Method for treating produced water
View Patent ↗Systems and methods have been developed for treating the waste water contaminated with methanol and boron in addition to other contaminants. The systems and methods allow specifically for the removal of the methanol and boron without the addition of significant chemicals to raise the pH. The water is 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.
1. A method for treating produced water comprising:
transferring produced water contaminated with at least one contaminant selected from a friction reducer and a fracturing polymer into an anaerobic treatment system;
holding the produced water in the anaerobic treatment system for at least a first mean residence time to generate anaerobic treatment system effluent;
aerating the anaerobic treatment system effluent in an aeration system for a second mean residence time to generate an aeration system effluent;
separating the aeration system effluent with a separator to generate a separated aqueous effluent and a separated solids effluent; and
providing the separated aqueous effluent as fracturing water to a fracturing fluid generation system.
2. The method of claim 1 further comprising:
separating an immiscible hydrocarbon phase from the produced water prior to transferring the produced water into the anaerobic treatment system.
3. The method of claim 1 further comprising:
receiving separate streams of produced water of different qualities from different sources, wherein at least one received stream is contaminated with at least one contaminant selected from a friction reducer and a fracturing polymer; and
transferring each of the separate streams to the anaerobic treatment system for combined treatment.
4. The method of claim 1 wherein the first mean residence time is about 50 days or more.
5. The method of claim 1 wherein the first mean residence time is a period of time sufficient to reduce the ratio of chemical oxygen demand to biological oxygen demand to about 2-to-1.
6. The method of claim 1 wherein the separating further comprises:
treating the aeration system effluent via one or more of flotation, coagulation, flocculation and physical separation.
7. The method of claim 1 further comprising:
gelling the separated aqueous effluent to generate fracturing gel.
8. The method of claim 6 further comprising:
filtering the separated aqueous effluent sufficiently to reduce an NTU level of the separated aqueous effluent to less than about 10 NTU prior to providing separated aqueous effluent as fracturing water.
9. The method of claim 1 wherein the produced water is contaminated with a concentration of acrylamide sufficient to render the produced water unsuitable for use as fracturing water.
10. A method for treating produced water comprising:
transferring produced water contaminated with at least one contaminant selected from a friction reducer and a fracturing polymer into an anaerobic treatment system;
treating the produced water in an anaerobic treatment system for at least a first mean residence time to generate anaerobic treatment system effluent;
aerating the anaerobic treatment system effluent in an aeration system for a second mean residence time to generate an aeration system effluent;
separating solids from the aeration system effluent with a separator to generate a separated aqueous effluent and a separated solids effluent;
biologically digesting the separated aqueous effluent to obtain a digested effluent; and
separating contaminants from the digested effluent with a desalination system to obtain a desalination effluent having a concentration of salt less than a desired concentration of salt.
11. The method of claim 10 further comprising:
providing at least some of the separated aqueous effluent as fracturing water to a fracturing fluid generation system.
12. The method of claim 10 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.
13. The method of claim 10 , wherein the first mean residence time is about 50 days or more.
14. The method of claim 10 , wherein the produced water is further contaminated with boron and the method further comprises:
removing boron from the desalination effluent by passing the water through a boron-selective treatment system.
15. The method of claim 14 , wherein the boron-selective removal system comprises an ion-exchange resin selected for the removal of boron.
16. The method of claim 10 further comprising:
providing the desalination effluent for use as process water in an industrial process.
17. A method treating produced water comprising:
transferring the produced water into an anaerobic treatment system;
anaerobically treating the produced water in the anaerobic treatment system for at least a first mean residence time;
after anaerobically treating the produced water, aerating the produced water for a second mean residence time;
biologically digesting the produced water in a bioreactor to produce a bioreactor effluent having a desired concentration of methanol; and
separating contaminants from the bioreactor effluent with a reverse osmosis system, the reverse osmosis system passing at least some boron in its permeate.
18. The method of claim 17 wherein the produced water contains boron and the method further comprises:
removing at least some of the boron from the reverse osmosis permeate via an ion-exchange resin selected for the removal of boron to obtain boron treatment system effluent having a desired level of boron.
19. The method of claim 17 further comprising: receiving the produced water at a first pH less than about 10.0; and
wherein the steps of claim 17 are performed on water at a pH less than about 10.0.
20. The method of claim 17 wherein at least some of the methanol removed by the bioreactor is generated by the anaerobic treatment system.