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METHOD OF PREPARING HIGH-OCTANE ADDITIVE TO PETROL, CONTAINING ETHYL-TERT-BUTYL ETHER (ETBE)

机译:含乙基叔丁基-丁基醚(ETBE)的高脂肪汽油添加剂的制备方法

摘要

FIELD: chemistry.;SUBSTANCE: invention relates to preparation of high-octane oxygen-containing petrol components. Described is a high-octane additive which contains ethyl-tert-butyl ether obtained through chemical contact of isobutene-containing hydrocarbon mixtures and ethanol with acidic ionite catalyst(s) at temperature of (30-100)°C, pressure (0.5-2.0) MPa, bulk speed of feeding material of (3.5-10.0) h-1 and molar ratio of ethanol, supplied and recycled, to isobutene equal to (0.95-1.1): 1.0. The reaction is carried out in one or two direct flow zones with subsequent separation of unreacted C4 hydrocarbons in the rectification zone and output of the end product from the bottom of the rectification zone. The lateral stream is extracted from the rectification zone in amount of (5.0-15.0) % above the inlet point of the reaction mass and directed to direct reaction zone which is first on the path (or the only one).;EFFECT: simplification of the process, increased efficiency of the apparatus and obtaining concentrated 99,0% ethyl-tert-butyl ether.;5 cl, 7 ex, 1 tbl, 2 dwg
机译:技术领域本发明涉及高辛烷值含氧汽油组分的制备。描述了一种高辛烷值添加剂,其中包含乙基叔丁基醚,该乙基叔丁基醚是通过在温度(30-100)℃,压力(0.5-2.0)下将含异丁烯的烃混合物和乙醇与酸性离子矿催化剂化学接触而获得的MPa,供料和循环的异丁烯供料的循环速度为(3.5-10.0)h -1 的乙醇的摩尔比等于(0.95-1.1):1.0。反应在一个或两个直流区中进行,随后在精馏区中分离出未反应的C 4 烃,并从精馏区底部输出最终产物。从反应区入口点上方(5.0-15.0)%的量从精馏区中提取侧向物流,并将其引导至直接在反应路径(或唯一的路径)上直接反应的区域。该过程提高了设备​​的效率并获得了浓缩的99,0%乙基叔丁基醚。; 5 cl,7 ex,1 tbl,2 dwg

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