Treatment of industrial waste water

• US 4,188,291 A
• Filed: 04/06/1978
• Issued: 02/12/1980
• Est. Priority Date: 04/06/1978
• Status: Expired due to Term

• Current Assignee: Donald R. Anderson
• Original Assignee: Donald R. Anderson
• Inventors: Anderson, Donald R.
• Primary Examiner(s): Hart, Charles N.
• Assistant Examiner(s): Therkorn, Ernest G.
• Application Number:
  US05/894,174
• Time in Patent Office: 677 Days
• Field of Search: 210/23 F, 210/23 H, 210/45, 210/46, 210/47, 210/49, 210/51, 210/52, 210/53, 210/56, 210/71, 210/72, 210/73 R, 210/73 SG, 210/257 M, 210/259, 203/7, 203/26, 203/10, 203/36, 203/DIG. 20, 204/180 P, 159/24 R, 159/24 A, 159/24 B, 159/DIG. 13, 159/20
• US Class Current: 210/639
• CPC Class Codes: B01D 2311/04 Specific process operations in the feed stream; Feed pretreatment
• CPC Class Codes: B01D 2311/08 Specific process operations in the concentrate stream
• CPC Class Codes: B01D 2311/2646 Decantation
• CPC Class Codes: B01D 2321/162 Use of acids
• CPC Class Codes: B01D 61/025 Reverse osmosis; Hyperfiltration
• CPC Class Codes: B01D 65/08 Prevention of membrane fouling or of concentration polarisation
• CPC Class Codes: C02F 1/441 by reverse osmosis
• CPC Class Codes: C02F 1/52 by flocculation or precipitation of suspended impurities C02F1/463 takes precedence
• CPC Class Codes: C02F 1/5236 using inorganic agents
• CPC Class Codes: C02F 2303/16 Regeneration of sorbents, filters
• CPC Class Codes: C02F 5/02 Softening water by precipitation of the hardness
• CPC Class Codes: C02F 9/00 Multistage treatment of water, waste water or sewage
• CPC Class Codes: Y02W 10/37 using solar energy
• CPC Class Codes: Y10S 203/21 Acrylic acid or ester

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.

Claims

1. 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.

2. 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.

3. The method of claim 2 wherein clarified water is recovered from the magnesium hydroxide and silica coprecipitants prior to addition of the magnesium hydroxide.

4. 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.

5. 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.

6. 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.

7. 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.

8. 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.

9. The method of claim 8 wherein said industrial waste water is from an electrical power generation plant blow down stream.

10. 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.