Voltage reduction of membrane cell for the electrolysis of brine

Claim 2

In the electrolysis of brine in a membrane cell, the improvement which comprises lowering the voltage drop across the cell by dissolving deposits upon the membrane by increasing the acidity of the anolyte, diluting the electrolyte located immediately adjacent to said anolyte and separated from said anolyte by a membrane, reducing the current density, and maintaining such conditions during electrolysis for a period sufficiently long to rejuvenate said membrane.

Claim 3

A method according to claim 1 wherein the acid employed is hydrochloric acid, the anolyte pH is adjusted with the acid to a pH in the range of about 0.5 to 2.5 from a higher pH, the caustic concentration in the compartment immediately adjacent to the anolyte compartment is reduced to about 20 to 45 grams per liter, the current density is reduced to about 0.01 to 0.1 ampere per square centimeter, such conditions are maintained for a period of 1/2 to 10 hours and the membrane is a cation-active permselective membrane of a polymeric material selected from the group consisting of a hydrolyzed copolymer of a perfluorinated hydrocarbon and a fluorosulfonated perfluorovinyl ether, and a sulfostyrenated perfluorinated ethylene propylene polymer.

Claim 4

A process according to claim 2 wherein the cell is a three compartment cell, the membrane is a hydrolyzed copolymer of tetrafluoroethylene and a fluorosulfonated fluorovinyl ether of the formula FSO 2 CF 2 CF 2 OCF(CF 3 )CF 2 OCF=CF 2 , which copolymer has an equivalent weight of about 900 to 1,600, the anolyte is acidified with hydrochloric acid to a pH of 1 to 2, the buffer compartment electrolyte sodium hydroxide concentration is lowered to 20 to 35 grams per liter and the current density is decreased to 0.01 to 0.05 ampere/sq. cm. for 1/2 to 1 hour, after which electrolysis is resumed at an anolyte pH of about 4, a buffer compartment caustic concentration of about 50 to 100 grams per liter, a current density of about 0.3 ampere/sq. cm. and a voltage of 3.5 to 4.5, which voltage is 0.2 to about 0.5 volt lower than that required to maintain said current density before the rejuvenation treatment.

Claim 5

A process according to claim 2 wherein the cell is a two compartment cell, the membrane is a hydrolyzed copolymer of tetrafluoroethylene and a fluorosulfonated fluorovinyl ether of the formula FSO 2 CF 2 CF 2 OCF(CF 3 )CF 2 OCF=CF 2 , which copolymer has an equivalent weight of about 900 to 1,600, the anolyte is acidified with hydrochloric acid to a pH of 1 to 2, the catholyte sodium hydroxide concentration is lowered to 20 to 45 grams per liter and the current density is decreased to 0.01 to 0.05 ampere/sq. cm. for 1/2 to 1 hour, after which the electrolysis is resumed at an anolyte pH of about 4, a catholyte compartment caustic concentration of 130 to 200 g./l., a current density of about 0.3 ampere/sq. cm. and a voltage of 3.5 to 4.5, which voltage is 0.2 to about 0.5 volt lower than that required to maintain such current density before the rejuvenation treatment.

Claim 6

A process according to claim 3 wherein the lowering of the buffer compartment pH is effected by a combination of water dilution and decrease in current density.

Claim 7

A process according to claim 4 wherein the lowering of the pH of the catholyte compartment is effected by a combination of water dilution and decrease in current density.

Claim 8

A method according to claim 1 wherein a brine is fed to the anolyte compartment which contains from 3 to 30 p.p.m. of calcium and/or magnesium sludge as the oxide(s).

Claim 9

A method according to claim 3 wherein a brine is fed to the anolyte compartment which contains from 3 to 30 p.p.m. calcium and/or magnesium sludge as the oxide(s).

Claim 10

A method according to claim 4 wherein a brine is fed to the anolyte compartment which contains from 3 to 30 p.p.m. of calcium and/or magnesium sludge as the oxide(s).