Process for producing high-octane, low-olefin motor fuels and motor fuel
components
    1.
    发明授权
    Process for producing high-octane, low-olefin motor fuels and motor fuel components 失效
    生产高分子,低油脂电动机燃料和电动机燃料成分的方法

    公开(公告)号:US5141525A

    公开(公告)日:1992-08-25

    申请号:US687269

    申请日:1991-04-18

    CPC分类号: C07C41/06 C10L1/023

    摘要: High-octane, low-olefin motor fuels and motor fuel components having a content of alkyl tert.-alkyl ethers can be produced by reacting a crude hydrocarbon stream, which contains tertiary C.sub.5 -C.sub.8 -olefins in addition to saturated and olefinically, diolefinically and acetylenically unsaturated hydrocarbons in the same boiling range, simultaneously with one or more C.sub.1 -C.sub.4 -alkanols in a quantity from 0.5 to 5 mol per mol of the tertiary olefin(s) and with excess hydrogen relative to the total unsaturation under a pressure from 12 to 80 bar and at a temperature from 60.degree. to 180.degree. C. on a catalyst known per se or a mixture of catalysts known per se, which effect(s) both the etherification and the olefin hydrogenation.

    摘要翻译: 具有烷基叔烷基醚含量的高辛烷值,低烯烃运动燃料和发动机燃料组分可以通过使含有叔C5-C8-烯烃的粗烃流除饱和和烯属二烯烃和 在相同沸点范围内的炔属不饱和烃,同时具有一种或多种相对于总不饱和度为0.5至5摩尔的每摩尔叔烯烃的一种或多种C 1 -C 4 - 链烷醇和在12压力下的总不饱和度 至80巴,温度为60℃至180℃的本身已知的催化剂或本身已知的催化剂的混合物,其同时进行醚化和烯烃氢化。

    Process for the hydrogenation of hydrocarbons
    3.
    发明授权
    Process for the hydrogenation of hydrocarbons 失效
    烃类氢化方法

    公开(公告)号:US4431528A

    公开(公告)日:1984-02-14

    申请号:US392035

    申请日:1982-06-25

    摘要: Unsaturated hydrocarbons and mixtures in which the latter are present are treated with anion exchangers prior to hydrogenation and are then hydrogenated catalytically in a known manner. The treatment with anion exchangers is carried out at 0.degree.-120.degree. C. and at a space velocity of 0.1 to 10 l of hydrocarbons to be hydrogenated per l of exchanger, per hour. The process avoids other, energy-intensive pretreatments, for example distillation of the hydrocarbons to be hydrogenated, or washing, and can be carried out in simple equipment. A considerable prolongation of the catalyst operating time is achieved in the subsequent catalytic hydrogenation.

    摘要翻译: 存在后者的不饱和烃和混合物在氢化之前用阴离子交换剂处理,然后以已知的方式氢化催化。 阴离子交换剂的处理在0℃-120℃下进行,空间速度为0.1至10升待每1个交换器每小时氢化的烃。 该方法避免了其他能量密度的预处理,例如蒸馏待氢化的烃或洗涤,并且可以在简单的设备中进行。 在随后的催化氢化中实现催化剂操作时间的显着延长。