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The results revealed that the CW-1 + UV/TiO2/O3 reactor batch configuration reduced COD and BOD5 by an average of 62.1% and 88.7%, respectively.
GPRs are studied using a batch configuration of the setup to allow an overall mass balance of the experiments.
But instead of using a semi-continuous configuration as used in SEDS process, the plant was utilized in a batch configuration.
The E. coli AQPZ was previously synthesized in a similar CF system using the batch configuration [41].
There was also no increase in conversion when a split batch configuration was used, with half the substrate and enzymes added 6 hours after the first half.
This leads to higher overall xylan recovery from flow-through reactor compared to batch configuration, because some in-situ xylose degradation occurs in batch reactor due to longer exposure to high temperatures.
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Besides studying the well known batch configurations (rectifier, stripper, middle vessel column) we also suggest two novel configurations such as double column batch rectifier (DCBR) and double column batch stripper (DCBS).
Fed-batch configuration produced dihydroxyacetone in quantities (2 5 fold) greater than batch culture (Liu et al. 2013b).
In the fed-batch configuration, a relatively high ethanol concentration, 51.2 g/L, corresponding to a 90% ethanol yield, was obtained despite some inhibition due to the slight accumulation of glucose during FWM feeding.
The experiments and analysis in this study were done in a batch reactor configuration.
Optimized batch photoreactor configuration (1.8 L) was used for degrading a 25 mg L−1 RR243 aqueous solution, achieving 90% decolorization in 45 min and 60% mineralization in 100 min.
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