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updating of natural gas liquid by catalyzed alkylation of ionic liquid

机译:离子液体的催化烷基化反应更新天然气液体

摘要

we provide a process that comprises: a. dehydrogenating the natural gas liquid to produce a mixture comprising unconverted olefins and paraffins; B. without further purification or modification, send the mixture to a single alkylation reactor; and c. alkylating olefins with an isoparaffin, using an ionic liquid catalyst, to produce one or more alkylated products. we also provide an integrated process unit to carry out the process, comprising: a. a dehydrogenation reactor; B. a single alkylation reactor; ç. a separator, following the alkylation reactor, which separates the effluent from the alkylation reactor in a catalyst phase and a hydrocarbon phase; d. a distillation unit, following the separator, which receives the hydrocarbon phase and separates it into alkylated products, an unreacted paraffin phase and an isoparaffin phase; and. a first recycling line that feeds the unreacted paraffin phase to the dehydrogenation reactor; and f. a second recycling line that feeds the isoparaffin phase in the alkylation reactor.
机译:我们提供的流程包括:使天然气液体脱氢以产生包含未转化的烯烃和链烷烃的混合物; B.未经进一步纯化或修饰,将混合物送入单个烷基化反应器;和c。使用离子液体催化剂,用异链烷烃将烯烃烷基化,以生产一种或多种烷基化产物。我们还提供了执行该过程的集成过程单元,包括:脱氢反应器; B.单烷基化反应器; C。在烷基化反应器之后的分离器,其将来自烷基化反应器的流出物在催化剂相和烃相中分离; d。在分离器之后的蒸馏单元,其接收烃相并将其分离成烷基化产物,未反应的石蜡相和异链烷烃相;和。将未反应的石蜡相进料到脱氢反应器的第一回收线;和f。第二个循环管线将异链烷烃相供入烷基化反应器中。

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