Phosphorus control for waste streams from glyphosate manufacturing processes

Patent metadata

Field	Value
Publication number	US-11964892-B2
Application number	US-202217668750-A
Country	US
Kind code	B2
Filing date	Feb 10, 2022
Priority date	Jun 26, 2017
Publication date	Apr 23, 2024
Grant date	Apr 23, 2024

Abstract

This invention relates to processes for the removal of phosphorous from aqueous waste streams comprising phosphorus-containing compounds produced in the manufacture of glyphosate, in order to meet and typically exceed environmental regulations. More particularly, various embodiments of the present invention relate to the removal of phosphorous-containing compounds utilizing biological treatment system(s), oxidizing agent(s), and/or precipitant(s). The processes of the invention are also applicable to the removal of phosphorous compounds from phosphorous-containing waste streams other than those waste streams resulting from the manufacture of glyphosate.

First claim

What is claimed is:

1. A process for recovery of phosphorus from a waste stream comprising inorganic phosphorous, the process comprising:
subjecting at least a portion of the waste stream to biological treatment by microorganisms to form a biologically treated waste stream;
contacting the biologically treated waste stream with an oxidizing agent to form an oxidized treated waste stream, wherein the oxidizing agent is selected from the group consisting of calcium hypochlorite, sodium hypochlorite, bleach, and combinations thereof;
contacting the oxidized treated waste stream with a precipitant, thereby forming within the oxidized treated waste stream phosphate containing precipitates, wherein the precipitant comprises a metal selected from the group consisting of calcium, aluminum, iron, magnesium, and mixtures thereof; and
recovering a phosphate containing cake from the oxidized treated waste stream, thereby forming a treated waste stream.

2. The process as set forth in claim 1 wherein the precipitant comprises calcium.

3. The process as set forth in claim 1 wherein the precipitant is selected from the group consisting of FeCl 3 , Al 2 (SO 4 ) 3 , CaO, and combinations thereof.

4. The process as set forth in claim 1 wherein the treated waste stream comprises no more than about 3 ppm phosphorous.

5. The process as set forth in claim 1 wherein the total phosphorous removal [(weight P waste stream −weight P treated waste stream )/(weight P waste stream )×100] is at least about 50%.

6. The process as set forth in claim 1 wherein the total COD removal [(COD waste stream −COD treated waste stream )/(COD waste stream )×100] is at least about 50%.

7. The process as set forth in claim 1 wherein the oxidizing agent is calcium hypochlorite.

8. The process as set forth in claim 1 wherein the oxidizing agent is bleach.

9. The process as set forth in claim 1 wherein the biologically treated waste stream prior to contact with the oxidizing agent has a pH of from about 1 to about 7.5.

10. The process as set forth in claim 1 wherein the molar ratio of oxidizing agent to glyphosate present in the biologically treated waste stream is at least about 1:1.

11. The process as set forth in claim 1 wherein the molar ratio of oxidizing agent to aminomethylphosphonic acid (AMPA) present in the biologically treated waste stream is at least about 1:1.

12. The process as set forth in claim 1 wherein the oxidized treated waste stream is contacted with the precipitant at a rate of from about 0.05 g/l to about 2 g/l.

13. The process as set forth in claim 1 wherein the oxidized treated waste stream is contacted with the precipitant at a weight ratio of precipitant to oxidizing agent of from about 50:1 to about 500:1.

14. A process for recovery of phosphorus from a waste stream comprising inorganic phosphorous, the process comprising:
contacting at least a portion of the waste stream with a precipitant, thereby forming within the waste stream phosphate containing precipitates, to produce a precipitant treated stream, wherein the waste stream has a pH of from about 3 to about 7 when initially contacted with the precipitant, wherein the precipitant is selected from the group consisting of FeCl 3 , Al 2 (SO 4 ) 3 , CaO, and combinations thereof;
subjecting at least a portion of the precipitant treated stream to biological treatment by microorganisms to form a biologically treated waste stream; and
recovering a phosphate containing cake from the biologically treated waste stream, thereby forming a treated waste stream, wherein at least a portion of the waste stream is contacted with an oxidizing agent prior to contact of the waste stream with the precipitant, to form an oxidized treated stream and thereby oxidizing at least one organic phosphorus compound to form phosphate (PO 4 3− ), and wherein the oxidized treated stream is contacted with the precipitant.

15. The process as set forth in claim 14 wherein the total phosphorous removal [(weight P waste stream −weight P treated waste stream )/(weight P waste stream )×100] is at least about 50%.

16. The process as set forth in claim 14 wherein the total COD removal [(COD waste stream −COD treated waste stream )/(COD waste stream )×100] is at least about 50%.

17. The process as set forth in claim 14 , the process further comprising:
removing a portion of the waste stream as a precipitation phosphate liquor stream and contacting the precipitation phosphate liquor stream with a precipitant thereby forming within the precipitation phosphate liquor stream phosphate containing precipitates and producing a precipitant treated phosphate stream, wherein the portion of the waste stream removed as the precipitation phosphate liquor stream is different than the portion of the waste stream contacted with the oxidizing agent; and
combining the precipitant treated phosphate stream with the waste stream to form a combined precipitant treated phosphate waste stream and subjecting the combined precipitant treated phosphate waste stream to biological treatment by microorganisms to form a biologically treated waste stream.

18. A process for recovery of phosphorus from a waste stream comprising inorganic phosphorous, the process comprising:
removing a portion of the waste stream as a oxidation phosphate liquor stream and contacting the oxidation phosphate liquor stream with an oxidizing agent to oxidize at least one organic phosphorus compound to form phosphate (PO 4 3− ) and thereby forming an oxidized phosphate stream, wherein the oxidizing agent is selected from the group consisting of calcium hypochlorite, sodium hypochlorite, bleach, and combinations thereof;
combining the oxidized phosphate stream with the waste stream to form a combined oxidized phosphate waste stream and contacting the combined oxidized phosphate waste stream with a precipitant, producing a precipitant treated phosphate stream, wherein the precipitant comprises a metal selected from the group consisting of calcium, aluminum, iron, magnesium, and mixtures thereof;
subjecting the precipitant treated phosphate stream to biological treatment by microorganisms to form a biologically treated waste stream; and
recovering a phosphate containing cake from the biologically treated waste stream, thereby forming a treated waste stream.

Assignees

• Monsanto Technology Llc

Inventors

• Lei Peng
• Ren Ming
• Vaughn Anthony E

Classifications

• C02F9/00 Primary

  Multistage treatment of water, waste water or sewage · CPC title

• C01B25/26 Primary

  Phosphates (perphosphates C01B15/16) · CPC title

• C07F9/025

  Purification; Separation; Stabilisation; Desodorisation of organo-phosphorus compounds (of natural phosphatides C07F9/103; phosphines C07F9/5095) · CPC title

• C07F9/3808

  Acyclic saturated acids which can have further substituents on alkyl · CPC title

• C07F9/3813

  N-Phosphonomethylglycine; Salts or complexes thereof · CPC title