Rejuvenation of the efficiency of sea water electrolysis cells by periodic removal of anodic deposits

Claim 1

A method of removing mineral deposits from electrodes, at least one of said electrodes is a dimensionally stable anode, in an electrolysis cell comprising operating the electrolysis cell at a current density of at least 0.2 amps per square inch until there is a reduction in cell efficiency, briefly reversing the cell polarity at reduced current densities of less than about 50 milliamps per square inch for a period of time sufficient to remove interfering mineral deposits and thereafter operating the electrolysis cell normally by reversing polarity and operating at current densities of at least about 0.2 amps per square inch.

Claim 2

A method of removing mineral deposits from electrodes, at least one of said electrodes is a dimensionally stable anode, in an electrolysis cell comprising operating the electrolysis cell at a current density of at least 0.2 amps per square inch until there is a reduction in cell efficiency, briefly reversing the cell polarity at reduced current densities of less than about 50 milliamps per square inch for a period of time sufficient to remove interfering mineral deposits and thereafter operating the electrolysis cell normally by reversing polarity and operating at current densities of at least about 0.2 amps per square inch.

Claim 4

A method of removing manganese from at least one dimensionally stable anode of an electrolysis cell comprising operating the electrolysis cell normally at a current density of at least about 0.2 amps per square inch until there is an undesirable reduction in cell efficiency due to the build up of anodic manganese deposits, briefly reversing the cell polarity at lower current densities of less than about 50 milliamps per square inch for a period of time sufficient to remove said anodic manganese deposits and then returning the cell to normal operating conditions.

Claim 5

A method of removing manganese from at least one dimensionally stable anode of an electrolysis cell comprising operating the electrolysis cell normally at a current density of at least about 0.2 amps per square inch until there is an undesirable reduction in cell efficiency due to the build up of anodic manganese deposits, briefly reversing the cell polarity at lower current densities of less than about 50 milliamps per square inch for a period of time sufficient to remove said anodic manganese deposits and then returning the cell to normal operating conditions.

Claim 7

A method of removing interfering mineral deposits from electrodes including anodic manganese deposits in a sea water electrolysis cell wherein at least one of said electrodes is a dimensionally stable anode comprising operating said cell normally by supplying an operating current from a primary rectifier to said cell such that the current density is at least about 0.2 amps per square inch until there is a reduction in cell efficiency due to mineral deposits forming on the electrodes, thereafter discontinuing the power supply from the primary rectifier and activating a secondary rectifier so as to supply a reduced current to said cell of opposite polarity, said current supplied from said secondary rectifier resulting in a current density of less than about 50 milliamps per square inch for a time period sufficient to remove interfering mineral deposits including anodic manganese deposits from the electrodes, said time period normally requiring from about one to ten minutes for each 24 hours of normal cell operation, thereafter discontinuing the power supply from the secondary rectifier and resupplying the power to the cell from the primary rectifier as before while preventing most current flow through the secondary rectifier by means of a resistor in line with the secondary rectifier during normal operation of the cell.

Claim 8

A method of removing interfering mineral deposits from electrodes including anodic manganese deposits in a sea water electrolysis cell wherein at least one of said electrodes is a dimensionally stable anode comprising operating said cell normally by supplying an operating current from a primary rectifier to said cell such that the current density is at least about 0.2 amps per square inch until there is a reduction in cell efficiency due to mineral deposits forming on the electrodes, thereafter discontinuing the power supply from the primary rectifier and activating a secondary rectifier so as to supply a reduced current to said cell of opposite polarity, said current supplied from said secondary rectifier resulting in a current density of less than about 50 milliamps per square inch for a time period sufficient to remove interfering mineral deposits including anodic manganese deposits from the electrodes, said time period normally requiring from about one to ten minutes for each 24 hours of normal cell operation, thereafter discontinuing the power supply from the secondary rectifier and resupplying the power to the cell from the primary rectifier as before while preventing most current flow through the secondary rectifier by means of a resistor in line with the secondary rectifier during normal operation of the cell.