Production of high-octane gasoline blending stock
    33.
    发明公开
    Production of high-octane gasoline blending stock 失效
    生产eine MischvorratsfürBenzin mit hoher Oktanzahl。

    公开(公告)号:EP0230356A1

    公开(公告)日:1987-07-29

    申请号:EP87300146.5

    申请日:1987-01-08

    IPC分类号: C10G35/095 C07C2/00

    CPC分类号: C10G35/065

    摘要: he process for preparing a high-octane gasoline involves catalyzing a light hydrocarbon containing one or more C 2 -C 7 paraffins and/or C 2 -C 7 olefins with a crystalline aluminogallosilicate with the skeleton comprised of SiO 4 , AlO 4 and GaO 4 tetrahedra at temperatures ranging from 350°C to 650°C under a hydrogen partial pressure of not higher than 5 kg/cm 2 . The crystalline aluminogallosilicate to be used as the catalyst for the process has its skeleton comprised of SiO 4 , AlO 4 and Ga0 4 tetrahedra and having the following formula:
    wherein M is a metal selected from an alkaline metal, and alkaline earth metal and a mixture thereof, n is the valence of said metal, a is a positive number of (b + 1) ± 3.0, b is between 0.3 and 30, c is between 8 and 2,000, and d is between 1 and 200.

    摘要翻译: 制备高辛烷值汽油的方法包括在350℃的温度范围内用含有SiO 4,AlO 4和GaO 4四面体的骨架催化含有一种或多种C 2 -C 7链烷烃和/或C 2 -C 7烯烃的轻质烃与结晶铝硅酸盐 C至650℃,氢分压不高于5kg / cm 2。 用作该方法的催化剂的结晶铝硅酸盐硅骨架的骨架由SiO4,AlO4和GaO4四面体组成,具有下列结构式:aM2 / nO.bAl2O3.Ga2O3.cSiO2.dH2O ...其中M是选自 碱金属和碱土金属及其混合物,n是所述金属的化合价,a是正数(b + 1)+/- 3.0,b在0.3和30之间,c在8和2,000之间,c d在1到200之间。

    Process for the production of aromatic hydrocarbons from aliphatic hydrocarbons
    37.
    发明公开
    Process for the production of aromatic hydrocarbons from aliphatic hydrocarbons 失效
    从二氧化碳生产芳香烃的方法

    公开(公告)号:EP0493040A3

    公开(公告)日:1992-08-12

    申请号:EP91311902.0

    申请日:1991-12-20

    IPC分类号: C10G35/06

    CPC分类号: C10G35/065 C10G50/00

    摘要: Aromatic hydrocarbons are produced by catalytic conversion of aliphatic hydrocarbons using an aluminogallosilicate catalyst. A feed of the aliphatic hydrocarbon is mixed with a recycle gas and the mixture is contacted with the catalyst. The resultant conversion product is separated into a gas phase and a liquid phase containing aromatic hydrocarbons. The gas phase is separated into a hydrogen-rich gas and a methane- and/or ethane-rich gas while the liquid phase is separated into an aromatic hydrocarbon-containing product and a light hydrocarbon-containing gas. At least part of the methane- and/or ethane-rich gas and the light hydrocarbon-containing gas is recycled as the above recycle gas. The catalytic conversion is performed while increasing the reaction temperature as the process proceeds.

    Process for preparing pyruvate
    40.
    发明公开
    Process for preparing pyruvate 失效
    Verfahren zur Herstellung von Pyruvat。

    公开(公告)号:EP0337246A1

    公开(公告)日:1989-10-18

    申请号:EP89105871.1

    申请日:1989-04-04

    IPC分类号: C07C59/19 C07C51/23

    CPC分类号: C07C51/235 C07C59/19

    摘要: A process for preparing pyruvate in high yield is disclosed, comprising reacting propylene glycol with molecular oxygen in an aqueous solution in the presence of a platinum catalyst containing a metallic component selected from the group consisting of lead, thallium, and cadmium while controlling the pH of the reaction mixture between 7 and 9. The crude pyruvate can be purified by treating with activated carbon in the presence of water.

    摘要翻译: 公开了一种以高产率制备丙酮酸盐的方法,包括在含有选自铅,铊和镉的金属组分的铂催化剂存在下,在水溶液中使丙二醇与分子氧反应,同时控制pH 反应混合物在7和9之间。粗制丙酮酸盐可以通过在水存在下用活性炭处理来纯化。