High efficiency water-softening process

• US 9,056,784 B2
• Filed: 02/16/2012
• Issued: 06/16/2015
• Est. Priority Date: 09/19/2006
• Status: Active Grant

• Current Assignee: Ken V. Pandya
• Original Assignee: Ken V. Pandya
• Inventors: Pandya, Ken V.
• Primary Examiner(s): DRODGE, JOSEPH W
• Application Number:
  US13/398,648
• Publication Number:
  US 20120145643A1
• Time in Patent Office: 1,216 Days
• Field of Search: 210/638, 210/639, 210/650, 210/651, 210/709, 210/717, 210/719, 210724-727, 210/739, 210/804, 210/806, 210/908, 210/911, 210/912
• US Class Current: 1/1
• CPC Class Codes: B01D 21/01 using flocculating agents for purifying water C02F1/52; for liquid radioactive waste G21F9/10
• CPC Class Codes: B01D 61/58 Multistep processes
• CPC Class Codes: C02F 1/001 Processes for the treatment of water whereby the filtration technique is of importance C02F1/44 takes precedence; construction of filters in general B01D24/00 - B01D41/00
• CPC Class Codes: C02F 1/04 by distillation or evaporation
• CPC Class Codes: C02F 1/5236 using inorganic agents
• CPC Class Codes: C02F 1/56 Macromolecular compounds
• CPC Class Codes: C02F 1/66 by neutralisation; pH adjustment for degassing C02F1/20; using ion-exchange C02F1/42; for flocculation or precipitation of suspended impurities C02F1/52; for removing dissolved compounds C02F1/58
• CPC Class Codes: C02F 11/122 using filter presses C02F11/123 takes precedence
• CPC Class Codes: C02F 2001/007 Processes including a sedimentation step
• CPC Class Codes: C02F 2101/10 Inorganic compounds
• CPC Class Codes: C02F 2101/203 Iron or iron compound
• CPC Class Codes: C02F 2101/206 Manganese or manganese compounds
• CPC Class Codes: C02F 2101/32 Hydrocarbons, e.g. oil
• CPC Class Codes: C02F 2209/001 Upstream control, i.e. monitoring for predictive control
• CPC Class Codes: C02F 2209/10 Solids, e.g. total solids [TS], total suspended solids [TSS] or volatile solids [VS]
• CPC Class Codes: C02F 2209/20 Total organic carbon [TOC]
• CPC Class Codes: C02F 5/00 Softening water; Preventing scale; Adding scale preventatives or scale removers to water, e.g. adding sequestering agents softening using ion-exchange C02F1/42

Abstract

A high-efficiency water softening process is disclosed. The softening-process is particularly effective for the treatment of water process streams containing a broad array of contaminants, such as Ca, Mg, Ba, Sr, iron, aluminum, manganese, copper, zinc, silica, TOC, oil, and grease. The softening-process includes steps of: (a) adding carbonate ions and hydroxide ions to said water process stream until the process stream pH is raised to between at or about 10.5 and at or about 14.0; (b) optionally adding a coagulation aid so as to facilitate the creation of separated solids comprising a substantial portion of the contaminants; (c) optionally adding a polyelectrolyte so as to facilitate the creation of separated solids comprising a substantial portion of the contaminants; and (d) phase-separating the separated solids so as to remove the contaminants and produce a highly purified water process stream.

Claims

1. A process for removing at least some contaminants selected from the group consisting of Ca, Mg, Ba, Sr, Cu, Zn, iron, Mn, A1, SiO2, TOC, oil, grease, and TDS and TSS from a contaminated water stream, the process comprising steps of:

collecting a quantity of the water stream containing said contaminants for treatment;

analyzing the composition of the quantity of the water stream containing said contaminants for an amount of said contaminants in the quantity of the water stream;

adding at least one of carbonate or bicarbonate to the quantity of the water stream in an amount at least stoichiometrically equivalent to said contaminants in the quantity of the water stream;

adjusting the pH of the quantity of the water stream to a value from about 10.5 to 14;

separating the solids including said contaminants from the quantity of the water stream; and

recovering water containing a reduced contaminant content, wherein the step of separating comprises;

adding at least one of a coagulation or flocculation aid chemical to the quantity of the water stream, except where the water stream comprises an effective amount of aluminum material or caustic soda to effect flocculation or coagulation of solids of the contaminants of the water stream, and

and allowing solids formed by the coagulation or flocculation, including said contaminants and carbonate or bicarbonate and hydroxide precipitates in the quantity of the water stream to settle or rise from the water in a settling tank.

2. The process of claim 1, wherein the step of adjusting the pH further comprises adjusting the pH of the quantity of the water stream to a value from about 10.5 to 14 with at least one of sodium hydroxide and potassium hydroxide.

3. The process of claim 1, wherein the step of adjusting the pH further comprises adjusting the pH of the quantity of the water stream to a value from about 10.5 to 14 with at least one of carbon dioxide and carbon monoxide.

4. The process of claim 1, wherein the step of adjusting the pH further comprises adjusting the pH of the quantity of the water stream to a value from about 10.5 to 14 with at least one of lime and soda ash.

5. The process of claim 1, wherein the step of separating further comprises:

adding at least one polyelectrolyte selected from the group consisting of positive and negative polyelectrolyte chemicals to the quantity of the water stream.

6. The process of claim 1, wherein the coagulation aid chemical is selected from the group consisting of ferric chloride, alum, ferric sulfate and a waste caustic soda from an alumina plant, and the step of separating further comprises:

adding at least one polyelectrolyte selected from the group consisting of positive and negative polyelectrolyte chemicals to the quantity of the water stream.

7. The process of claim 1 wherein the quantity of the water stream is collected in a storage tank containing a separation system for removing precipitated contaminants from the storage tank.

8. The process of claim 1 wherein the formed solids settle in the quantity of the water stream.

9. The process of claim 1 wherein the formed solids remain in suspension or float in the quantity of the water stream.

10. The process of claim 1 wherein at least a portion of the step of separating the solids from the quantity of the water stream is performed by mechanical separation equipment selected from the group consisting of at least one of a reaction clarifier and a sludge thickener.

11. The process of claim 1 wherein the step of separating the solids from the quantity of the water stream further comprises treatment in a mechanical solid/liquid separator.

12. The process of claim 1 wherein the step of separating the solids from the quantity of the water stream further comprises treatment in a mechanical solid/liquid separator selected from the group consisting of a rotary drum vacuum filter, a press filter, a media filter, a membrane filter, or an ultra-filter system or a micro-filter system.

13. The process of claim 1 wherein the calcium plus magnesium contaminants in the quantity of the water stream are removed to a level less than 100 parts per million.

14. The process of claim 1 wherein the calcium plus magnesium contaminants in the quantity of the water stream are reduced to less than 1 percent of the calcium plus magnesium initially present.

15. The process of claim 1 wherein steps of collecting, adding, and adjusting are carried out in a storage tank.

16. The process of claim 1 wherein the calcium plus magnesium content, stated as CaCO₃, of the water, is reduced to less than 100 ppm and the TOC content of the water is reduced.

25. The process of claim 1 wherein the step of separating the solids from the quantity of the water stream further comprises treatment in a mechanical solid/liquid separator.

26. The process of claim 1 wherein the step of separating the solids from the quantity of the water stream further comprises treatment in a mechanical solid/liquid separator selected from the group consisting of a rotary drum vacuum filter, a press filter, a media filter, a membrane filter, or an ultra-filter system or a micro-filter system.

17. A process for removing at least some contaminants selected from the group consisting of Ca, Mg, Ba, Sr, Cu, Zn, iron, Mn, A1, SiO2, TOC, oil, grease, and TDS and TSS from a contaminated water stream, the process comprising steps of:

analyzing the composition of the quantity of the water stream containing said contaminants for an amount of said contaminants in the quantity of the water stream;

adding at least one of carbonate or bicarbonate to the quantity of the water stream in an amount at least stoichiometrically equivalent to said contaminants in the quantity of the water stream;

adjusting the pH of the quantity of the water stream to a value from about 10.5 to 14;

separating the solids including said contaminants from the quantity of the water stream; and

recovering water containing a reduced contaminant content, wherein the step of separating comprises;

adding at least one of a coagulation or flocculation aid chemical to the quantity of the water stream, except where the water stream comprises an effective amount of aluminum material or caustic soda to effect flocculation or coagulation of solids of the contaminants of the water stream, and

and allowing solids formed by the coagulation or flocculation, including said contaminants and carbonate or bicarbonate and hydroxide precipitates in the quantity of the water stream to settle or rise from the water in a settling tank.

18. The process of claim 17, wherein the step of adjusting the pH further comprises adjusting the pH of the water stream to a value from about 10.5 to 14 with at least one of sodium hydroxide and potassium hydroxide.

19. The process of claim 17, wherein the step of adjusting the pH further comprises adjusting the pH of the water stream to a value from about 10.5 to 14 with at least one of carbon dioxide and carbon monoxide.

20. The process of claim 17, wherein the step of adjusting the pH further comprises adjusting the pH of the water stream to a value from about 10.5 to 14 with at least one of lime and soda ash.

21. The process of claim 17, wherein the step of separating further comprises:

adding at least one polyelectrolyte selected from the group consisting of positive and negative polyelectrolyte chemicals to the water stream.

22. The process of claim 17, wherein the coagulation aid chemical is selected from the group consisting of ferric chloride, alum, ferric sulfate and a waste caustic soda from an alumina plant, and the step of separating further comprises:

adding at least one polyelectrolyte selected from the group consisting of positive and negative polyelectrolyte chemicals to the water stream.

23. The process of claim 17 wherein the quantity of the water stream is collected in a storage tank containing a separation system for removing precipitated contaminants from the storage tank.

24. The process of claim 17 wherein at least a portion of the step of separating the solids from the quantity of the water stream is performed by mechanical separation equipment selected from the group consisting of at least one of a reaction clarifier and a sludge thickener.

27. The process of claim 17 wherein the calcium plus magnesium contaminants in the quantity of the water stream are removed to a level less than 100 parts per million.

28. The process of claim 17 wherein the calcium plus magnesium contaminants in the quantity of the water stream are reduced to less than 1 percent of the calcium plus magnesium initially present.

29. The process of claim 17 wherein the calcium plus magnesium contents, stated as CaCO₃, of the water, is reduced to less than 100 ppm and the TOC content of the water is reduced.

30. A process for removing one or more contaminants from a contaminated water stream, at least one of which one or more contaminants is selected from the group consisting of Ca, Mg, Ba, Sr, Cu, Zn, iron, Mn, A1, SiO2, TOC, oil, grease, and TDS and TSS, the process comprising steps of:

analyzing the composition of the quantity of the water stream containing said contaminants for an amount of said contaminants in the quantity of the water stream;

adding at least one of carbonate or bicarbonate to the quantity of the water stream in an amount at least stoichiometrically equivalent to said contaminants in the quantity of the water stream;

adjusting the pH of the quantity of the water stream to a value from about 10.5 to 14;

separating the solids including said contaminants from the quantity of the water stream; and

recovering water containing a reduced contaminant content, wherein the step of separating comprises;

adding at least one of a coagulation or flocculation aid chemical to the quantity of the water stream, except where the water stream comprises an effective amount of aluminum material or caustic soda to effect flocculation or coagulation of solids of the contaminants of the water stream, and

and allowing solids formed by the coagulation or flocculation, including said contaminants and carbonate or bicarbonate and hydroxide precipitates in the quantity of the water stream to settle or rise from the water in a settling tank.