Recovery of alkali values from salt-containing trona deposits
AssigneeIntermountain Research and Development Corporation
InventorWilliam R. Frint
Life of this patent
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Abstract
A method for recovering alkali values from subterranean deposits of trona ore associated with sodium chloride by contacting the trona with an aqueous mining solution containing sodium hydroxide and subsequently utilizing the alkali values contained in the resultant salt- and sodium carbonate-containing solution. The alkali values are preferably crystallized as substantially salt-free sodium carbonate monohydrate, which is dried to recover soda ash. The mother liquor containing all of the salt is then treated to prepare a dilute sodium hydroxide solution, which may be employed as aqueous mining solution in a cyclic method to recover additional alkali values from trona.
Claims7
A cyclic method for recovering alkali values from underground trona deposits associated with substantial deposits of sodium chloride, which comprises
- (i) introducing into the region of a trona deposit associated with substantial amounts of sodium chloride an aqueous NaCl-containing mining solvent resulting from the process set forth below and having dissolved therein from about 2 to 7% by weight sodium hydroxide to effect dissolution of trona as sodium carbonate;
- (ii) withdrawing from the region a portion of the resulting mining solution essentially saturated with sodium chloride and low in sodium bicarbonate content, the volume of solution being left in the region of the trona deposit to replace dissolved trona being insufficient as a purge to maintain the sodium chloride level in the withdrawn solution below an essentially saturated level;
- (iii) fractionally crystallizing dissolved sodium carbonate from the withdrawn mining solution as sodium carbonate monohydrate by introducing ammonia into the solution at a temperature of from 30.degree. to 50.degree. C., leaving in solution essentially all of the sodium chloride and leaving sufficient sodium carbonate dissolved in solution to yield the required sodium hydroxide concentration in the aqueous mining solvent prepared in steps (v) and (vi) set forth below;
- (iv) separating the crystallized solid from the mining solution and thereafter recovering the ammonia from the mining solution;
- (v) causticizing mining solution to convert sodium carbonate remaining in solution to sodium hydroxide;
- (vi) adding sufficient water to the mining solution to compensate substantially for that in the volume of solvent left in the region of the trona deposit and to result in an aqueous mining solution containing from about 2 to 7% by weight sodium hydroxide and essentially all of the sodium chloride withdrawn from the region of the trona deposit, the sodium chloride concentration being at least 5% by weight;
- and
- (vii) reintroducing the resulting aqueous mining solution, containing essentially all of the sodium chloride withdrawn from the region of the trona deposit, into the region of the trona deposit and repeating the cycle of recovery.
Dependencies are inferred from the claim text.