Production of high purity salt from high sulfate salt deposits

Claim 2

A process comprising: contacting a subterranean deposit containing NaCl contaminated with calcium and sulfate with an aqueous solvent to produce an aqueous brine containing dissolved calcium and sulfate values; transferring said contaminated brine to a calcium treatment zone and contacting said brine with a reagent to insolublize said calcium values, thereby producing a slurry with an aqueous phase substantially free from dissolved calcium values; transferring said aqueous phase to the first of a plurality of solar evaporation ponds arranged in a production zone for series flow such that the brine is maintained at its saturated concentration with respect to NaCl throughout the zone and becomes progressively more concentrated with respect to sulfate in successive ponds, thereby producing an NaCl crystal crop in each of said ponds; adjusting the flow rate of brine through said production zone to maintain the concentration of sulfate in the last of said ponds below its saturated concentration, thereby producing a sulfate-enriched effluent brine from said production zone; removing said sulfate-enriched effluent brine from said production zone; and harvesting the NaCl crystal crop from individual solar evaporation ponds of said production zone.

Claim 3

A process according to claim 1 wherein said sulfate-enriched effluent brine is transferred to a sulfate-disposal zone; said brine is cooled to depress the solubility of sulfate therein, thereby to form a slurry, the aqueous phase of which is depleted with respect to sulfate values; and said aqueous phase is recycled to said production zone.

Claim 4

A process according to claim 2 wherein during a period when the brine is the production zone is cold, sulfate-enriched effluent brine from said zone is returned to said subterranean deposit.

Claim 5

A process according to claim 1 wherein said sulfate-enriched effluent brine is recycled to contact said subterranean deposit as a portion of said aqueous solvent.

Claim 6

A process according to claim 1 comprising: contacting a subterranean halite deposit contaminated with glauberite (CaSO 4 ·Na 2 SO 4 ) with an aqueous solvent to produce an aqueous brine containing dissolved calcium and sulfate values; transferring said contaminated brine to an agitated reaction zone and mixing said brine in said reaction zone with sufficient reagent selected from the group consisting of sodium carbonate, sodium phosphate and sodium silicate to insolublize said calcium values, thereby producing a slurry with an aqueous phase containing substantially all of said sulfate values but substantially free from dissolved calcium values; transferring said aqueous phase to the first of a plurality of solar evaporation ponds arranged in a production zone for series flow such that the brine is maintained at its saturated concentration with respect to NaCl throughout the zone, deposits a crystal crop of NaCl substantially free from sulfate contaminants in each of said ponds and becomes progressively more concentrated with respect to sulfate in successive said ponds; and adjusting the flow rate of brine through said production zone to maintain the concentration of sulfate in the last of said ponds in said zone below about 7 percent by weight, based on the total weight of the brine, thereby producing a sulfate-enriched, NaCl-saturated effluent brine from said zone.

Claim 7

A process according to claim 5 wherein the concentration of sulfate in the production zone during periods in which the ambient air is above about 18° C is maintained below about 6 percent by weight.

Claim 8

A process according to claim 5 wherein the sulfate-enriched effluent brine from the production zone is recycled to said subterranean deposit wherein it is mixed with said aqueous solvent, thereby recycling substantially all of the sulfate values extracted from said deposit back to said deposit.