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Endurance Tests and Kinetic Experiment in a Plug-Flow Reactor with a Fixed Catalyst Bed

机译:具有固定催化剂床的塞流反应器的耐久性试验和动力学实验

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摘要

As an example of the liquid-phase hydrogenation of methyl-phenol ketone to 1-phenylethanol, variants of the construction of a pilot reactor are considered for performing long-term tests of heterogeneous catalysts of a fixed bed. Calculations for the reactor unit during hydrogenation on NTK-11 are presented as an example. It is shown that a cascade of three adiabatic reactors with a catalyst bed height of 4.5 m each is needed to ensure a residual reactant concentration below 1 wt %.
机译:作为甲基苯酚酮液相加氢成1-苯基乙醇的一个例子,考虑了中试反应器构造的变体,以进行固定床非均相催化剂的长期测试。以NTK-11氢化过程中反应器单元的计算为例。结果表明,需要三个级联的绝热反应器,每个催化剂床的高度为4.5 m,以确保残留的反应物浓度低于1 wt%。

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