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For the below schematic, the flow rates ( Q ) and biomass concentrations ( X ) are depicted for each reactor stream with appropriate superscripts.
For the below schematic, the flow rates Q and biomass concentrations X are depicted for each reactor stream with appropriate superscripts. By performing mass balances across appropriate control volumes, derive equations that describe the relationship between the concentration of biomass in the reactor and sludge settleability in the secondary clarifier. Clearly identify any assumptions.
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