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Process and apparatus for the separation of p-xylene in C.sub.8 aromatic hydrocarbons with a simulated moving bed adsorption and a crystallization

机译:通过模拟移动床吸附和结晶分离C.sub.8芳烃中对二甲苯的方法和设备

摘要

To continuously produce and separate high purity p-xylene from a C.sub. 8 aromatic hydrocarbon charge, successive use is made in combination of (1) a stage of separating low-purity p-xylene (75 to 98%) by simulated moving bed adsorption chromatography, with a ratio for the solvent to charge flow rates of 1.2 to 2.5; (2) a stage of purifying and washing the low-purity p-xylene by recrystallization (-25° to +10° C.); (3) a stage of catalytic isomerization of the charge which has been p- xylene-depleted by the separating stage (1); and recovering an isomerate which is then recycled to the charge. The solvent for desorption in stage (1) and washing in stage (2) is advantageously toluene.
机译:为了连续地从C.sub。生产和分离高纯度对二甲苯。 8种芳烃进料,连续使用是结合以下步骤进行的:(1)通过模拟移动床吸附色谱分离低纯度对二甲苯(75%至98%)的阶段,溶剂与进料的流量之比为1.2至2.5; (2)通过重结晶(-25℃至+ 10℃)纯化和洗涤低纯度对二甲苯的阶段; (3)通过分离步骤(1)已经耗尽了对二甲苯的装料的催化异构化步骤;并回收异构体,然后将其循环到装料中。在步骤(1)中解吸并在步骤(2)中洗涤的溶剂有利地是甲苯。

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