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Process for the preparation of highly pure raffinate II and methyl tert-butyl ether

机译:制备高纯萃余液II和甲基叔丁基醚的方法

摘要

An isobutene-free methyl-tert-butylether and a 4C hydrocarbon mixture are prepared by reaction of an isobutene containing 4C hydrocarbon stream with methanol in the presence of an acid catalyst by a two step process in which the second step comprises reaction of residual isobutene at an acid ion exchange resin in a reactive distillation column using a recycle ratio of less than 1. Production of methyl-tert-butylether (MTBE) and a 4C hydrocarbon mixture essentially free of isobutene by reaction of an isobutene containing 4C hydrocarbon stream with methanol in the presence of an acid catalyst comprises as a first step reaction, in at least one reactor, of isobutene with methanol to a state of equilibrium and, in a second step, reaction of the residual isobutene in the mixture at an acid ion exchange resin in a reactive distillation column whereby the reactive distillation column is operated at 3-15 bara and 55-75 degrees C using a recycle ratio of less than 1.
机译:不含异丁烯的甲基叔丁基醚和4C烃混合物是通过在酸催化剂存在下,通过含4C烃物流的异丁烯与甲醇通过两步法反应制得的,其中第二步包括将残留的异丁烯在在反应蒸馏塔中使用小于1的循环比的酸性离子交换树脂。通过使含4C烃流的异丁烯与甲醇在甲醇中反应,制得甲基叔丁基醚(MTBE)和基本不含异丁烯的4C烃混合物。酸催化剂的存在包括第一步,在至少一个反应器中,异丁烯与甲醇的反应达到平衡状态,第二步,混合物中的残留异丁烯在酸性离子交换树脂上的反应。反应蒸馏塔,其中反应蒸馏塔在3-15 bara和55-75摄氏度下以小于1的循环比运行

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