Brine systems for chlor-alkali membrane cells

Claim 2

A process for using sodium chloride brines averaging between about 23% to about 28% NaCl as feed salt for chlor-alkali electrolytic membrane cells, which comprises: (a) Subjecting said brine to a brine purification treatment wherein the brine is purified to remove impurities sufficient to make a satisfactory brine feed for electrolysis in chlor-alkali membrane cells, (b) Concentrating the so treated brine resulting from Step (a) in an evaporator or slurry concentrator to a slurry containing up to about 30% NaCl solids; and then, (c) Combining depleted salt solution resulting from the anode compartment of the membrane cells with the slurry produced by Step (b) to produce a cell brine feed having the desired ratio of salt to water.

Claim 3

The process of claim 1 wherein the sodium chloride brine is natural or solution brine.

Claim 4

The process of claim 1 wherein the brine is made from rock salt, solar salt or by-product salt.

Claim 5

The process of claim 1 wherein a portion of the brine produced by Step (a) is combined directly with the depleted salt solution in Step (c) while the remaining portion of the brine is concentrated to a slurry in Step (b) and then combined in Step (c).

Claim 6

The process of claim 1 wherein the brine is subjected to a primary purification treatment, then concentrated to a slurry, then mixed with the depleted salt solution resulting from the electrolysis, said mixture then being subjected to a secondary brine purification to remove any remaining impurities detrimental to the membrane cell electrolysis.

Claim 7

The process of claim 1 wherein the brine used as starting material is concentrated in a slurry concentrator to produce a salt slurry containing about 12% to about 21% NaCl solids content.

Claim 8

A process for retrofitting an existing chlor-alkali diaphragm cell plant having caustic evaporator effects to accommodate energy efficient membrane cells while at the same time allowing for use of the major components of equipment from said diaphragm cell plant which comprises: (a) Installing membrane cells and auxiliary electrical equipment as required in replacement of the diaphragm cells and electrical equipment in said plant installation, (b) Adding a secondary brine treatment process, (c) Converting at least one of the evaporator effects used to concentrate the diaphragm cell caustic to an evaporator effect adapted to produce a salt slurry from a brine feed, (d) Feeding purified brine to said evaporator and concentrating said solution to a slurry containing up to 30% solid salt, (e) Combining depleted salt solution resulting from the anode compartments of the membrane cells installed in said retrofitted plant installation with the slurry produced in Step (c) to produce a brine feed having the desired ratio of salt to water, (f) Employing the remaining evaporator effects for concentration of the caustic liquor produced by the cells to produce the desired concentration of caustic soda, (g) Employing the vapors produced from the evaporation of Step (f) as the primary heat source for the salt concentration in Step (c).

Claim 9

A process for retrofitting an existing chlor-alkali diaphragm cell plant having caustic evaporator effects to accommodate energy efficient membrane cells while at the same time allowing for use of the major components of equipment from said diaphragm cell plant which comprises: (a) Installing membrane cells and auxiliary electrical equipment as required in replacement of the diaphragm cells and electrical equipment in said plant installation, (b) Adding a secondary brine treatment process, (c) Converting at least one of the evaporator effects used to concentrate the diaphragm cell caustic to an evaporator effect adapted to produce a salt slurry from a brine feed, (d) Feeding purified brine to said evaporator and concentrating said solution to a slurry containing up to 30% solid salt, (e) Combining depleted salt solution resulting from the anode compartments of the membrane cells installed in said retrofitted plant installation with the slurry produced in Step (c) to produce a brine feed having the desired ratio of salt to water, (f) Employing the remaining evaporator effects for concentration of the caustic liquor produced by the cells to produce the desired concentration of caustic soda, (g) Employing the vapors produced from the evaporation of Step (f) as the primary heat source for the salt concentration in Step (c).

Claim 10

The process of claim 7 wherein the brine employed as salt feed in said plant is natural or solution mined brine having an average concentration of salt of between about 23% to 28% NaCl.

Claim 11

The process of claim 8 wherein the brine is concentrated in Step (c) to a slurry varying between about 12% and 21% crystalline salt.

Claim 12

The process of claim 9 wherein the depleted salt solution resulting from the anode compartment is increased in dissolved salt content from about 10% to 23% to the desired dissolved salt content required for the operation of the membrane cell.