System and Method for Processing Aqueous Solutions

• US 20130052105A1
• Filed: 08/27/2012
• Published: 02/28/2013
• Est. Priority Date: 08/25/2011
• Status: Abandoned Application

• Current Assignee: B9 Plasma Incorporated
• Original Assignee: B9 Plasma Incorporated
• Inventors: Butler, James Charles
• Application Number:
  US13/595,946
• Publication Number:
  US 20130052105A1
• Time in Patent Office: Days
• US Class Current: 423/140
• CPC Class Codes: C02F 1/38 by centrifugal separation
• CPC Class Codes: C02F 1/74 with air aeration of stretches of water C02F7/00
• CPC Class Codes: C02F 2103/10 from quarries or from mining activities
• CPC Class Codes: C02F 2103/28 from the paper or cellulose industry
• CPC Class Codes: C02F 2103/36 from the manufacture of organic compounds
• CPC Class Codes: C02F 2209/005 Processes using a programmable logic controller [PLC]
• CPC Class Codes: C02F 2209/02 Temperature
• CPC Class Codes: C02F 2209/06 pH
• CPC Class Codes: C02F 9/00 Multistage treatment of water, waste water or sewage

Abstract

A system and method for processing aqueous solutions is provided. A method for controlled bubble collapse is provided, which catalyzes chemical reactions in aqueous solutions that cause metal and other ions and compounds in solution to form hydroxide, oxide, protonated, polyatomic and other stable precipitate species, compounds or complexes. The reactions convert metal ions in solution into stable metal hydroxide, oxide and other precipitates or solid complexes. Further processing including recirculation, detention, precipitate formation and detection can be utilized. Pressure and flow modulated and regulated recirculation of precipitate laden aqueous solution through a hydrocyclone particle or precipitate separation circuit can also be utilized.

Claims

1. An apparatus for reducing total dissolved solids in aqueous solutions, comprising:

a bubble collapse reactor having an inlet for receiving a solution and an outlet;

a pressure control valve at the inlet;

a gas and liquid separator and a fuel gas transfer pump downstream of the bubble gas reactor for removing fuel gas;

a detention and precipitation tank downstream of the gas and liquid separator; and

an outlet.

2. The apparatus of claim 1, further comprising a hydrocyclone separator downstream of the detention and precipitation tank.

3. The apparatus of claim 2, further comprising a fluid separator, a precipitate auger, and a precipitate dryer downstream of the hydrocyclone separator.

4. The apparatus of claim 1, further comprising a first controller for controlling the bubble collapse reactor, the pressure control valve, the gas and liquid separator, and the fuel gas transfer pump.

5. The apparatus of claim 2, further comprising a second controller for controlling the hydrocyclone separator.

6. The apparatus of claim 1, wherein the apparatus catalyzes reactions in an aqueuos solution between metal ions and hydroxides in solution that form stable metal oxyhydroxide precipitates.

7. The apparatus of claim 1, wherein the apparatus catalyzes formation of stable metal oxyhydroxide precipitates in an aqueous solution without chemical addition.

8. The apparatus of claim 1, wherein the apparatus catalyzes formation of stable metal oxyhydroxide precipitates in an aqueous solution without pH adjustment.

9. An apparatus for reducing total dissolved solids in aqueous solutions, comprising:

a bubble collapse reactor having an inlet for receiving a solution and an outlet;

a pressure control valve at the inlet;

a gas and liquid separator and a fuel gas transfer pump downstream of the bubble collapse reactor for removing fuel gas;

a hydrocyclone separator downstream of the gas and liquid separator; and

an outlet.

10. The apparatus of claim 9, further comprising a detention and precipitation tank between the gas and liquid separator and the hydrocyclone separator.

11. The apparatus of claim 9, further comprising a fluid separator, a precipitate auger, and a precipitate dryer downstream of the hydrocyclone separator.

12. The apparatus of claim 9, further comprising a chiller between the bubble collapse reactor and the gas and liquid separator.

13. The apparatus of claim 9, further comprising a first controller for controlling the bubble collapse reactor, the pressure control valve, the gas and liquid separator, and the fuel gas transfer pump.

14. The apparatus of claim 10, further comprising a second controller for controlling the hydrocyclone separator.

15. The apparatus of claim 9, wherein the apparatus catalyzes reactions in an aqueuos solution between metal ions and hydroxides in solution that form stable metal oxyhydroxide precipitates.

16. The apparatus of claim 9, wherein the apparatus catalyzes formation of stable metal oxyhydroxide precipitates in an aqueous solution without chemical addition.

17. The apparatus of claim 9, wherein the apparatus catalyzes formation of stable metal oxyhydroxide precipitates in an aqueous solution without pH adjustment.

18. A method of processing solution to remove dissolved solids comprising:

pumping a solution into a supply tank and allowing sediment to settle;

circulating the solution to a bubble collapse reactor at a controlled pressure;

catalyzing reactions by collapsing bubbles to convert metal ions in solution into stable metal hydroxide, oxide and other precipitates;

discharging the solution to a gas and liquid separator;

pumping off separated fuel gas;

transferring the solution to a detention and precipitation tank to remove precipitates; and

discharging the solution.

19. The method of claim 18, further comprising detaining the solution in the detention and precipitation tank until a detention termination condition is detected.

20. The method of claim 19, further comprising further processing the solution in a hydrocyclone for forming precipitate compositions.

21. The method of claim 20, further comprising separating the precipitate compositions from the solution in a fluid separator.

22. The method of claim 21, wherein the solution is transferred to the hydrocyclone if an elevation or drop in total solids in solution is detected in the detention and precipitation tank.

23. The method of claim 21, further comprising re-circulating the solution to the bubble collapse reactor after processing by the hydrocyclone.

24. The method of claim 18, further comprising re-circulating the solution to the bubble collapse reactor and the gas and liquid separator for additional processing prior to transferring the solution to the detention and precipitation tank.

25. The method of claim 24, further comprising mixing the solution with unprocessed solution before re-circulation to the bubble class reactor.

26. The method of claim 20, further comprising re-circulating the solution through the hydrocyclone and changing operating parameters of the hydrocyclone on each pass.

27. A method of harvesting Fe(OH)₃ from a process solution, comprising the steps of:

pumping a process solution into bubble collapse reactor at a controlled pressure;

catalyzing reactions by collapsing bubbles to convert metal ions in solution into stable metal hydroxide, oxide and other precipitates;

discharging the solution to a gas and liquid separator;

pumping off separated fuel gas;

transferring the solution to a hydrocyclone separator; and

harvesting Fe(OH)₃ from the solution.

28. A portable system for recovering dissolved solids from aqueous solutions, comprising:

a portable platform transportable to a location where processing of an aquesous solution is desired;

an input pump for pumping aqueous solution to be treated;

a bubble collapse reactor mounted to said portable platform and including an inlet for receiving the aqueous solution from the pump and an outlet;

a pressure control valve at the inlet of the bubble collapse reactor;

a gas and liquid separator mounted to the platform and downstream of the bubble gas reactor for separating gas from the aqueous solution;

a first outlet for discharging liquid separated by the gas and liquid separator; and

a second outlet for discharing gas separated by the gas and liquid separator.

29. The system of claim 28, further comprising a slurry pump for pumping a slurry at the location, a clarifier downstream of the slurry pump for processing the slurry, and a sediment dryer and sediment auger for processing sediment produced by the clarifier.

30. The system of claim 29, further comprising a transfer pump downstream of the clarifier for transferring clarified solution from the clarifier and a storage water tank downstream of the transfer pump for storing clarified solution, the input pump in fluid communication with the storage water tank.

31. The system of claim 28, further comprising a process water supply tank for storing liquid output by the first output for subsequent re-processing by the system.

32. The system of claim 28, further comprising a fuel gas storage tank for storing gas discharged from the second outlet.

33. The system of claim 28, further comprising a detention and precipitation tank, a hyrdocyclone, a fluid separator, and a precipitate dryer in fluid communication with the system for detaining and processing solution output by the system.

34. The system of claim 33, further comprising a processed water storage tank in communication with the fluid separator for storing processed water.

35. A method of harvesting Fe₂O₃ from a process solution, comprising the steps of:

pumping a process solution into bubble collapse reactor at a controlled pressure;

catalyzing reactions by collapsing bubbles to convert metal ions in solution into stable metal hydroxide, oxide and other precipitates;

discharging the solution to a gas and liquid separator;

pumping off separated fuel gas;

transferring the solution to a hydrocyclone separator; and

harvesting Fe₂O₃ from the solution.