Abstract:In the fine chemical industry, exothermic liquid−liquid reactions are commonly carried out in semibatch reactors (SBRs). It has been an essential issue to design thermally safe and productive operations for isoperibolic liquid−liquid SBRs. Because it is time-consuming and money-consuming to determinate accurate kinetic parameters, a kinetic-parameter-free approach for this issue is highly desired. In this work, we find that once MTSR in the isothermal liquid− liquid SBRs increase with the increase in the react… Show more
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