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This work presents the development and characterisation of a multipurpose batch reactor with a variable heating/cooling structure for temperature control.
Under these conditions, over 84% of conversion was obtained after 4 h of reaction in a batch reactor, with a productivity of 0.27 mmol g−1 h−1 per gram of derivative.
One of the bioreactors was a batch reactor with a continuous magnetic stirring tank, and the other bioreactors were enclosed tubular bioreactors operating in semi-continuous mode with two cycles.
The results show that the reaction can be carried out twelve times faster in a CFI than in a batch reactor, with a conventional oil to methanol molar ratio of 1 6 (100% excess methanol).
Initial nitration rates of toluene have been measured at sulphuric acid strengths between 76 and 79percentnt in a stirred cell with pure toluene, and also in a stirred batch reactor with a dilute solution of toluene in an inert solvent.
Experiment was carried out in a batch reactor with a capacity of 500 mL (YEW SII SIE lab analytics supplies, Malaysia).
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An alumina supported molybdenum nitride catalyst (Mo2N/Al2O3) is examined for the ethanolysis of Kraft lignin in supercritical ethanol in a batch reactor with an initial nitrogen pressure of 0 MPa (gauge).
In this paper, a new modeling approach is proposed for adsorption kinetics investigation performed in batch reactors with a fluid solid system.
Here, we demonstrate that improving bioelectrochemical reactor design to a higher cathode surface to volume ratio results in an enhanced acetate titer; 5.7 ± 0.74 g L−1 (11.5 ± 6.6 g m−2 d−1) in galvanostastically controlled (−5 A m−2cathode) batch reactors with a mixed microbial community.
This paper describes an experimental investigation to determine the impact of pressurised reactor conditions within the reduction zone of a gasification process employing a semi-batch reactor with a bituminous coal.
The efficacy of the proposed framework is shown through two case studies: a batch reactor with Arrhenius-type reactions and a carbon dioxide adsorption system.
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