Hi, we have a sludge blend tank which mixes primary and secondary wastewater sludge at about 5 & 3% dry solids respectively. Our mixer does not operate when the tank level is below 2m and as we run a drier, the lower we can get this level the more down time we can have to carry out maintenance or repair.
The blend tank feeds centrifuges, and after the mixer stops, the centrifuges play up due to the lack of mixing. We would like to pipe the two sludge feeds into one mixing manifold at the bottom of the tank and then use some sort of nozzle or venturi arrangement to get some agitation in the tank.
The tank diameter is 8m and sludge flow rates are about 10m3/h for each stream. Existing pipe work is 100mm diameter. Is there any rule of thumb we could use to determine a target tank entry velocity to provide adequate mixing? We would probably have two tank feed points so as to bypass the nozzle arrangement when the mixer is running to reduce head on the progressive cavity pumps.
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