US4188291A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Treatment of industrial waste water
Assignee: Individual
•
Filing: 1978-04-06
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Granted: 1980-02-12
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Expires: 1998-04-06
Abstract
Abstract A method is disclosed for processing industrial waste waters and, in particular, blow down water from thermal electric plants. The water is processed to concentrate the salts contained therein and to obtain a concentrated brine which can then be passed to a thermal evaporator and/or solar evaporation ponds. The water is processed by the addition of magnesium hydroxide and carbon dioxide in amounts sufficient to precipitate the calcium as calcium carbonate, thereby obtaining a water reduced in calcium content and increased in magnesium content from the industrial waste water. The treated water is processed to recover a purified water from a brine, preferably by reverse osmosis. Calcium hydroxide is added to the brine generated by the reverse osmosis process in an amount sufficient to precipitate magnesium hydroxide therefrom which can be recycled to supply the magnesium hydroxide used in pre-treatment of the water prior to the reverse osmosis process. A clarified brine is recovered from the magnesium hydroxide precipitation step and may then be naturally or thermally evaporated to produce a saturated slurry of salt solids. This slurry can then be further reduced to dryness by solar evaporation.
Inventors
- 👤 Donald R. Anderson
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 15:59
CPC Classifications
C; C02; C02F; C02F9/00; B; B01; B01D; B01D61/00; B01D61/02; B01D61/025; B01D65/00; B01D65/08; C02F1/00; C02F1/52; C02F1/5236; C02F5/00; C02F5/02; B01D2311/00; B01D2311/04; B01D2321/00; B01D2321/16; B01D2321/162; C02F2303/00; C02F2303/16; Y; Y02; Y02W; Y02W10/00; Y02W10/30; Y02W10/37; Y10; Y10S; Y10S203/00; Y10S203/21
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
139 words
A method for processing industrial waste water containing magnesium and calcium salts which comprises: (a) adding magnesium hydroxide and gaseous carbon dioxide to the waste water in an amount sufficient to precipitate calcium carbonate in the water; (b) settling the precipitates in said water and recovering a treated water having substantially reduced calcium content and a higher magnesium salt content than said waste water; (c) processing the treated water by reverse osmosis, distillation, electroldialysis or freezing to obtain a purified water and a residual brine enriched in calcium and magnesium contents; (d) adding calcium hydroxide to at least a portion of said brine in an amount sufficient to precipitate magnesium hydroxide therefrom; (e) separating said magnesium hydroxide from said brine; and (f) returning said magnesium hyroxide for addition to said waste water in the aforesaid precipitation of calcium carbonate.
Claim 2
Independent Claim
139 words
A method for processing industrial waste water containing magnesium and calcium salts which comprises: (a) adding magnesium hydroxide and gaseous carbon dioxide to the waste water in an amount sufficient to precipitate calcium carbonate in the water; (b) settling the precipitates in said water and recovering a treated water having substantially reduced calcium content and a higher magnesium salt content than said waste water; (c) processing the treated water by reverse osmosis, distillation, electroldialysis or freezing to obtain a purified water and a residual brine enriched in calcium and magnesium contents; (d) adding calcium hydroxide to at least a portion of said brine in an amount sufficient to precipitate magnesium hydroxide therefrom; (e) separating said magnesium hydroxide from said brine; and (f) returning said magnesium hyroxide for addition to said waste water in the aforesaid precipitation of calcium carbonate.
Claim 3
Dependent Claim
49 words
The method of claim 1 wherein said treated water is processed by reverse osmosis and including the step of adding calcium hydroxide to the waste water in an amount sufficient to coprecipitate magnesium hydroxide and silica in the water prior to the addition of magnesium hydroxide and carbon dioxide.
Claim 4
Dependent Claim
24 words
The method of claim 2 wherein clarified water is recovered from the magnesium hydroxide and silica coprecipitants prior to addition of the magnesium hydroxide.
Claim 5
Dependent Claim
37 words
The method of claim 3 wherein said industrial waste water also contains one or both of ferric and fluoride salts which are also coprecipitated with said magnesium hydroxide and silica as ferric hydroxide and calcium fluoride, respectively.
Claim 6
Dependent Claim
34 words
The method of claim 1 which comprises adding carbon dioxide to the treated water from step (b) in an amount sufficient to neutralize the treated water to a pH of about 5.5 to 8.0.
Claim 7
Dependent Claim
28 words
The method of claim 5 wherein said industrial waste water also contains aluminum salts and comprising the futher step of separating aluminum hydroxide from the neutralized treated water.
Claim 8
Dependent Claim
41 words
The method of claim 6 wherein said treated waste water is processed by reverse osmosis and including the addition of a mineral acid to adjust the pH of said water from 5 to about 6 before said processing by reverse osmosis.
Claim 9
Dependent Claim
32 words
The method of claim 1 including the step of processing said brine after separation of said magnesium hydroxide by vapor compression evaporation to cocentrate said brine to a slurry of salt solids.
Claim 10
Dependent Claim
20 words
The method of claim 8 wherein said industrial waste water is from an electrical power generation plant blow down stream.
Claim 11
Independent Claim
183 words
The method of processing waste water from an electrical power generation plant which comprises: (a) adding calcium hydroxide to the waste water in an amount sufficient to coprecipitate magnesium hydroxide and silica in the water; (b) adding magnesium hydroxide and gaseous carbon dioxide to the waste water in an amount sufficient to precipitate calcium carbonate in the water; (c) settling the precipitates in said water and recovering a treated water having substantially reduced silica and calcium contents and a higher magnesium salt content than said waste water; (d) processing the treated water by reverse osmosis, distillation, electrodialysis or freezing to obtain a purified water and a residual brine enriched in calcium and magnesium contents; (e) adding calcium hydroxide to at least a portion of said brine in an amount sufficient to precipitate magnesium hydroxide therefrom; (f) separating said magnesium hydroxide from said brine; (g) returning said magnesium hydroxide for addition to said waste water in the aforesaid precipitation of calcium carbonate; and (h) processing said brine from step (f) by vapor compression evaporation to concentrate said brine to a slurry of salt solids.
Claim 12
Independent Claim
183 words
The method of processing waste water from an electrical power generation plant which comprises: (a) adding calcium hydroxide to the waste water in an amount sufficient to coprecipitate magnesium hydroxide and silica in the water; (b) adding magnesium hydroxide and gaseous carbon dioxide to the waste water in an amount sufficient to precipitate calcium carbonate in the water; (c) settling the precipitates in said water and recovering a treated water having substantially reduced silica and calcium contents and a higher magnesium salt content than said waste water; (d) processing the treated water by reverse osmosis, distillation, electrodialysis or freezing to obtain a purified water and a residual brine enriched in calcium and magnesium contents; (e) adding calcium hydroxide to at least a portion of said brine in an amount sufficient to precipitate magnesium hydroxide therefrom; (f) separating said magnesium hydroxide from said brine; (g) returning said magnesium hydroxide for addition to said waste water in the aforesaid precipitation of calcium carbonate; and (h) processing said brine from step (f) by vapor compression evaporation to concentrate said brine to a slurry of salt solids.
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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) | 1983-02-11 | 1983-08-13 | 1984-02-12 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1987-02-11 | 1987-08-13 | 1988-02-12 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1991-02-11 | 1991-08-13 | 1992-02-12 | $7700.00 | Window Closed / Lapsed |