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A multi-phase process for removing phosphorus from wastewater in a triple ditch or triple basin system where wastewater influent is sequentially directed to each of the three basins or ditches, sometimes referred to as first and second outer basins and an intermediate basin. During each phase of the

A multi-phase process for removing phosphorus from wastewater in a triple ditch or triple basin system where wastewater influent is sequentially directed to each of the three basins or ditches, sometimes referred to as first and second outer basins and an intermediate basin. During each phase of the process, the mixed liquor in at least one of the basins is subject to settling. In one or more phases of the process, the mixed liquor, in certain basins, is subjected to anaerobic and aerobic treatment. Anaerobic treatment results in the growth or proliferation of phosphorus storing microorganisms. These phosphorus-storing microorganisms take up phosphorus when the mixed liquor is subjected to aerobic conditions. One of the basins, the intermediate basin, can be designed to have a volume greater than either of the first or second outer basins. Further, the triple basin or triple ditch system is designed to transfer mixed liquor suspended solids or biomass from one basin to another. Each outer basin is provided with a submersible pump that is operatively connected to a network of pipes such that mixed liquor suspended solids can be transferred from each of the first and second outer basins to the intermediate basin. Further, mixed liquor suspended solids can be transferred back and forth between the two outer basins.

대표청구항 ▼

1. A multi-phase process for the removal of phosphorus from a wastewater influent stream in a triple basin wastewater treatment facility having first, second and third basins wherein during the course of the multi-phase process a settling phase is carried out in at least two of the three basins, the

1. A multi-phase process for the removal of phosphorus from a wastewater influent stream in a triple basin wastewater treatment facility having first, second and third basins wherein during the course of the multi-phase process a settling phase is carried out in at least two of the three basins, the process comprising:a. during the multi-phase process, directing the wastewater influent stream into each of the three basins during three different phases of the process to form mixed liquor;b. during the multi-phase process, maintaining at least two of the three basins under anaerobic conditions, one basin being maintained under anaerobic conditions during one phase and another basin being maintained under anaerobic conditions during another phase;c. maintaining at least one of the three basins under aerobic conditions during selected phases of the process;d. during each of the phases of the process, maintaining at least one of the basins in a settling mode, and wherein during the course of the multi-phase process at least two of the three basins are used for settling; ande. wherein maintaining the basins under anaerobic conditions give rise to the growth of phosphorus storing microorganisms and wherein the phosphorus storage microorganisms take up phosphorus in the basins maintained under aerobic conditions. 2. The process of claim 1 wherein the process includes at least six phases and wherein during two phases the wastewater influent is initially directed into basins being maintained under anaerobic conditions, and wherein during two other phases the wastewater influent stream is initially directed into basins being maintained under aerobic conditions. 3. The process of claim 1 wherein the three basins include first and second outer basins and an intermediate basin, and wherein the process includes pumping the mixed liquor from one or both of the outer basins to the intermediate basin. 4. The process of claim 1 wherein the three basins include first and second outer basins and an intermediate basin, and wherein during at least one phase of the process wastewater influent is directed into the first outer basin and effluent from the first outer basin is directed to the intermediate basin and effluent from the intermediate basin is directed to the second outer basin; and wherein during another phase of the process, the wastewater influent is directed into the second outer basin and the effluent of the second outer basin is directed to the intermediate basin and effluent from the intermediate basin is directed to the first outer basin. 5. The process of claim 4 wherein the first and second outer basins assume a settling mode during certain phases of the process. 6. The process of claim 4 including at least one process phase where the wastewater influent is directed into the intermediate basin and wherein the effluent from the intermediate basin is directed to one of the first or second outer basins which assumes a settling mode. 7. The process of claim 1 wherein the process includes at least one anoxic phase wherein the mixed liquor in at least one of the basins is maintained under anoxic conditions. 8. The process of claim 1 wherein during at least one phase of the process the mixed liquor in the intermediate basin is maintained under anoxic conditions so as to perform a denitrifying function. 9. The process of claim 1 wherein the three basins include first and second outer basins and an intermediate basin, wherein the process includes at least six phases:a. a first phase wherein influent wastewater is directed into a first outer basin maintained under anaerobic conditions and wherein effluent from the first outer basin is directed to the intermediate basin where the mixed liquor therein is maintained under aerobic conditions and wherein the effluent from the intermediate basin is directed to the second outer basin which is maintained in a settling mode;b. a second phase like the first phase except that the mixed liquor of the fir st outer basin is maintained under aerobic conditions;c. a third phase where influent wastewater is directed into the intermediate basin and the mixed liquor of the intermediate basin is maintained under aerobic conditions, and wherein the effluent of the intermediate basin is directed to the second outer basin where mixed liquor therein along with the mixed liquor in the first outer basin is maintained in a settling mode;d. a fourth phase wherein wastewater influent is directed into the second outer basin which is maintained under anaerobic conditions and wherein the effluent of the second outer basin is directed to the intermediate basin which is maintained under aerobic conditions and wherein the mixed liquor of the intermediate basin is directed to the first outer basin which is maintained in a settling mode;e. a fifth phase like the fourth phase with the exception that the second outer basin is maintained under aerobic conditions; andf. a sixth phase where wastewater influent is directed into the intermediate basin which is maintained under aerobic conditions and wherein the effluent of the intermediate basin is directed to the first outer basin where the mixed liquor therein along with the mixed liquor in the second outer basin is maintained in a settling mode. 10. The process of claim 9 including transferring mixed liquor suspended solids from either or both of the first and second outer basins to the intermediate basin. 11. The process of claim 9 wherein the volume of the intermediate basin exceeds the volume of either the first or second outer basin. 12. The process of claim 11 wherein the intermediate basin constitutes 35% to 50% of the total volume of all three basins. 13. The process of claim 9 including at least one additional anoxic phase where wastewater influent is directed into the intermediate basin and the mixed liquor in the intermediate basin is maintained under anoxic conditions, and wherein the mixed liquor effluent from the intermediate basin is directed to one of the first or second outer basins which is maintained in a settling mode. 14. The process of claim 13 wherein the process includes two anoxic phases. 15. The process of claim 1 wherein one basin at a time is maintained under anaerobic conditions. 16. The process of claim 1 including, during one or more phases of the process, increasing the concentration of mixed liquor suspended solids in a basin maintained under anaerobic conditions by transferring mixed liquor suspended solids from a basin maintained in a settling mode to the basin maintained under anaerobic conditions. 17. A process for removing phosphorus from wastewater in a triple basin system having first and second outer basins and an intermediate basin, comprising:a. in one phase of treatment, directing wastewater influent into a first outer basin and mixing the wastewater with activated sludge to form mixed liquor and maintaining the mixed liquor in the first outer basin under anaerobic conditions;b. directing the effluent from the first outer basin to the intermediate basin, and maintaining the mixed liquor in the intermediate basin under aerobic conditions;c. directing the effluent from the intermediate basin to the second outer basin and maintaining the second outer basin in a settling mode so as to separate activated sludge from treated effluent;d. in another phase of treatment, changing the treatment conditions in the first outer basin from anaerobic to aerobic, and directing the mixed liquor effluent from the first outer basin to the intermediate basin and directing the effluent from the intermediate basin to the second outer basin;e. in another phase of treatment, switching the wastewater influent from being directed into the first outer basin to being directed into the intermediate basin, and maintaining the mixed liquor in the intermediate basin under aerobic conditions and transferring the mixed liquor effluent from the intermediate basin to at least one of the first or seco nd basins while maintaining the first and second outer basins in a settling mode; andf. wherein the anaerobic treatment of the mixed liquor gives rise to the growth of phosphorus storage microorganisms and wherein the phosphorus storage microorganisms take up phosphorus when exposed to aerobic conditions. 18. The process of claim 17 further includinga. in another phase of treatment, directing the wastewater influent into the second outer basin and mixing the wastewater with activated sludge to form mixed liquor and maintaining the mixed liquor in the second outer basin under anaerobic conditions;b. while the second outer basin is being maintained under anaerobic conditions, directing mixed liquor effluent from the second outer basin to the intermediate basin and maintaining the mixed liquor in the intermediate basin under aerobic conditions while directing the mixed liquor effluent from the intermediate basin to the first outer basin and maintaining the first outer basin in a settling mode;c. in another phase of treatment, changing the conditions in the second outer basin to where the mixed liquor therein is maintained under aerobic conditions while the effluent from the second outer basin is directed to the intermediate basin and the effluent of the intermediate basin is directed to the first outer basin which remains in a settling mode; andd. in another phase of treatment, switching the wastewater influent from the second outer basin to the intermediate basin and maintaining the mixed liquor in the intermediate basin under aerobic conditions and transferring the mixed liquor effluent from the intermediate basin to at least one of the first or second outer basins while maintaining the first and second outer basins in a settling mode. 19. The process of claim 17 including increasing the concentration of mixed liquor suspended solids in the intermediate basin by transferring mixed liquor suspended solids from the first or second outer basins to the intermediate basin. 20. The process of claim 17 wherein the volume of the intermediate basin exceeds the volume of the first or second outer basins. 21. The process of claim 20 wherein the volume of the intermediate basin constitutes approximately 35% to 50% of the total volume of all three basins. 22. The process of claim 17 including transferring a portion of the mixed liquor suspended solids from one of the outer basins being maintained in a settling mode to the other outer basin being operated under anaerobic conditions.