Production of high-octane, unleaded motor fuel
    2.
    发明授权
    Production of high-octane, unleaded motor fuel 失效
    生产高价,不合格的电机燃料

    公开(公告)号:US3787314A

    公开(公告)日:1974-01-22

    申请号:US3787314D

    申请日:1972-11-21

    CPC classification number: C10G61/06 C10G47/14 C10G59/02

    Abstract: A charge stock containing kerosene boiling range hydrocarbons is converted into a high-octane motor fuel which does not require the use of metal-containing additives otherwise needed for suitable anti-knock characteristics. The process involves a combination of hydrocracking and catalytic reforming, and is effected in a manner which significantly increases the quantity of normally liquid motor fuel product. The novel form of hydrocracking results in a product predominantly comprising naphthenic hydrocarbons and highly-branched paraffins, the latter being rich in isobutane. Following separation to recover the isobutane, catalytic reforming is utilized to dehydrogenate the naphthenic compounds, and dehydrocyclisize paraffinic hydrocarbons, to produce an aromatic concentrate.

    Abstract translation: 含有煤油沸点范围烃的电荷原料转化成高辛烷值的发动机燃料,其不需要使用除了合适的抗爆震特性所需的含金属添加剂。 该方法涉及加氢裂化和催化重整的组合,并且以显着增加常规液体马达燃料产品的量的方式实现。 加氢裂化的新形式导致主要包含环烷烃和高度支化的链烷烃的产物,后者富含异丁烷。 在分离回收异丁烷之后,使用催化重整使环烷烃化合物脱氢,并将石蜡烃脱氢环化,生成芳族浓缩物。

    Simultaneous production of aromatic hydrocarbons and isobutanes
    3.
    发明授权
    Simultaneous production of aromatic hydrocarbons and isobutanes 失效
    同时生产芳族碳氢化合物和ISOBUTANES

    公开(公告)号:US3756940A

    公开(公告)日:1973-09-04

    申请号:US3756940D

    申请日:1972-04-18

    Inventor: DONALDSON G

    CPC classification number: C10G61/06 C10G59/02 C10G69/08 C10L1/06

    Abstract: A NAPHTHA BOILING RANGE HYDROCARBON CHARGE STOCK IS CONVERTED INTO AROMATIC HYDROCARBONS AND AN ISOBUTANE CONCENTRATE VIA A COMBINATION PROCESS INVOLVING CATALYTIC REFORMING, SEPARATION AND HYDROCRACKING. THE CATALYTIC REFORMING IS EFFECTED IN TWO DISTINCT, INDIVIDUAL REFORMING REACTION ZONES, ONE OF WHICH OPERATES AT A RELATIVELY HIGH SEVERITY, AND THE SECOND OF WHICH OPERATES AT A RELATIVELY LOW SEVERITY. FOLLOWING SEPARATION OF AN AROMATIC CONCENTRATE, THE REMAINING SATURATED HYDROCARBONS ARE SUBJECTED TO A PARTICULAR HYDROCRACKING PROCESS WHICH RESULTS IN EXCEEDINGLY HIGH YIELDS OF ISOBUTANE.

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