Enhanced recovery of sodium carbonate from NaCl-containing sodium carbonate solutions

Claim 3

In the method of producing sodium carbonate from the aqueous NaOH- and NaCl-containing effluent from a chloralkali electrolytic diaphragm cell by carbonating the effluent, the improvement for recovering anhydrous sodium carbonate from the carbonated effluent which comprises subjecting the Na 2 CO 3 - and NaCl-containing effluent containing at least 10% by weight sodium chloride to evaporative crystallization at superatmospheric pressure and at a temperature of at least 120° C. to induce crystallization of anhydrous sodium carbonate without co-crystallization of sodium chloride until a crystallizer mother liquor containing less than 9% by weight Na 2 CO 3 and greater than 23% by weight NaCl is obtained; and separating the crystallized anhydrous sodium carbonate without NaCl crystallization from the crystallizer mother liquor to recover an anhydrous sodium carbonate product, essentially free of sodium chloride.

Claim 4

In the method of producing sodium carbonate from the aqueous NaOH- and NaCl-containing effluent from a chloralkali electrolytic diaphragm cell by carbonating the effluent, the improvement for recovering anhydrous sodium carbonate from the carbonated effluent which comprises subjecting the Na 2 CO 3 - and NaCl-containing effluent containing at least 10% by weight sodium chloride to evaporative crystallization at superatmospheric pressure and at a temperature of at least 120° C. to induce crystallization of anhydrous sodium carbonate without co-crystallization of sodium chloride until a crystallizer mother liquor containing less than 9% by weight Na 2 CO 3 and greater than 23% by weight NaCl is obtained; and separating the crystallized anhydrous sodium carbonate without NaCl crystallization from the crystallizer mother liquor to recover an anhydrous sodium carbonate product, essentially free of sodium chloride.

Claim 5

The method of claim 2 which further comprises recycling the NaCl-containing crystallizer liquor, after recovery of the product therefrom, to the electrolytic cell.

Claim 6

In the cyclic method of recovering alkali values by solution mining from subterranean trona ore deposits by the steps of introducing an aqueous sodium hydroxide solvent into contact with in situ trona ore to effect dissolution of sodium sesquicarbonate in the ore; withdrawing the resultant sodium carbonate-containing solution; crystallizing and recovering a sodium carbonate salt from such solution, leaving behind a mother liquor; causticizing residual sodium carbonate in the mother liquor; and recycling causticized mother liquor as aqueous sodium hydroxide solvent, the improvement for enhancing recovery of sodium carbonate values from an NaCl-containing aqueous sodium carbonate solution which results from solution mining trona deposits associated with substantial deposits of sodium chloride, which comprises subjecting such aqueous sodium carbonate solution which contains at least about 10% by weight sodium chloride to evaporative crystallization at superatmospheric pressure and at a temperature of at least 120° C. to induce crystallization of anhydrous sodium carbonate crystals without co-crystallization of sodium chloride until a crystallizer mother liquor containing less than 9% by weight Na 2 CO 3 and greater than 23% by weight NaCl is obtained but leaving sufficient sodium carbonate dissolved in solution for its causticization to sodium hydroxide that is required in the recycled aqueous sodium hydroxide solvent; and separating the crystallized anhydrous sodium carbonate without NaCl crystallization from the crystallizer mother liquor to recover an anhydrous sodium carbonate product, essentially free of sodium chloride.

Claim 7

In the cyclic method of recovering alkali values by solution mining from subterranean trona ore deposits by the steps of introducing an aqueous sodium hydroxide solvent into contact with in situ trona ore to effect dissolution of sodium sesquicarbonate in the ore; withdrawing the resultant sodium carbonate-containing solution; crystallizing and recovering a sodium carbonate salt from such solution, leaving behind a mother liquor; causticizing residual sodium carbonate in the mother liquor; and recycling causticized mother liquor as aqueous sodium hydroxide solvent, the improvement for enhancing recovery of sodium carbonate values from an NaCl-containing aqueous sodium carbonate solution which results from solution mining trona deposits associated with substantial deposits of sodium chloride, which comprises subjecting such aqueous sodium carbonate solution which contains at least about 10% by weight sodium chloride to evaporative crystallization at superatmospheric pressure and at a temperature of at least 120° C. to induce crystallization of anhydrous sodium carbonate crystals without co-crystallization of sodium chloride until a crystallizer mother liquor containing less than 9% by weight Na 2 CO 3 and greater than 23% by weight NaCl is obtained but leaving sufficient sodium carbonate dissolved in solution for its causticization to sodium hydroxide that is required in the recycled aqueous sodium hydroxide solvent; and separating the crystallized anhydrous sodium carbonate without NaCl crystallization from the crystallizer mother liquor to recover an anhydrous sodium carbonate product, essentially free of sodium chloride.

Claim 8

The method of claim 1, 2 or 4 wherein the NaCl-containing sodium carbonate solution subjected to evaporative crystallization possesses an NaCl:Na 2 CO 3 weight ratio which is less than 2.7:1.

Claim 9

The method of claim 1, 2 or 4 wherein the crystallization temperature is sufficiently high to reduce the sodium carbonate concentration in the crystallizer mother liquor below 6% by weight Na 2 CO 3 .

Claim 10

The method of claim 1, 2 or 4 wherein the temperature of the crystallizer is at least about 160° C.

Claim 11

The method of claim 7 wherein the NaCl-containing sodium carbonate solution subjected to evaporative crystallization possesses an NaCl:Na 2 CO 3 weight ratio which is less than about 4.5:1.

Claim 12

The method of claim 1, 2 or 4 which further comprises introducing an aqueous diluent into the solids-free crystallizer mother liquor in an amount sufficient to prevent precipitation of sodium chloride upon cooling of the mother liquor below the crystallization temperature at atmospheric pressure.