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    • 105. 发明授权
    • Process for producing light olefins using reaction with distillation as
an intermediate step
    • 使用蒸馏反应生产轻质烯烃的方法作为中间步骤
    • US5817906A
    • 1998-10-06
    • US511332
    • 1995-08-10
    • Terry L. MarkerChristopher David Gosling
    • Terry L. MarkerChristopher David Gosling
    • C07C1/20C07C6/00
    • C07C1/20C07C2521/12C07C2529/08C07C2529/70C07C2529/84C07C2529/85C07C2531/08Y02P20/127
    • The present invention relates to a process for the production of light olefins comprising olefins having from 2 to 4 carbon atoms per molecule from a crude oxygenate feedstock. The crude oxygenate feedstock comprises an alcohol, and water. The process comprises passing the crude oxygenate feedstock to catalyst to a distillation with reaction zone to convert the alcohol to an ether and produce an ether product having a reduced water relative to the crude oxygenate feedstock and a first water stream. The ether product is passed to an oxygenate conversion zone containing a metal aluminosilicate catalyst to produce a light olefin stream. The use of crude oxygenate feedstock, having a high proportion of water, combined with a process for producing additional water in the conversion of the alcohol to an ether, actually reduces the amount of water contacted with the water sensitive, metal alumino-silicate catalyst in the oxygenate conversion zone which provides the advantage of extended catalyst life and greater catalyst stability in the oxygenate conversion zone.
    • 本发明涉及一种用于生产轻质烯烃的方法,其包含每分子含有2-4个碳原子的由粗含氧化合物原料生产的烯烃。 粗含氧化合物原料包括醇和水。 该方法包括将粗含氧化合物原料转移至催化剂至具有反应区的蒸馏以将醇转化为醚,并产生相对于粗含氧化合物原料和第一水流具有降低的水的醚产物。 将醚产物送至含有金属铝硅酸盐催化剂的含氧化合物转化区以产生轻质烯烃流。 使用具有高比例的水的粗含氧化合物原料与在醇转化为醚的过程中产生额外的水的方法相结合,实际上减少了与水敏感的金属铝硅酸盐催化剂接触的水的量 含氧化合物转化区,其提供延长的催化剂寿命和在含氧化合物转化区中更大的催化剂稳定性的优点。