Method for supplying return activated sludge
A method of processing waste water to produce a filtrate is provided. The method includes the steps of: introducing untreated wastewater to an inlet zone of a bioreactor; introducing a concentrate of treated waste water with at least 10,000 mg/L of total suspended solids into the inlet zone of the bioreactor to form a biological active mixture; aerating the biological active mixture in an aeration zone of the bioreactor to produce treated waste water; filtering the treated waste water to produce a filtrate and the concentrate, wherein the filtrate created by the filtering has total suspended solids of less than 10 mg/L; transferring at least a portion of the concentrate to the inlet zone of the bioreactor; and transferring the filtrate external to the bioreactor as clean water.
1 . A method of processing wastewater to produce a filtrate comprising the following steps:
introducing untreated wastewater to an inlet zone of a bioreactor;
introducing a concentrate of treated wastewater into the inlet zone of the bioreactor to form a biological active mixture, the concentrate having at least 10,000 mg/L of total suspended solids;
aerating the biological active mixture in an aeration zone of the bioreactor to produce further treated wastewater;
filtering the further treated wastewater to produce a filtrate and produce a further concentrate, wherein the filtrate created by the filtering has total suspended solids of less than 10 mg/L and the further concentrate has total suspended solids of at least 10,000 mg/L, wherein the filtering is performed by a filter having a permeable substrate, and further comprising: fouling the permeable substrate to form a layer of deposited suspended solids from the further treated wastewater on the permeable substrate, removing at least a portion of the layer, and mixing the removed portion of the layer with at least a portion of the further treated wastewater to form the further concentrate with the at least 10,000 mg/L of total suspended solids;
transferring at least a portion of the further concentrate to the inlet zone of the bioreactor; and
transferring the filtrate external to the bioreactor as clean water.
2 . A method of processing wastewater to produce a filtrate comprising the following steps:
combining untreated wastewater and a concentrate of treated wastewater to form a biological active mixture, the concentrate having at least 10,000 mg/L of total suspended solids;
transferring the biological active mixture into an inlet zone of a bioreactor;
aerating the biological active mixture in an aeration zone of the bioreactor to produce further treated wastewater;
filtering the further treated wastewater to produce a filtrate and produce a further concentrate, wherein the filtrate created by the filtering has total suspended solids of less than 10 mg/L and the further concentrate has total suspended solids of at least 10,000 mg/L, wherein the filtering is performed by a filter having a permeable substrate, and further comprising: fouling the permeable substrate to form a layer of deposited suspended solids from the further treated wastewater on the permeable substrate, removing at least a portion of the layer, and mixing the removed portion of the layer with at least a portion of the further treated wastewater to form the further concentrate with the at least 10,000 mg/L of total suspended solids;
transferring at least a portion of the further concentrate to the inlet zone of the bioreactor; and
transferring the filtrate external to the bioreactor as clean water.
3 . The method of claim 1 , further comprising holding the biological active mixture in the inlet zone for a predetermined time to enable an anoxic process in an anoxic zone and/or a denitrification zone.
4 . The method of claim 1 , wherein a contactor mixes the untreated wastewater and the concentrate in the inlet zone, wherein the mixing is turbulent.
5 . The method of claim 1 , wherein the transferring at least a portion of the further concentrate step further comprises: pumping the further concentrate and/or maintaining a differential liquid head between a source of the further concentrate and the inlet zone.
6 . The method of claim 1 , further comprising:
monitoring the total suspended solids of the further concentrate; and
controlling the filtering of the further treated wastewater to maintain the further concentrate with at least 10,000 mg/L total suspended solids.
7 . The method of claim 1 , further comprising spraying at least a portion of the further treated wastewater at the permeable substrate to remove at least a portion of the layer of deposited suspended solids, and introducing gas bubbles from at least one gas feeder into the further treated wastewater,
wherein the filtering is performed by a filter comprising:
a liquid-permeable filtering element having a first face and a second face opposite of the first face, wherein at least an area of the first face of the liquid-permeable filtering element is subject to the further treated wastewater under pressure and a pressure across said area is greater than 0 and less than or equal to 5.9 kPa, wherein the further concentrate is accumulated on the first face of the liquid-permeable filtering element, and
at least one nozzle that directs at least one jet at the second face of the liquid-permeable filtering element, through the liquid-permeable filtering element, and towards the first face of the liquid-permeable filtering element to remove and/or aid in removal of the layer of deposited solids.
8 . The method of claim 1 , wherein a level of dissolved oxygen in the further concentrate is no more than 0.5 mg/L.
9 . The method of claim 1 , wherein a level of nitrate (NO 3 ) in the further concentrate is no more than 3 mg/L.
10 . The method of claim 2 , wherein the combining step further comprises actively mixing the untreated wastewater and the concentrate of treated wastewater with at least 10,000 mg/L of total suspended solids to form the biological active mixture.
11 . The method of claim 2 , wherein the combining step further comprises combining the untreated wastewater and the concentrate of treated wastewater with at least 10,000 mg/L of total suspended solids in a transfer pipe to form the biological active mixture.