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After day 232 (Run IV), the reactor was operated under constant operational conditions with no further changes in the influent flow rate or influent nitrogen concentration.
Before starting the continuous operation, the reactor was operated in batch mode with CD medium in order to increase biomass concentration.
One reactor was operated without alkalinity addition.
The reactor was operated at two different MLSS range.
The reactor was operated in both batch and semicontinuous modes.
A batch reactor was operated and hydroxybutyrate homopolymer was obtained.
On average, the MIT reactor was operated 112 hours per week at its design power level of 5 MW.
In this work, a methanol steam reforming (MSR) reactor was operated using an indirect heating method.
The vertically moving biofilm reactor was operated as a sequencing batch biofilm reactor (VMSBBR).
The reactor was operated in batch and the composition of its contents was determined periodically.
In the second stage, the reactor was operated at oxygen concentrations of 0.6, 0.4 and 0.2 mg/L.
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