Chemically enhanced primary sludge fermentation method
View Patent ↗A method of treating wastewater to increase effluent volatile fatty acid content consisting of providing wastewater to a primary treatment vessel and adding a select quantity of a chemical, typically an aluminum or iron salt, to the wastewater, enhancing the separation of organic matter. Separated organic matter is then removed from the chemically treated wastewater forming a primary sludge and a primary effluent. A portion of the primary sludge is fermented to form a volatile fatty acid rich liquor. The volatile fatty acid rich liquor may then be used with the primary effluent, directed to a bioreactor, thereby forming a volatile fatty acid enriched bioreactor feed. The volatile fatty acid enriched influent may be further treated through known biological phosphorous and nitrogen removal methods.
1. A method of treating wastewater to increase effluent volatile fatty acid content comprising:
providing a wastewater to a primary treatment vessel;
adding a select quantity of a chemical to the wastewater to enhance separation of organic matter from the wastewater, wherein the select quantity of the chemical added to the wastewater is selected to cause at least one of a desired decrease in phosphorous concentration and a desired increase in the quantity of primary sludge removed in a removing step;
removing separated organic matter from the chemically treated wastewater to form a primary sludge and a primary effluent;
fermenting a portion of the primary sludge to form a volatile fatty acid rich liquor; and
mixing the volatile fatty acid rich liquor with the primary effluent to form a volatile fatty acid enriched effluent.
2. A method of treating wastewater to increase effluent volatile fatty acid content comprising:
providing a wastewater to a primary treatment vessel;
adding a select quantity of aluminum sulfate to the wastewater to enhance separation of organic matter from the wastewater wherein the quantity of aluminum sulfate added to the wastewater is selected to attain in the wastewater, after the addition, a molar ratio of aluminum to phosphorus between 0.1 and 20;
removing separated organic matter from the chemically treated wastewater to form a primary sludge and a primary effluent;
fermenting a portion of the primary sludge to form a volatile fatty acid rich liquor; and
mixing the volatile fatty acid rich liquor with the primary effluent to form a volatile fatty acid enriched effluent.
3. A method of treating wastewater to increase effluent volatile fatty acid content comprising:
providing a wastewater to a primary treatment vessel;
adding a select quantity of a chemical to the wastewater to enhance separation of organic matter from the wastewater;
removing separated organic matter from the chemically treated wastewater to form a primary sludge and a primary effluent;
fermenting a portion of the primary sludge to form a volatile fatty acid rich liquor; and
mixing the volatile fatty acid rich liquor with the primary effluent to form a volatile fatty acid enriched effluent, wherein the volatile fatty acid enriched effluent has a ratio of volatile fatty acid content to ortho-phosphate content by weight equal to or greater than 7 to 1.
4. A method of treating wastewater to increase effluent volatile fatty acid content comprising:
providing a wastewater to a primary treatment vessel;
adding a select quantity of a chemical to the wastewater to enhance separation of organic matter from the wastewater;
removing separated organic matter from the chemically treated wastewater to form a primary sludge and a primary effluent;
fermenting a portion of the primary sludge to form a volatile fatty acid rich liquor for a period of time to produce greater than 0.1 pounds of a volatile fatty acid for each pound of primary sludge fermented; and
mixing the volatile fatty acid rich liquor with the primary effluent to form a volatile fatty acid enrichment effluent.
5. The method of claim 4 wherein the period of time the primary sludge is fermented in the fermentation step is between 2 and 8 days.
6. A method of treating wastewater to reduce effluent phosphorus content comprising:
providing wastewater to a primary treatment vessel;
adding a select quantity of a chemical to the wastewater to enhance separation of organic matter from the wastewater;
removing separated organic matter from the chemically treated wastewater to form a primary sludge and a primary effluent;
fermenting a portion of the primary sludge to form a volatile fatty acid rich liquor;
enriching a bioreactor influent with the volatile fatty acid rich liquor; and
treating the enriched bioreactor influent with a biological phosphorus removal process to reduce a phosphorus content of the enriched bioreactor influent.
7. The method of claim 6 wherein the chemical is one of an aluminum salt, iron salt and a polymer.
8. The method of claim 6 wherein the select quantity of chemical added to the wastewater is selected to cause at least one of a desired decrease in phosphorous concentration and a desired increase in the quantity of primary sludge removed in the removing step.
9. The method of claim 6 wherein the chemical is aluminum sulfate and the quantity of aluminum sulfate added to the wastewater is selected to attain in the wastewater, after the aluminum sulfate addition, a molar ratio of aluminum to phosphorus between 0.1 and 20.
10. The method of claim 6 wherein the enriched bioreactor influent has a ratio of volatile fatty acid content to ortho-phosphate content by weight equal to or greater than 7 to 1.
11. The method of claim 6 wherein the primary sludge is fermented in the fermentation step for a period of time to produce greater than 0.1 pounds of the volatile fatty acid for each pound of primary sludge fermented.
12. The method of claim 6 wherein the period of time the primary sludge is fermented in the fermentation step is between 2 and 8 days.
13. A method of treating wastewater to reduce effluent total nitrogen content comprising:
providing wastewater to a primary treatment vessel;
adding a select quantity of a chemical to the wastewater to enhance separation of organic matter from the wastewater;
removing separated organic matter from the chemically treated wastewater to form a primary sludge and a primary effluent;
fermenting a portion of the primary sludge to form a volatile fatty acid rich liquor;
enriching a bioreactor influent with the volatile fatty acid rich liquor; and
treating the enriched bioreactor influent with a biological nitrogen removal process to reduce a nitrogen content of the enriched bioreactor influent.
14. The method of claim 13 wherein the chemical is one of an aluminum salt, iron salt and a polymer.
15. The method of claim 13 wherein the select quantity of chemical added to the wastewater is selected to cause at least one of a desired decrease in nitrogen concentration and a desired increase in the quantity of primary sludge removed in the removing step.
16. The method of claim 13 wherein the chemical is one of ferric chloride and aluminum sulfate and the quantity of the chemical added to the wastewater is selected to attain in the wastewater, after the chemical addition, a reduced level of colloidal material.
17. The method of claim 13 wherein the primary sludge is fermented in the fermentation step for a period of time to produce greater than 0.1 pounds of the volatile fatty acid for each pound of primary sludge fermented.
18. The method of claim 13 wherein the period of time the primary sludge is fermented in the fermentation step is between 2 and 8 days.