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Synthesis of Linear Alkylbenzene in a Novel Liquid-Solid Circulating Moving Bed Reactor

机译:新型液固循环移动床反应器中直链烷基苯的合成

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摘要

For the alkylation of benzene with long-chain olefins, using Hβ zeolite catalyst as replacement of HF or AlCl_3 has the advantages of no corrosion, less environmental pollution, and much more 2-phenyl isomer, which has the highest biodegradability and solubility, and better detergent properties among the related isomers. The characterization of the coke shows that the deactivation of catalyst is caused by the jam of bulkier molecules, such as naphthalene, indane and linear alkylbenzenes, which are too big to move quickly in the intracrystalline pores of catalyst. The deactivated catalyst can be regenerated by benzene washing at higher temperature. To make the processes of reaction and regeneration continuous, a novel moving bed reactor is developed. Comparing with the processes with fixed bed reactors, the processes in this work have the advantages of continuous operation, low temperature, low pressure, low mole ratio of benzene to olefins, and high weight hourly space velocity.
机译:对于长链烯烃与苯的烷基化反应,使用Hβ沸石催化剂代替HF或AlCl_3具有无腐蚀,对环境的污染小,2-苯基异构体多的优点,具有最高的生物降解性和溶解性,并且效果更好。相关异构体中的洗涤剂特性。焦炭的特征表明,催化剂的失活是由体积较大的分子(如萘,茚满和线性烷基苯)的堵塞引起的,这些分子太大而无法在催化剂的晶内孔中快速移动。失活的催化剂可以通过在较高温度下的苯洗涤来再生。为了使反应和再生过程连续进行,开发了新型的移动床反应器。与固定床反应器的方法相比,这项工作的方法具有连续运行,低温,低压,苯与烯烃的摩尔比低以及每小时空速高的优点。

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