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PROCESS FOR PREPARING HIGHLY PURE RAFFINATE II AND METHYL TERT-BUTYL ETHER
PROCESS FOR PREPARING HIGHLY PURE RAFFINATE II AND METHYL TERT-BUTYL ETHER
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机译:制备高纯提余液II和甲基叔丁基丁醚的方法
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ABSTRACTPROCESS FOR PREPARING HIGHLY PURE RAFFINATE II AND METHYL TERT-BUTYL ETHERThe invention relates to a process for preparing methyl tert-butyl ether (MTBE) and a virtually isobutene-free C[err]-hydrocarbon mixture by reaction of an isobutene-containing C[err]-hydrocarbon stream with methanol over an acid catalyst, wherein, in a first stage in one or more reactor(s), isobutene is reacted with methanol to equilibrium formation of MTBE and, in a second stage in a reactive distillation column, the remaining isobutene present in the mixture is reacted over an acid catalyst, where the reactive distillation column is operated in a pressure range from 3 to 15 bar abs. and in a temperature range in the reaction zone from 55[err]C to 75[err]C at a hydraulic loading in the catalytic packing of from 10% to 110% and a refluxratio of less than 1.The use of the virtually isobutene-free C[err]-hydrocarbon mixture and the MTBE prepared according to the invention.FIGURE 1
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机译:抽象制备高纯提余液II和甲基叔丁基丁醚的方法本发明涉及通过使含异丁烯的C [err]-烃物流与甲醇在酸催化剂上反应来制备甲基叔丁基醚(MTBE)和实际上不含异丁烯的C [err]-烃混合物的方法,其中,在一个或多个反应器中的第一阶段,使异丁烯与甲醇反应以平衡形成MTBE,在反应蒸馏塔的第二阶段中,混合物中剩余的异丁烯在酸性催化剂上反应,其中反应蒸馏塔在3至15 bar abs的压力范围内运行。在反应区中的温度范围为55°C至75°C,催化填料中的水力负荷为10%至110%,回流比率小于1。使用实际上不含异丁烯的C [err]-烃混合物和根据本发明制备的MTBE。图1
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