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Isomers of raw feed streams comprising paraffinic and cyclic hydrocarbons and double functional processes for ring opening

机译:包含链烷烃和环状烃的原料进料流的异构体以及开环的双功能过程

摘要

A C4-C6 feed containing low octane paraffins and substantial amounts of cyclic hydrocarbons in contacted with hydrogen and a high chloride, platinum alumina catalyst under conditions selected simultaneously to open cyclic hydrocarbon rings and isomerize paraffins to more highly branched paraffins in order to produce a high octane product stream which has a relatively low cyclic content. The process is operated at relatively low severity conditions that provide favourable equilibrium conditions for isoparaffin conversion, comprising a temperature of 40 to 260 DEG C (105 to 500 DEG F), a pressure of 7 to 70 barsg (0.8 to 7.1 MPa) and a space velocity of 0.5 to 12 hr-1, while maintaining a chloride concentration in the feed stream of 30 to 300 wt ppm. The ring opening is also obtained without excessive generation of light hydrocarbons. Multiple stage reaction zones may be used to operate the first stage at slightly higher severity (higher temperature) than the second stage to maximize ring opening and obtain favourable equilibrium of iso- to normal -paraffins.
机译:一种C4-C6进料,其中含有低辛烷值链烷烃和大量环烃,在与氢和高氯化物,铂氧化铝催化剂接触的条件下,同时打开环烃环并将链烷烃异构化为更高支链的链烷烃,以生产高价的链烷烃。具有相对低的循环含量的辛烷产物流。该方法在相对较低的苛刻条件下运行,可为异链烷烃转化提供有利的平衡条件,温度为40至260℃(105至500 F),压力为7至70 barg(0.8至7.1 MPa),空速为0.5至12hr-1,同时将进料流中的氯化物浓度保持在30至300 wt ppm。在没有过量生成轻烃的情况下也获得了开环。多级反应区可用于以比第二级稍高的强度(更高的温度)操作第一级,以最大化开环并获得异链烷烃与正链烷烃的有利平衡。

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