Waste water treatment method

• US 8,105,488 B2
• Filed: 03/06/2009
• Issued: 01/31/2012
• Est. Priority Date: 09/01/2006
• Status: Active Grant

• Current Assignee: Anticline Disposal, LLC (NGL Energy Partners LP)
• Original Assignee: Anticline Disposal, LLC (NGL Energy Partners LP)
• Inventors: Shafer, Lee L., James, John W., Rath, Richard D., Eubank, Jesse
• Primary Examiner(s): BARRY, CHESTER T
• Application Number:
  US12/399,242
• Publication Number:
  US 20100038310A1
• Time in Patent Office: 1,061 Days
• Field of Search: 210/605, 210/630, 210/669, 210/681, 210/767, 210/902
• US Class Current: 210/605
• 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 1/24 by flotation C02F1/465 takes precedence
• CPC Class Codes: C02F 1/42 by ion-exchange ion-exchange in general B01J
• CPC Class Codes: C02F 1/441 by reverse osmosis
• CPC Class Codes: C02F 1/463 by electrocoagulation
• CPC Class Codes: C02F 2103/365 from petrochemical industry (e.g. refineries)
• CPC Class Codes: C02F 3/12 Activated sludge processes
• CPC Class Codes: C02F 3/1268 Membrane bioreactor systems
• CPC Class Codes: C02F 3/286 including two or more steps
• CPC Class Codes: C02F 3/30 Aerobic and anaerobic processes
• CPC Class Codes: C02F 9/00 Multistage treatment of water, waste water or sewage
• CPC Class Codes: Y02W 10/10 Biological treatment of water, waste water, or sewage
• CPC Class Codes: Y10S 210/902 Materials removed

Abstract

Systems and methods have been developed for reclaiming water contaminated with the expected range of contaminants typically associated with produced water, including water contaminated with slick water, methanol and boron. The system includes anaerobically digesting the contaminated water, followed by aerating the water to enhance biological digestion. After aeration, the water is separated using a flotation operation that effectively removes the spent friction reducing agents and allows the treated water to be reclaimed and reused as fracturing water, even though it retains levels of contaminants, including boron and methanol, that would prevent its discharge to the environment under existing standards. The treated water may further be treated by removing the methanol via biological digestion in a bioreactor, separating a majority of the contaminants from the water by reverse osmosis and removing the boron that passes through the reverse osmosis system with a boron-removing ion exchange resin.

Claims

1. A method for generating fracturing water from produced water:

transferring produced water contaminated with slick water, methanol and boron into an anaerobic pond;

holding the produced water in the anaerobic pond for at least a first mean residence time;

transferring anaerobic pond effluent to an aeration pond;

aerating the anaerobic pond effluent in the aeration pond for a second mean residence time;

transferring aeration pond effluent from the aeration pond to a solid/liquid flocculation separator; and

separating the aeration pond effluent with the solid/liquid flocculation separator to generate an aqueous effluent separated from a solids effluent;

biologically digesting the aqueous effluent in a bioreactor until a desired concentration of methanol is obtained;

transferring bioreactor effluent from the bioreactor to a reverse osmosis system;

separating contaminants from bioreactor effluent with the reverse osmosis system, the reverse osmosis system passing at least some boron in its permeate; and

removing the boron from the reverse osmosis permeate via a boron-selective removal process to obtain a desired level of boron in the reverse osmosis permeate.

2. The method of claim 1 further comprising:

providing at least some of the aqueous effluent as fracturing water to a fracturing fluid generation system.

3. The method of claim 1 further comprising:

receiving the produced water at a first pH less than about 10.0; and

wherein the steps of claim 1 are performed on water at a pH less than about 10.0.

4. The method of claim 1 wherein the first mean residence time is about 50 days or more.

5. The method of claim 1 further comprising:

removing the boron by passing the water through an ion-exchange resin selected for the removal of boron.

6. The method of claim 1 further comprising:

gelling the liquid effluent to generate fracturing gel.

7. The method of claim 1 further comprising:

transferring solids from the separator back to the anaerobic pond.

8. The method of claim 1 further comprising:

transferring solids from the bioreactor back to the anaerobic pond.

11. The method of claim 9 further comprising:

receiving the produced water at a first pH less than about 10.0; and

wherein the steps of claim 1 are performed on water at a pH less than about 10.0.

20. The method of claim 18 further comprising:

receiving the produced water at a first pH less than about 10.0; and

wherein the steps of claim 1 are performed on water at a pH less than about 10.0.

9. A method for generating fracturing water from produced water:

transferring produced water contaminated with slick water, methanol and boron into an anaerobic pond;

holding the produced water in the anaerobic pond for at least a first mean residence time;

transferring anaerobic pond effluent to an aeration pond;

aerating the anaerobic pond effluent in the aeration pond for a second mean residence time;

transferring aeration pond effluent from the aeration pond to a solid/liquid flocculation clarification treatment system;

floating the aeration pond effluent with the solid/liquid flocculation clarification treatment system to generate a floated aqueous effluent and a floc effluent;

biologically digesting the floated aqueous effluent in a bioreactor until a desired concentration of methanol is obtained;

transferring bioreactor effluent from the bioreactor to a first reverse osmosis system;

separating contaminants from bioreactor effluent with the first reverse osmosis system, the first reverse osmosis system passing at least some boron in its permeate;

transferring reject from the first reverse osmosis system to an electrocoagulation system;

neutralizing electrostatic charges of contaminants suspended in the reject of the first reverse osmosis system to remove or destroy some of the suspended contaminants with the electrocoagulation system to generate an electrocoagulation effluent containing at least some boron;

transferring at least some solids from the electrocoagulation system to an injection well;

transferring the electrocoagulation effluent and the first osmosis system permeate to a second reverse osmosis system;

separating contaminants from the electrocoagulation effluent with the second reverse osmosis system, the second reverse osmosis system passing at least some boron in its permeate;

transferring the second reverse osmosis permeate to the boron-selective treatment system; and

removing the boron from the first reverse osmosis permeate and the electrocoagulation effluent via a boron-selective removal process to obtain a desired level of boron in the first reverse osmosis permeate and the electrocoagulation effluent.

10. The method of claim 9 further comprising:

providing at least some of the floated aqueous effluent as fracturing water to a fracturing fluid generation system.

12. The method of claim 9 wherein the first mean residence time is about 50 days or more.

13. The method of claim 9 further comprising:

removing the boron by passing the water through an ion-exchange resin selected for the removal of boron.

14. The method of claim 9 further comprising:

gelling the liquid effluent to generate fracturing gel.

15. The method of claim 9 further comprising:

transferring solids from the dissolved air flotation treatment system back to the anaerobic pond.

16. The method of claim 9 further comprising:

transferring solids from the bioreactor back to the anaerobic pond.

17. The method of claim 9 further comprising:

transferring at least some of the solids from the electrocoagulation system back to the anaerobic pond.

18. A method for generating fracturing water from produced water:

transferring produced water contaminated with slick water, methanol and boron into an anaerobic pond;

holding the produced water in the anaerobic pond for at least a first mean residence time;

transferring anaerobic pond effluent to an aeration pond;

aerating the anaerobic pond effluent in the aeration pond for a second mean residence time;

transferring aeration pond effluent from the aeration pond to a solid/liquid separator; and

separating the aeration pond effluent with the solid/liquid separator to generate an aqueous effluent separated from a solids effluent;

biologically digesting the aqueous effluent in a bioreactor until a desired concentration of methanol is obtained;

transferring bioreactor effluent from the bioreactor to a reverse osmosis system;

separating contaminants from bioreactor effluent with the reverse osmosis system, the reverse osmosis system passing at least some boron in its permeate;

transferring reject from the reverse osmosis system to an electrocoagulation system;

neutralizing electrostatic charges of contaminants suspended in the reject of the reverse osmosis system to remove or destroy some of the suspended contaminants with the electrocoagulation system to generate an electrocoagulation effluent containing at least some boron;

transferring at least some solids from the electrocoagulation system to an injection well;

transferring the electrocoagulation effluent to a boron-selective treatment system;

transferring the reverse osmosis permeate to the boron-selective treatment system; and

removing the boron from the reverse osmosis permeate and the electrocoagulation effluent via a boron-selective removal process to obtain a desired level of boron in the reverse osmosis permeate and the electrocoagulation effluent.

19. The method of claim 18 further comprising:

providing at least some of the aqueous effluent as fracturing water to a fracturing fluid generation system.

21. The method of claim 18 wherein the first mean residence time is about 50 days or more.

22. The method of claim 18 further comprising:

removing the boron by passing the water through an ion-exchange resin selected for the removal of boron.

23. The method of claim 18 further comprising:

gelling the liquid effluent to generate fracturing gel.

24. The method of claim 18 further comprising:

transferring solids from the separator back to the anaerobic pond.

25. The method of claim 18 further comprising:

transferring solids from the bioreactor back to the anaerobic pond.

26. The method of claim 18 further comprising:

transferring at least some of the solids from the electrocoagulation system back to the anaerobic pond.

27. A system for treating water contaminated with methanol and boron comprising:

an anaerobic digester that receives the water and holds at least a portion of the water under anaerobic conditions;

an aerator that aerates the water;

a solid/liquid flocculation separator that separates contaminants from the water to produce a reclaimed water stream suitable for use as fracturing water;

at least one bioreactor that biologically digests methanol in the water until a desired concentration of methanol is obtained;

a boron-selective removal system that removes boron from the water until a desired concentration of boron is obtained; and

at least one filtration system that removes contaminants from the water until a desired concentration of contaminants other than boron and methanol is obtained.

28. The system of claim 27 wherein the anaerobic digester treats the water prior to the aerator treating the water.

29. The system of claim 28 wherein the aerator treats the water prior to separating contaminants from the water with the separator.

30. The system of claim 29 wherein the separator separates contaminants from the water prior to treating the water with the bioreactor, the boron-selective removal system and the filtration system.

31. The system of claim 27 wherein the solid/liquid flocculation separator utilizes dissolved air flotation to separate contaminants from the water.

32. The system of claim 27 wherein the boron-selective removal system includes a boron-selective resin.

33. The system of claim 27 wherein the at least one filtration system that removes contaminants from the water except that at least 50% of both boron and methanol passes through the filtration system in its permeate.

34. The system of claim 27 wherein the system is connected so that effluent of the bioreactor is treated with the at least one filtration system and permeate of the at least one filtration system is treated by the boron-selective removal system.

35. The system of claim 34 wherein the water is contaminated with at least about 7,000 milligrams per liter (mg/l) of total dissolved solids, at least about 10 mg/l of boron, and at least 500 mg/l about methanol and wherein the effluent of the boron-selective removal system contains less than about 500 mg/l of total dissolved solids, less than about 2 mg/l boron, and less than about 1 mg/l methanol.

36. The system of claim 35 wherein the water treated by the filtration system has a pH less than about 10.

37. The system of claim 36 wherein the water treated by the filtration system has a pH less than about 9.

38. The system of claim 36 wherein the water treated by the filtration system has a pH less than about 8.

39. The system of claim 27 wherein at least one filtration system utilizes reverse osmosis to separate contaminants from the water.

40. The system of claim 27 wherein the at least one bioreactor includes a first vessel bioreactor that biologically digests the water in a vessel and a membrane bioreactor biologically digests the water and also filters the water.

41. The system of claim 27 further comprising:

an electrocoagulation system for the removal or destruction of contaminants from reject of the reverse osmosis system; and

an injection well for the storage of solids from the electrocoagulation system.

42. A method for removing contaminants from produced water including boron, methanol and contaminants that inhibit the gelling of fracturing fluid when the produced water is used as fracturing water comprising:

anaerobically digesting the produced water containing the contaminants for a first period of time;

after anaerobically digesting the produced water, aerating the produced water for a second period of time;

after aerating the produced water, treating the produced water in a solid/liquid flocculation separator;

filtering effluent of the solid/liquid flocculation separator to generate a filtered water containing concentrations of boron and methanol;

biologically digesting the filtered water, thereby reducing the concentration of methanol in the filtered water;

separating contaminants from the filtered water using reverse osmosis, the reverse osmosis passing boron in its permeate and reject; and

electrocoagulating the reject, the electrocoagulation effluent passing boron in its effluent;

removing the boron from the reverse osmosis permeate and the electrocoagulation effluent via a boron removing ion exchange resin.

43. The method of claim 42 further comprising:

gelling the filtered water to generate fracturing gel.