IP Library Granted Patent US 7,048,859
Granted Patent B1
US 7,048,859 · App. 10/013,406 · Granted May 23, 2006

Method for treatment of aqueous streams comprising biosolids

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Quick Facts
Patent No.
US 7,048,859
App. No.
10/013,406
Granted
May 23, 2006
Kind
B1
Abstract

A process is provided which can be used to clarify substantially aqueous streams and optionally separate biosolids, especially proteins, from food processing operations which comprises contacting an aqueous stream comprising biosolids with an anionic inorganic colloid and an organic polymer to flocculate the biosolids.

Claims (23)

1. A process consisting essentially of contacting a substantially aqueous stream, which comprises biosolids having anionic surface charges, with (a) an anionic inorganic colloid and (b) an organic polymer to produce flocculated biosolids under a condition effective to reduce the chemical oxygen demand of said stream; and optionally removing said flocculated biosolids from said stream; before said contacting, the pH of said stream is reduced with an acid to a pH of from 4.5 to less than 7; said inorganic colloid is present in said stream in the concentration of from about 20 to about 2000 ppm by weight and is selected from the group consisting of polysilicic acid, polysilicic acid microgel, acidic polyaluminosilicate, acid-stabilized polysilicate microgel, colloidal silica, colloidal tin oxide, aluminum modified colloidal silica, clay, and combinations of two or more thereof; and said organic polymer is present in said stream in the concentration of from about 1 to about 2500 ppm by weight, has a number average molecular weight greater than 1,000,000 and is selected from the group consisting of polyacrylamide, guar gum, and combinations thereof.

2. A process according to claim 1 wherein the pH of said stream is reduced to lower than 6 and said acid is selected from the group consisting of sulfuric acid, hydrochloric acid, carbon dioxide, sulfonic acids, carboxylic acids, acrylic acids, and combinations of two or more thereof.

3. A process consisting essentially of contacting a substantially aqueous stream, which comprises biosolids having anionic surface charges, with (a) an anionic inorganic colloid, (b) an organic polymer and (c) a coagulant selected from the group consisting of ferric chloride, ferrous sulfate, zinc chloride, zinc sulfate, alum, aluminum chloride, polyaluminum chloride and combinations of two or more thereof; before said contacting, the pH of said stream is reduced with an acid to a pH of from 4.5 to less than 7; said inorganic colloid is present in said steam in the concentration of from about 20 to about 2000 ppm by weight and is selected from the group consisting of polysilicic acid, polysilicic acid microgel, acidic polyaluminosilicate, acid-stabilized polysilicate microgel, colloidal silica, colloidal tin oxide, aluminum modified colloidal silica, clay, and combinations of two or more thereof; and said organic polymer is present in said steam in the concentration of from about 1 to about 2500 ppm by weight, has a number average molecular weight greater than 1,000,000 and is selected from the group consisting of polyacrylamide, guar gum, and combinations thereof.

4. A process according to claim 1 , 2 , or 3 wherein said anionic inorganic colloid is selected from the group consisting of polysilicic acid, polysilicic acid microgel, acidic polyaluminosilicate, acid-stabilized polysilicate microgel, and combinations of two or more thereof.

5. A process according to claim 4 wherein said polymer is polyacrylamide.

6. A process according to claim 5 wherein said acid and said anionic inorganic colloid are added simultaneously.

7. A process according to claim 6 wherein said stream comprising biosolids is derived from food processing stream.

8. A process according to claim 5 wherein said stream comprising biosolids is derived from food processing stream.

9. A process according to claim 1 , 2 , or 3 wherein said anionic inorganic colloid is colloidal silica.

10. A process according to claim 9 wherein said polymer is polyacrylamide.

11. A process according to claim 10 wherein said acid and said anionic inorganic colloid are added simultaneously.

12. A process according to claim 10 wherein said stream comprising biosolids is derived from food processing stream.

13. A process consisting essentially of contacting a substantially aqueous stream, which comprises biosolids having anionic surface charges, with (a) an anionic inorganic colloid and (b) a second organic polymer to produce flocculated biosolids under a condition effective to reduce the chemical oxygen demand of said stream; and optionally removing said flocculated biosolids from said stream; before said contacting, combining said stream with an effective amount of a first organic polymer to neutralize at least 1% anionic charges in said stream and to produce some cationic sites on said biosolids wherein said first organic polymer has a number average molecular weight lower than 1,000,000 and is selected from the group consisting of polyamine, diallyl dimethyl ammonium chloride polymers, and combinations thereof; said inorganic colloid is resent in said stream in the concentration of from about 20 to about 2000 ppm by weight and is selected from the group consisting of polysilicic acid, polysilicic acid microgel, acidic polyaluminosilicate, acid-stabilized polysilicate microgel, colloidal silica, colloidal tin oxide, aluminum modified colloidal silica, clay, and combinations of two or more thereof; and said second organic polymer is present in said stream in the concentration of from about 1 to about 2500 ppm by weight, has a number average molecular weight greater than 1,000,000 and is selected from the group consisting of polyacrylamide, guar gum, and combinations thereof.

14. A process according to claim 13 wherein said anionic inorganic colloid is selected from the group consisting of polysilicate, polyaluminosilicate, polysilicic acid microgel, and combinations of two or more thereof.

15. A process according to claim 14 wherein said first organic polymer has a number average molecular weight in the range from 10,000 to 500,000 and said polymer is said high low molecular weight cationic organic polymer.

16. A process according to claim 14 wherein said stream comprising biosolids is derived from food processing.

17. A process for reducing chemical oxygen demand of a substantially aqueous stream, which comprises biosolids having anionic surface charges, consisting essentially of:

(a) contacting said stream with (1) an acid to reduce pH of said stream to pH from 4.5 to no greater than pH 6; (2) an anionic inorganic colloid selected from the group consisting of polysilicate, polyaluminosilicate, polysilicic acid microgel, and mixtures thereof;

and (3) a cationic polyacrylamide having a molecular weight of at least 1,000,000 to produce flocculated biosolids wherein said anionic inorganic colloid has an average microgel size of greater than 10 am; and

(b) removing said flocculated biosolids from said stream.

18. A process for reducing chemical oxygen demand of a substantially aqueous stream, which comprises biosolids having anionic surface charges, consisting essentially of:

(a) contacting said stream with (1) an inorganic coagulant selected from the group consisting of ferric chloride, ferrous sulfite, zinc chloride, zinc sulfate, alum, aluminum chloride, polyaluminum chloride, and combinations of two or more thereof; (2) an anionic inorganic colloid selected from the group consisting of polysilicic acid, polysilicic acid microgel, acidic polyaluminosilicate and acid-stabilized polysilicate microgel to reduce pH of said stream to pH from 4.5 to no greater than pH 6 wherein said anionic inorganic colloid has an average microgel size of greater than 10 nm; and (3) a cationic polyacrylamide having a molecular weight of at least 1,000,000 to produce flocculated biosolids; and

(b) removing said flocculated biosolids from said stream.

Assignments (4)
RELEASE OF SECURITY INTEREST Recorded Apr 4, 2018
From: JPMORGAN CHASE BANK, N.A., AS ADMINISTRATIVE AGENT
To: THE CHEMOURS COMPANY FC, LLC
Reel/Frame 045845/0913 →
SECURITY INTEREST Recorded Apr 4, 2018
From: THE CHEMOURS COMPANY FC, LLC
To: JPMORGAN CHASE BANK, N.A., AS ADMINISTRATIVE AGENT
Reel/Frame 045846/0011 →
SECURITY AGREEMENT Recorded Jun 10, 2015
From: THE CHEMOURS COMPANY FC LLC; THE CHEMOURS COMPANY TT, LLC
To: JPMORGAN CHASE BANK, N.A.
Reel/Frame 035839/0675 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 15, 2015
From: E. I. DU PONT DE NEMOURS AND COMPANY
To: THE CHEMOURS COMPANY FC, LLC
Reel/Frame 035432/0023 →