IP Library Granted Patent US 10,196,289
Granted Patent B2
US 10,196,289 · App. 13/698,129 · Granted Feb 5, 2019

Treatment of phosphate-containing wastewater

Inventors: Pierre Cote (Dundas, CA); Ahren Britton (Vancouver, CA); Ram Prasad Melahalli Sathyanarayana (Vancouver, CA); Rhonda Maria Hyslop (North Vancouver, CA)
Assignee: Ostara Nutrient Recovery Technologies Inc.
C02F9/00B01D61/022B01D61/04C01B25/26C01B25/45C01F11/22C02F1/52C02F1/5236B01D2311/04B01D2311/06C02F1/20C02F1/441C02F1/442C02F1/66C02F1/76C02F3/302C02F2001/425C02F2101/105C02F2101/14C02F2101/16C02F2103/007C02F2303/16
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Quick Facts
Patent No.
US 10,196,289
App. No.
13/698,129
Granted
Feb 5, 2019
Kind
B2
Abstract

A method for treating, and recovering phosphate compounds from, phosphate-containing wastewater. The method includes the steps of: (a) removing fluoride from the wastewater; (b) recovering a phosphate compound from the wastewater by maintaining super saturation conditions for the phosphate compound; and (c) polishing the wastewater. A silica removal step may be optionally performed after step (a) and before step (b).

Claims (25)

1. A method for treating, and recovering phosphate compounds from, wastewater, the method comprising:

(a) measuring, precipitating and removing fluoride from the wastewater by raising the pH of the wastewater by adding a calcium-containing base with a stoichiometric amount of calcium to precipitate the fluoride, wherein the pH does not promote precipitation of phosphates, and then further raising the pH of the wastewater by adding one or more calcium-free bases;

(b) recovering struvite from the wastewater from which fluoride has been removed by maintaining supersaturation conditions for the struvite; and

(c) polishing the wastewater

wherein step (c) comprises subjecting the wastewater from step (b) to a two-stage membrane treatment comprising:

(i) a first membrane treatment to obtain a first concentrate comprising divalent ions and a first permeate comprising monovalent ions; and

(ii) a second membrane treatment for the first permeate to obtain a second concentrate comprising monovalent ions and a second permeate comprising effluent.

2. A method according to claim 1 wherein the first concentrate is recirculated to step (a).

3. A method according to claim 1 wherein the first membrane treatment comprises nanofiltration.

4. A method according to claim 1 wherein the second membrane treatment comprises reverse osmosis.

5. A method according to claim 1 comprising lowering the pH to about pH 3 to 5 prior to the two-stage membrane treatment.

6. A method according to claim 1 comprising removing suspended solids by filtration prior to the two-stage membrane treatment.

7. A method according to claim 1 comprising removing ammonia from the second permeate.

8. A method according to claim 7 wherein removing ammonia comprises subjecting the second permeate to ion exchange.

9. A method according to claim 8 wherein ammonia-containing liquid of the ion exchange is recirculated to step (b).

10. A method according to claim 1 , wherein prior to step (b) the wastewater is subjected to a first membrane treatment to obtain a first concentrate comprising divalent ions and a first permeate comprising monovalent ions, wherein the first concentrate defines feed for step (b).

11. A method according to claim 10 wherein wastewater from step (b) is recirculated to step (a).

12. A method according to claim 10 wherein the first permeate is subjected to a second membrane treatment to obtain a second concentrate comprising monovalent ions and a second permeate comprising effluent.

13. A method according to claim 12 wherein the second membrane treatment comprises reverse osmosis.

14. A method according to claim 10 wherein the first membrane treatment comprises nanofiltration.

15. A method according to claim 10 comprising lowering the pH to about pH 3 to 5 prior to the first membrane treatment.

16. A method according to claim 10 comprising removing suspended solids by filtration prior to the first membrane treatment.

17. A method according to claim 10 comprising removing ammonia from the second permeate.

18. A method according to claim 17 wherein removing ammonia comprises subjecting the second permeate to ion exchange.

19. A method according to claim 18 wherein ammonia-containing liquid of the ion exchange is recirculated to step (b).

Assignments (3)
RELEASE OF SECURITY INTEREST Recorded Apr 22, 2020
From: WHEATSHEAF GROUP LIMITED
To: OSTARA NUTRIENT RECOVERY TECHNOLOGIES INC.
Reel/Frame 052468/0175 →
SECURITY INTEREST Recorded Nov 29, 2017
From: OSTARA NUTRIENT RECOVERY TECHNOLOGIES INC.
To: WHEATSHEAF GROUP LIMITED
Reel/Frame 044253/0717 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 19, 2012
From: COTE, PIERRE; BRITTON, AHREN; SATHYANARAYANA, RAM PRASAD MELAHALLI; HYSLOP, RHONDA MARIA
To: OSTARA NUTRIENT RECOVERY TECHNOLOGIES INC.
Reel/Frame 029321/0303 →
Continuity (2)
Provisional Application 61346002 · May 18, 2010
Related Publication 20130062289A1 · Mar 14, 2013
Cited By (1)
US 12,312,266