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Scale up study of capillary microreactors in solvent-free semihydrogenation of 2‐methyl‐3‐butyn‐2‐ol

机译:在2-甲基-3-丁炔-2-醇的无溶剂半氢化反应中进行毛细管微反应器的放大研究

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摘要

A 2.5 wt.% Pd/ZnO catalytic coating has been deposited onto the inner wall of capillary reactors with a diameter of 0.53 and 1.6 mm. The coatings were characterised by XRD, SEM, TEM and elemental analysis. The performance of catalytic reactors was studied in solvent-free hydrogenation of 2-methyl-3-butyn-2-ol. No mass transfer limitations was observed in the reactor with a diameter of 0.53 mm up to a catalyst loading of 1.0 kg(Pd) m−3. The activity and selectivity of the catalysts has been studied in a batch reactor to develop a kinetic model. The kinetic model was combined with the reactor model to describe the obtained data in a wide range of reaction conditions. The model was applied to calculate the range of reaction conditions to reach a production rate of liquid product of 10–50 kg a day in a single catalytic capillary reactor.
机译:将2.5重量%的Pd / ZnO催化涂层沉积到直径为0.53和1.6mm的毛细管反应器的内壁上。通过XRD,SEM,TEM和元素分析对涂层进行表征。在2-甲基-3-丁炔-2-醇的无溶剂加氢中研究了催化反应器的性能。在直径为0.53 mm的反应器中直至催化剂负载为1.0 kg(Pd)m-3时,均未观察到传质限制。已经在间歇反应器中研究了催化剂的活性和选择性以建立动力学模型。将动力学模型与反应器模型相结合,以描述在广泛的反应条件下获得的数据。该模型用于计算反应条件的范围,以在单个催化毛细管反应器中达到每天10–50 kg的液体产品生产率。

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