Patent Application
20050189301
Prior Art
Many food-processing operations require regular cleaning of process equipment with various chemicals. The wastewater generated from the wash process can have high fat or protein levels, which make the water difficult to process in water treatment plants due the high Biological Oxygen Demand (BOD) and Chemical Oxygen Demand (COD) levels.
It is desirable to achieve the following in such processes:
In accordance with our invention, the process comprises the following steps:
1. Adjusting the pH to less than 7 with an acid. The preferable pH is 5 to 3. Preferably sulfuric, phosphoric, or lactic acid is used. The salts described in step 2 can be incorporated in the acid solution.
2. Adding a calcium or magnesium salt. Preferably a calcium or magnesium salt with a polyvalent anion such as sulfate or phosphate
3. Separating the solids from the liquid phase. The separation is preferably done with a centrifuge. The most preferable centrifuge is a Sedicanter®. This is the product of a German company, Flotweg, and is most preferred because it can remove solids that are known in the art as “slippery”. The use of a Sedicanter®, high speed vertical disc clarifier, solid bowl, or horizontal scroll discharge decanter centrifuge improves the quality of the solid and liquid phase by providing a cleaner separation of the two phases on a continuous basis.
Flocculating agents maybe added to improve the speed and degree of separation.
4. Adjusting the pH of the solids and liquid phase to make them acceptable waste products; that is, products having a pH of 6-9 or more neutral.
The addition of calcium sulfate or calcium phosphate results in the co-precipitation of the protein, fat, and inorganic solids. The resulting solid has a density greater than one, which causes the solid phase to sink.
The chemicals used to process the waste stream do not degrade its value as a product and in some cases increase its value.
A dairy waste stream that contained high levels of fat and protein was treated in the following manner. This waste stream had a COD level of 150,000.
The pH was adjusted with a mixture of sulfuric acid and calcium sulfate to a pH of 4. The mixture was placed in a centrifuge, which separated the solid phase from the liquid phase. The pH of each phase was adjusted to 7. The solid phase is an acceptable feed supplement; that is, it has a low salt content which is low enough to be acceptable as cattle feed, and is high in protein. The liquid phase had a COD level of 30,000. The calcium and sulfate ions in the liquid phase have a low environmental impact on the water treatment plant; that is, the waste water had a low salt content acceptable to municipal authorities.
A waste stream that contained high levels of fat and protein was treated in the following manner.
The pH was adjusted with a mixture of sulfuric acid and calcium phosphate to a pH of 4. The mixture was placed in a centrifuge, which separated the solid phase from the liquid phase. The pH of each phase was adjusted to 7. The solid phase is a value added (i.e. higher price) feed supplement because it is fortified with calcium phosphate.
A waste stream that contained high levels of fat and protein was treated in the following manner.
The pH was adjusted with a mixture of phosphoric acid and calcium phosphate to a pH of 4.
The mixture was placed in a centrifuge, which separated the solid phase from the liquid phase. The pH of each phase was adjusted to 7. The solid phase is a value added feed supplement because it is fortified with calcium phosphate.
This application is a continuation-in-part of our prior co-pending provisional application No. 60/547,448, filed Feb. 26, 2004, entitled: “Food processing waste treatment”; the disclosure of which is incorporated herein by reference as if fully set forth; and we claim the benefit of the filing date of that application.
| Number | Date | Country | |
|---|---|---|---|
| 60547448 | Feb 2004 | US |
