IP Library Granted Patent US 9,266,762
Granted Patent B2
US 9,266,762 · App. 13/254,881 · Granted Feb 23, 2016

Membrane filtration process with high water recovery

View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 9,266,762
App. No.
13/254,881
Granted
Feb 23, 2016
Kind
B2
Abstract

A membrane filtration process includes pretreating an influent solution to remove suspended solids, to produce a pretreated solution. pH of the pretreated solution is adjusted to at least 8.3 or lower by injecting CO 2 into the pretreated solution, to produce a conditioned solution. Injecting CO 2 also serves to supplement bicarbonate in the conditioned solution. The conditioned solution is flowed through a membrane filtration unit, to produce a permeate solution and a retentate solution. The membrane filtration unit comprises reverse osmosis membranes or nanofiltration membranes, or both. The retentate solution is then treated to cause precipitation, to produce a supernatant solution and a reject solution. At least a portion of the supernatant solution is recirculated by combining it with the influent solution prior to the step of pretreating.

Claims (26)

1. A membrane filtration process, comprising:

pretreating an influent solution to remove suspended solids, to produce a pretreated solution;

reducing pH of the pretreated solution from above 8.3 to 8.3 or lower by injecting CO 2 into the pretreated solution, to produce a conditioned solution containing an increased concentration of bicarbonate relative to the pretreated solution;

flowing the conditioned solution through a reverse osmosis or nanofiltration membrane filtration unit, to produce a permeate solution and a retentate solution;

collecting the permeate solution;

treating the retentate solution to cause precipitation of solids, to produce a supernatant solution and a reject solution, wherein the treating comprises (i) a step to convert bicarbonate to carbonate selected from the group consisting of a) heating the retentate solution, (b) reducing pressure of the retentate solution, and (c) heating, and reducing pressure of, the retentate solution and (ii) adding an alkali to the retentate solution after step (i); and

recirculating at least a portion of the supernatant solution by combining the portion of the supernatant solution with the influent solution prior to the step of pretreating.

2. The process of claim 1 , further comprising, prior to the step of pretreating, injecting CO 2 into the influent solution.

3. The process of claim 2 , wherein injecting CO 2 into the influent solution causes an increase in bicarbonate concentration.

4. The process of claim 1 , further comprising, prior to the step of flowing, adding an anti-scaling agent to the conditioned solution.

5. The process of claim 1 wherein the step of treating comprises adjusting pH of the retentate solution to between 9.5 and 12.0.

6. The process of claim 1 , wherein the step of treating comprises adjusting pH of the retentate solution to between 10.0 and 11.5.

7. The process of claim 1 , wherein, in the step of treating, the retentate solution is treated in a precipitation clarifier.

8. The process of claim 7 , wherein the step of treating comprises adding an alkali to the retentate solution in the precipitation clarifier.

9. The process of claim 7 , wherein the step of treating comprises adding a precipitation seed agent to the retentate solution in the precipitation clarifier.

10. The process of claim 7 , wherein the step of treating comprises adding a coagulant agent to the retentate solution in the precipitation clarifier.

11. The process of claim 7 , wherein the step of treating comprises adding a flocculant agent to the retentate solution in the precipitation clarifier.

12. The process of claim 1 wherein the step of treating comprises heating the retentate solution.

13. The process of claim 1 , wherein the step of treating comprises reducing pressure of the retentate solution.

14. The process of claim 1 , wherein the step of treating comprises collecting CO 2 .

15. The process of claim 14 , further comprising injecting the collected CO 2 into the pretreated solution, the influent solution, or the portion of the supernatant solution.

16. The process of claim 1 , wherein the step of pretreating comprises using microfiltration, ultrafiltration or multi-media filtration.

17. The process of claim 1 , further comprising:

flowing the permeate solution through a secondary reverse osmosis membrane filtration unit, to produce a secondary permeate solution and a secondary retentate solution;

collecting the secondary permeate solution; and

recirculating at least a portion of the secondary retentate solution by combining the portion of the secondary retentate solution with the retentate solution prior to step of treating.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 12, 2018
From: GENERAL ELECTRIC COMPANY
To: BL TECHNOLOGIES, INC.
Reel/Frame 047502/0065 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 6, 2011
From: WANG, SIJING; ZHU, YANRONG; HE, GAORONG
To: GENERAL ELECTRIC COMPANY
Reel/Frame 026857/0769 →