals in the aqueous alkali metal chloride solution, and these impurities accumulate inside the cation exchange membrane, it will cause an increase in electrolysis voltage, a decrease in current efficiency, and an increase in the concentration of impurities in the alkali.

Method used

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  • Ion exchange membrane, method for producing ion exchange membrane, and electrolytic cell
  • Ion exchange membrane, method for producing ion exchange membrane, and electrolytic cell
  • Ion exchange membrane, method for producing ion exchange membrane, and electrolytic cell

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0187] As the reinforcing thread, a polytetrafluoroethylene (PTFE) 100-denier flat yarn twisted 900 times / m (hereinafter referred to as PTFE thread) was used. As the sacrificial yarn for the warp, a yarn obtained by twisting 35 denier, 8-filament polyethylene terephthalate (PET) at 200 twists / m (hereinafter referred to as PET yarn) was used. In addition, as the sacrificial yarn of the weft, a yarn obtained by twisting 35 denier, 8-filament polyethylene terephthalate (PET) at 200 times / m (called PET yarn in the fiber) was used. . First, plain weaving was performed with 24 PTFE threads / inch and two sacrificial threads arranged between adjacent PTFE threads to obtain a woven fabric with a thickness of 100 μm.

[0188] Next, prepare as a CF 2 = CF 2 with CF 2 = CFOCF 2 CF(CF 3 )OCF 2 CF 2 COOCH 3 The ion exchange capacity of the copolymer is 0.85 mg equivalent / g of polymer (A1) of dry resin, as CF 2 = CF 2 with CF 2 = CFOCF 2 CF(CF 3 )OCF 2 CF 2 SO 2The ion exchan...

Embodiment 2

[0196] In Example 1, except reducing the usage-amount of HS-210 and changing viscosity to 12.0 mPa*s, it carried out similarly to Example 1, and produced the ion exchange membrane. In this ion exchange membrane, the content of the fluorine-containing polymer in the binder was 100% by mass.

[0197] The distribution density was measured in the same manner as in Example 1, and the result was that every 1 cm 2 0.5mg in. In addition, when the coverage rate was measured in the same manner as in Example 1, it was 56.5%.

[0198] [Electrolysis Evaluation]

[0199] Using this ion-exchange membrane, the electrolytic performance was evaluated under the same conditions as in Example 1. As a result, the voltage showed a low value of 3.08V, and the measurement of impurity tolerance was performed. As a result, the decrease in current efficiency was as small as 0.74% / day, showing High impurity durability.

Embodiment 3

[0201] In Example 1, an ion exchange membrane was produced in the same manner as in Example 1 except that the usage-amount of HS-210 was increased and the viscosity was changed to 8.5 mPa·s. In this ion exchange membrane, the content of the fluorine-containing polymer in the binder was 100% by mass.

[0202] The distribution density was measured in the same manner as in Example 1, and the result was that every 1 cm 2 0.5mg in. In addition, when the coverage rate was measured in the same manner as in Example 1, it was 92.9%.

[0203] [Electrolysis Evaluation]

[0204] Using this ion exchange membrane, the electrolytic performance was evaluated under the same conditions as in Example 1. As a result, the voltage showed a low value of 3.06V, and the measurement of impurity tolerance was performed. As a result, the decrease in current efficiency was as small as 0.42% / day, showing High impurity durability.

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Abstract

The present invention provides an ion exchange membrane, a method for producing the ion exchange membrane, and an electrolytic cell. The ion exchange membrane is capable of reducing electrolysis voltage when being supplied to electrolysis, and is capable of stably exhibiting electrolysis performance with little influence of impurities in an electrolyte on electrolysis performance. This ion exchange membrane is provided with: a membrane main body that contains a fluorine-containing polymer having an ion exchange group, and a coating layer that is disposed on at least one surface of the membranemain body. The coating layer contains inorganic particles and a binder, and the inorganic particles and the binder are contained in the coating layer with respect to the total mass of the inorganic particles and the binder, wherein the mass ratio of the binder is 0.3-0.9, and the coating ratio of the coating layer on the membrane main body is 50% or more.

Description

technical field [0001] The invention relates to an ion exchange membrane, a manufacturing method of the ion exchange membrane and an electrolytic cell. Background technique [0002] Fluorine-containing ion exchange membranes are excellent in heat resistance and chemical resistance, and are widely used as separators for electrolysis for alkali metal chloride electrolysis, ozone generation electrolysis, fuel cells, water electrolysis, and hydrochloric acid electrolysis. use and are being extended to new uses. [0003] Among these, in the electrolysis of alkali metal chlorides for producing chlorine and alkali metal hydroxides, the ion-exchange membrane method has become the mainstream in recent years. In addition, in order to reduce the unit of power consumption, in the alkali metal chloride electrolysis using the ion exchange membrane method, a natural circulation zero-gap electrolytic cell in which the ion exchange membrane is closely bonded to the anode and cathode has bec...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C25B13/08C25B13/02C25B1/46B05D7/24C25B9/23
CPCC25B13/08C25B13/02C25B1/46B05D7/24C25B9/23
Inventor 小泷雄太贝原慎一冈本浩司五十岚雄太
Owner ASAHI KASEI KK