U.S. patents available from 1976 to present.
U.S. patent applications available from 2005 to present.

Nahcolite solution mining process

Patent 4815790 Issued on March 28, 1989. Estimated Expiration Date: Icon_subject May 13, 2008. Estimated Expiration Date is calculated based on simple USPTO term provisions. It does not account for terminal disclaimers, term adjustments, failure to pay maintenance fees, or other factors which might affect the term of a patent.

Patent References

2388009

3700280

3759328

3759574

3779602

3792902

Process for the solution mining of subterranean sodium bicarbonate bearing ore bodies
Patent #: 3953073
Issued on: 04/27/1976
Inventor: Kube

Producing shale oil from a cavity-surrounded central well
Patent #: 3967853
Issued on: 07/06/1976
Inventor: Closmann ,   et al.

Method of in situ mining
Patent #: 4249777
Issued on: 02/10/1981
Inventor: Morrell ,   et al.

Recovery of alkali values from sodium bicarbonate-containing ore with ammonia
Patent #: 4283372
Issued on: 08/11/1981
Inventor: Frint ,   et al.

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Inventors

Assignee

Application

No. 07/193920 filed on 05/13/1988

US Classes:

299/4, Input and output wells166/245, Specific pattern of plural wells166/272.6, Liquid material injected299/5, Dissolving or chemical reaction299/7WITH SEPARATION OF MATERIALS

Examiners

Primary: Suchfield, George A.

Attorney, Agent or Firm

International Classes

E21B 43/40 (20060101)
E21B 43/00 (20060101)
E21B 43/30 (20060101)
E21B 43/34 (20060101)
E21B 43/28 (20060101)

Abstract

Nahcolite solution mining process comprising drilling at least one well into a Nahcolite bed, circulating hot barren aqueous liquor in a cavity in said Nahcolite bed for a time sufficient to produce a pregnant liquor having an increase in the concentration of NaHCO3 in the range of from about 3 to about 20% while maintaining Na2 CO3 concentration in the range of about 0.25-4%, preferably less than 2.5%, withdrawing said pregnant liquor, cooling said pregnant liquor to preferentially precipitate NaHCO3 therefrom and to produce a barren liquor, recovering said NaHCO3, and reheating and re-injecting said barren liquor in said well. The cavity temperature is maintained below about 250° F. and preferably below about 200° F. The barren liquor is injected at a pressure of below about 150 psig. The pregnant liquor is extracted at a temperature in the range of from about 85° F. to about 200° F., and the cystallization occurs at a temperature of about 25°-120° F. The NaCl concentration is maintained at below about 6% and preferably below about 1.0%. Crystalline sodium bicarbonate of high purity (98+% NaHCO.sub. 3) is produced in the as-crystallized form, and simple washing increases the purity.

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