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A batch reactor was operated and hydroxybutyrate homopolymer was obtained.
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The batch reactors were operated under an optimized condition of the inoculum to substrate ratio of 14%, initial pH value of 4.3 and the experimental temperature of 35 °C.
Lab- and pilot-scale simultaneous nitrification, denitrification and phosphorus removal-sequencing batch reactors were operated under cyclic anaerobic and micro-aerobic conditions.
The batch reactors were operated under an optimized condition of the respective glucose, Fe2+ and Mg2+ concentration of 14.5 g/L, 180 mg/L and 690 mg/L, the initial pH of 6.0 and experimental temperature of 35 ± 1 oC.
Before starting the continuous operation, the reactor was operated in batch mode with CD medium in order to increase biomass concentration.
For the batch investigations of the catalyst's selectivity for GPRs, the reactor was operated in batch mode.
It would represent the level of solid that would be present if the entire solid were added initially and the reactor was operated in batch mode to enable comparison of fed-batch performance with the batch reactor performance on an equivalent basis.
The reactor was operated batch-wise with respect to the liquid phase but continuous with respect to the gas phase.
The reactor was operated in batch mode fermentation; yeast physiology and mass transfer behavior in packed bed reactor were monitored in close relation to parameters such as glucose concentration, medium flow rate and different support materials like alginate beads with and without chitosan coating.
The reactor was operated in batch and the composition of its contents was determined periodically.
The enzymatic reactions were carried out at the following conditions: initial sucrose concentration 70% (w/v), pH 5.5, 60 °C, 350 rpm, and superficial aeration rate 0.012 m s−1; the reactor was operated in batch for 26 h.
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