Method of producing cation-exchange membrane having roughed surface

Claim 3

The method of producing a cation-exchange membrane having roughed surface recited in claim 1, wherein the thickness of the silica powder layer formed on the carrier is 5μ to 250μ.

Claim 4

The method of producing a cation-exchange membrane having roughed surface recited in claim 1, wherein the silica powder layer was adhered with heating and pressing on the surface of the membrane under a condition of a temperature of 100°-200° C. and of a pressure of 5-100 kg/cm 2 .

Claim 5

The method of producing a cation-exchange membrane having roughed surface recited in claim 1, wherein the silica powder layer formed on the surface of the membrane is removed by dissolution with caustic soda aqueous solution of a concentration of 1-30 weight% at a temperature of 20°-90° C.

Claim 8

The method of producing a cation-exchange membrane having roughed surface recited in claim 5, wherein, after the boiling treatment of the roughed surface, it is further subjected to washing and drying.

Claim 11

The method of producing a cation-exchange membrane having roughed surface recited in claim 7, wherein, after heating in the mixed solution of caustic alkali aqueous solution and lower alcohol of C 1 -C 3 , washing and drying are applied thereto.

Claim 12

A cation-exchange membrane having a roughed surface and high strength said membrane being capable of reducing electrolysis voltage and maintaining current efficiency when used as a membrane in an electrolysis cell, which is obtainable by a process comprising the step of mixing silica powder having an average particle diameter of 0.01-20μ, with water to give a suspended or pasty mixture, step of supporting the resultant mixture on art paper or filter paper, step of drying the mixture to form silica powder layer, step of adhering with heating and pressing said silca powder layer on surface of membrane composed of perfluorocarbon polymer having cation-exchange group and/or group convertible into the cation-exchange group, and step of removing the silica powder layer formed on the surface of said membrane with caustic alkali aqueous solution.

Claim 13

A cation-exchange membrane having a roughed surface and high strength said membrane being capable of reducing electrolysis voltage and maintaining current efficiency when used as a membrane in an electrolysis cell, which is obtainable by a process comprising the step of mixing silica powder having an average particle diameter of 0.01-20μ, with water to give a suspended or pasty mixture, step of supporting the resultant mixture on art paper or filter paper, step of drying the mixture to form silica powder layer, step of adhering with heating and pressing said silca powder layer on surface of membrane composed of perfluorocarbon polymer having cation-exchange group and/or group convertible into the cation-exchange group, and step of removing the silica powder layer formed on the surface of said membrane with caustic alkali aqueous solution.

Claim 14

A cation-exchange membrane having a roughed surface and high strength said membrane being capable of reducing electrolysis voltage and maintaining current efficiency when used as a membrane in an electrolysis cell, which is obtainable by a process comprising the step of mixing silica powder having an average particle diameter of 0.01-20μ, with water to give a suspended or pasty mixture, step of supporting the resultant mixture on art paper or filter paper, step of drying the mixture to form silica powder, step of adhering the silica powder with heating and pressing on surface of a cation-exchange membrane having cation-exchange group and/or group convertible into the cation-exchange group, step of thereafter dissolving out thus silica powder formed on the surface of membrane with caustic alkali aqueous solution and step of treating the obtained roughed surface of the cation-exchange membrane with boiling aqueous solution of 1-10 weight% caustic soda.

Claim 15

A cation-exchange membrane having a roughed surface and high strength said membrane being capable of reducing electrolysis voltage and maintaining current efficiency when used as a membrane in an electrolysis cell, which is obtainable by a process comprising the step of mixing silica powder having an average particle diameter of 0.01-20μ, with water to give a suspended or pasty mixture, step of supporting the resultant mixture on art paper or filter paper, step of drying the mixture to form silica powder, step of adhering the silica powder with heating and pressing on surface of a cation-exchange membrane having cation-exchange group and/or group convertible into the cation-exchange group, step of thereafter dissolving out thus silica powder formed on the surface of membrane with caustic alkali aqueous solution and step of treating the obtained roughed surface of the cation-exchange membrane with boiling aqueous solution of 1-10 weight% caustic soda.

Claim 16

The cation-exchange membrane having roughed surface recited in claim 10, wherein step of washing and drying is followed after the step of the boiling treatment of the roughed surface.

Claim 17

A cation-exchange membrane having a roughed surface and high strength said membrane being capable of reducing electrolysis voltage and maintaining current efficiency when used as a membrane in an electrolysis cell, which is obtainable by a process comprising the step of mixing silica powder having an average particle diameter of 0.01-20μ, with water to give a suspended or pasty mixture, step of supporting the resultant mixture on art paper or filter paper, step of drying the mixture to form silica powder layer, step of adhering with heating and pressing on surface of membrane composed of perfluorocarbon polymer having cation-exchange group and/or group convertible into the cation-exchange group, step of removing with dissolving the silica powder layer formed on the surface of said membrane with caustic alkali aqueous solution, and step of heating the cation-exchange membrane having thus obtained roughed surface in a mixed solution of caustic alkali aqueous solution and lower alcohol of C 1 -C 3 at a temperature from 40° C. to the boiling point of the lower alcohol of C 1 -C 3 .

Claim 18

A cation-exchange membrane having a roughed surface and high strength said membrane being capable of reducing electrolysis voltage and maintaining current efficiency when used as a membrane in an electrolysis cell, which is obtainable by a process comprising the step of mixing silica powder having an average particle diameter of 0.01-20μ, with water to give a suspended or pasty mixture, step of supporting the resultant mixture on art paper or filter paper, step of drying the mixture to form silica powder layer, step of adhering with heating and pressing on surface of membrane composed of perfluorocarbon polymer having cation-exchange group and/or group convertible into the cation-exchange group, step of removing with dissolving the silica powder layer formed on the surface of said membrane with caustic alkali aqueous solution, and step of heating the cation-exchange membrane having thus obtained roughed surface in a mixed solution of caustic alkali aqueous solution and lower alcohol of C 1 -C 3 at a temperature from 40° C. to the boiling point of the lower alcohol of C 1 -C 3 .

Claim 19

The cation-exchange membrane having roughed surface recited in claim 12, wherein step of washing and drying is applied after the step of heating in the mixed solution of caustic alkali aqueous solution and lower alcohol of C 1 -C 3 .