Aeration Tanks



Once through the primary clarifiers the flow is sent to the aeration basins. These consist of twelve equal cells (21 feet by 21 feet by 20 feet) that are interconnected. The set up offers some options as to how the activated sludge process can be run. The feeds of both the Return Activated Sludge (RAS) (shown in the picture) and the primary effluent enter into the first two tanks. If they chose to run the activated sludge in a contact stabilization mode, they could just close the appropriate valves in each of the tanks. Thus one tank would be receiving only primary effluent and the other would be receiving only RAS. The dividing wall has a gate that can be opened to allow the sludge to pass from one tank to the other. At the time of the visit the plant was running the system in plug flow conditions, where each tank receives about half of the RAS and the primary effluent. The flow continues down through the other 10 tanks and finally out to the final clarifiers.

The aeration system is a fine bubble diffusion system and involves no mechanical aeration. Four blowers send air heated to about 120 degrees F to an air mixing manifold system in the aeration tank. The air is heated to increase the mixed liquor temperature to avoid possible freezing during the cold months of the year. The air enters through the top of the manifold while mixed liquor is pumped through the bottom. The air and mixed liquor mixture is then discharged through one of twelve jets thus creating a turbulent mixing action. The air loading is tapered with the first four tanks receiving 168 lbs/O2 per day and the last eight receiving only 64.7 lbs/O2 per day. The aeration unit was design to handle a maximum BOD5 loading of 3824 lbs/day.

Previously the plant had trouble with foaming sludge but it is believed that they were over correcting At the time there was more than one operator controlling the inlets to the aeration tanks, and due to differences in opinions, a consistent operating technique was never decided upon. One operator would set the air loading and RAS recycle rate and the other would change it to values that he thought were more appropriate. The tank was constantly being tampered with and as a result efficiency was far less than what is being achieved today.



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