US4059513A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Treatment of water to remove certain ions therefrom
Assignee: Individual
•
Filing: 1977-02-22
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Granted: 1977-11-22
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Expires: 1997-02-22
Abstract
Abstract High sulfate content water is treated in a multistage process to remove sulfate and hardness. Sulfate concentration is reduced in the first stage of the process by addition of calcium hydroxide. Calcium concentration is reduced in the second stage of the process by reaction of carbon dioxide or bicarbonate and calcium and hydroxide ions from the first stage of the process, forming insoluble calcium carbonate.
Inventors
- 👤 Karel V. Zadera
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 15:59
CPC Classifications
C; C02; C02F; C02F1/00; C02F1/66; C02F5/00; C02F5/02
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
251 words
A two stage method of treating water to reduce concentrations of sulfate and hardness for use in a physical separation process where minerals contained in makeup water are concentrated by removing substantially pure water, producing sulfate ion concentrations in excess of 1500 ppm, consisting of the following steps: a. Conducting a portion of said concentrated mineral rich process water to a first reaction chamber, adding calcium hydroxide to the first reaction chamber in an amount sufficient to substantially increase calcium ion concentration and to produce hydroxide ion concentration in excess of 1000 ppm as calcium carbonate and in the presence of solid calcium sulfate precipitate calcium sulfate, and removing portion of solid calcium sulfate from the first reaction chamber; b. Transferring only the supernatant water from the first reaction chamber, to the second reaction chamber, adding raw makeup water to the second reaction chamber, the amount of raw water being several times greater than the amount of supernatant water from the first reaction chamber, together with sufficient amount of carbon dioxide or bicarbonate, to react with essentially all the hydroxide brought from the first reaction chamber forming carbonate and precipitate essentially all of the formed calcium carbonate; c. Transferring only the supernatant water from the second reaction chamber to said physical separation process; d. adding sufficient sulfuric acid to said physical separation process to prevent scaling therein; e. treating said supernatant water in said physical separation process to yield substantially pure water and a makeup water containing carbonate and sulfate hardness.
Claim 2
Dependent Claim
251 words
A two stage method of treating water to reduce concentrations of sulfate and hardness for use in a physical separation process where minerals contained in makeup water are concentrated by removing substantially pure water, producing sulfate ion concentrations in excess of 1500 ppm, consisting of the following steps: a. Conducting a portion of said concentrated mineral rich process water to a first reaction chamber, adding calcium hydroxide to the first reaction chamber in an amount sufficient to substantially increase calcium ion concentration and to produce hydroxide ion concentration in excess of 1000 ppm as calcium carbonate and in the presence of solid calcium sulfate precipitate calcium sulfate, and removing portion of solid calcium sulfate from the first reaction chamber; b. Transferring only the supernatant water from the first reaction chamber, to the second reaction chamber, adding raw makeup water to the second reaction chamber, the amount of raw water being several times greater than the amount of supernatant water from the first reaction chamber, together with sufficient amount of carbon dioxide or bicarbonate, to react with essentially all the hydroxide brought from the first reaction chamber forming carbonate and precipitate essentially all of the formed calcium carbonate; c. Transferring only the supernatant water from the second reaction chamber to said physical separation process; d. adding sufficient sulfuric acid to said physical separation process to prevent scaling therein; e. treating said supernatant water in said physical separation process to yield substantially pure water and a makeup water containing carbonate and sulfate hardness.
Claim 3
Dependent Claim
26 words
A method of treating water as defined in claim 1, in which the carbon dioxide and bicarbonate is a natural component of the raw makeup water.
Claim 4
Dependent Claim
34 words
A method of treating water as defined in claim 1, in which carbon dioxide is added to the second reaction chamber to supplement natural carbon dioxide and bicarbonate content of the raw makeup water.
Claim 5
Dependent Claim
63 words
A method of treating water as defined in claim 1, in which the calcium hydroxide addition is effected by addition of low quality lime source, to the first reaction chamber with CaO content in excess of 20% and SiO 2 content in excess of 30%, and silica leaching is retarded due to the high calcium and hydroxide concentration in the first reaction chamber.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-11-21 | 1981-05-23 | 1981-11-22 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-11-21 | 1985-05-23 | 1985-11-22 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-11-21 | 1989-05-23 | 1989-11-22 | $7700.00 | Window Closed / Lapsed |