US4115219A
Expired / Lapsed
US
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Brine purification process
Assignee: Honeywell International Inc
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Filing: 1977-08-05
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Granted: 1978-09-19
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Expires: 1997-08-05
Abstract
Abstract In a process for purifying raw brine containing dissolved strontium, calcium and magnesium impurities wherein the raw brine is treated by contacting the brine with sodium carbonate for precipitation of strontium and calcium carbonate, contacting the brine containing the strontium and calcium carbonate solids with sodium hydroxide for precipitation of magnesium hydroxide, and removing strontium carbonate, calcium carbonate and magnesium hydroxide solids from the sodium chloride brine, the improvement which comprises passing at least a portion of said removed solids to the zone wherein the raw brine is contacted with sodium carbonate.
Inventors
- 👤 Alan B. Gancy
- 👤 Chester J. Kaminski
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-02 06:21
CPC Classifications
C; C01; C01F; C01F11/00; C01F11/18; C01D; C01D3/00; C01D3/14; C01D3/16; C01F11/181; C01F11/186; C01F11/187; C01F11/188; C01F5/00; C01F5/14
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
126 words
In a brine treatment process for removing dissolved strontium, calcium and magnesium impurities from a raw sodium chloride brine containing the same wherein the raw brine is contacted with sodium carbonate for formation of strontium carbonate and calcium carbonate solids, the brine containing the carbonate solids is contacted with sodium hydroxide for formation of magnesium hydroxide solids, and at least a major portion of said strontium carbonate, calcium carbonate and magnesium hydroxide solids is removed from the brine to produce a purified brine, and the brine is thereafter subjected to electrolysis in an electrolytic mercury cell, the improvement which comprises recycling said removed solids, in an amount of from about 25 to 1000% of the solids produced, for admixture with said raw brine and sodium carbonate.
Claim 2
Dependent Claim
126 words
In a brine treatment process for removing dissolved strontium, calcium and magnesium impurities from a raw sodium chloride brine containing the same wherein the raw brine is contacted with sodium carbonate for formation of strontium carbonate and calcium carbonate solids, the brine containing the carbonate solids is contacted with sodium hydroxide for formation of magnesium hydroxide solids, and at least a major portion of said strontium carbonate, calcium carbonate and magnesium hydroxide solids is removed from the brine to produce a purified brine, and the brine is thereafter subjected to electrolysis in an electrolytic mercury cell, the improvement which comprises recycling said removed solids, in an amount of from about 25 to 1000% of the solids produced, for admixture with said raw brine and sodium carbonate.
Claim 3
Dependent Claim
29 words
The process of claim 1 wherein sodium carbonate is employed to contact the raw brine in an amount sufficient to provide at least about 0.1 gpl excess sodium carbonate.
Claim 4
Dependent Claim
31 words
The process of claim 1 wherein sodium hydroxide is employed to contact said brine containing carbonate solids in an amount sufficient to provide at least about 0.1 gpl excess sodium hydroxide.
Claim 5
Dependent Claim
20 words
The process of claim 1 wherein the pH of said brine containing carbonate solids is from about 10 to 12.
Claim 6
Dependent Claim
24 words
The process of claim 1 wherein the pH of brine containing strontium carbonate, calcium carbonate and magnesium hydroxide is from about 10.5 to 12.5.
Claim 7
Dependent Claim
65 words
The process of claim 1 wherein the raw brine is contacted with said sodium carbonate and said recycled solids in a first treatment zone to form strontium carbonate and calcium carbonate solids, and the brine containing the carbonate solids is withdrawn from the first treatment zone and passed to a second treatment zone for contact with said sodium hydroxide to form said magnesium hydroxide solids.
Claim 8
Dependent Claim
68 words
The process of claim 6 wherein the brine containing the strontium carbonate, calcium carbonate and magnesium hydroxide solids is withdrawn from said second treatment zone and passed to a settling zone wherein strontium carbonate, calcium carbonate and magnesium hydroxide solids are removed by settling, and a portion of said removed settled solids are employed as said recycled solids, said recycled solids being passed to said first treatment zone.
Claim 9
Dependent Claim
46 words
The process of claim 6 wherein the raw brine contains from about 1 to 200 ppm dissolved strontium impurities, from about 100 to 6,000 ppm dissolved calcium impurities and from about 10 to 600 ppm dissolved magnesium impurities, calculated as elemental strontium, calcium and magnesium, respectively.
Claim 10
Dependent Claim
33 words
The process of claim 6 wherein sodium carbonate is added to the first treatment zone as sodium chloride brine saturated with sodium carbonate and containing up to 25 weight percent sodium carbonate solids.
Claim 11
Dependent Claim
21 words
The process of claim 6 wherein the purified brine is withdrawn from the settling zone and filtered to remove residual solids.
Claim 12
Dependent Claim
38 words
The process of claim 10 wherein the filtered brine contains less than about 1 ppm strontium, less than about 10 ppm calcium and less than about 1 ppm magnesium impurities, calculated as elemental strontium, calcium and magnesium, respectively.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-09-18 | 1982-03-20 | 1982-09-19 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-09-18 | 1986-03-20 | 1986-09-19 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-09-18 | 1990-03-20 | 1990-09-19 | $7700.00 | Window Closed / Lapsed |