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For extension of the decolorization period in a continuous process a sequencing batch reactor was used.
A specially designed tubular batch reactor was used for the externally heated atmospheric pressure pyrolysis.
A separate batch reactor was used to distinguish reactions involving biological phosphate removal from physicochemical reactions involving phosphate precipitation in order to establish the kinetics and stoichiometry of calcium phosphate formation.
Initially, the electrocatalytic hydrodechlorination of 2-chlorobiphenyl (2-ClBP) to biphenyl at a palladium-modified nickel foam (Pd/Ni) cathode in a batch reactor was used as a model reaction for a quantitative study of the influences of the operating parameters, including temperature, the initial concentrations of PCBs, current density and the amount of Pd loading, on the apparent reaction rate.
A large-scale (1.0 L) batch reactor was used so as to maximize the cellulose recovery from EFB by H2SO4 treatment at reaction temperatures between 121 and 190°C.
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The batch reactor is used in the pharmaceutical industry for the production of drugs, where a rapid and precise temperature control is necessary.
One case study involving a batch reactor is used to illustrate the ability of the combined tool to provide information on the detailed interactions between fluid mechanics, heat transfer, reaction and control strategy, and to provide insights on important design and operational decisions.
The initial 2-CP concentration of 200 mg L−1 and mineral salt medium with biomass concentration of 8.4 mg VSS L−1 in the batch reactor were used to evaluate 2-CP biodegradation.
Stainless steel batch reactors are used and the experiments are conducted from 333 to 373 K.
Experimental results, from a continuous-flow back-mixed reactor and from batch reactors, are used to show that polymer molecular weight distributions obtained in practice are consistent with predictions from the reaction scheme.
To optimize the performance of the system, two or more batch reactors are used in a predetermined sequence of operations.
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