CATALYST COMPOSITION AND PROCESSES THEREFOR AND THEREWITH
    2.
    发明申请
    CATALYST COMPOSITION AND PROCESSES THEREFOR AND THEREWITH 失效
    催化剂组合物及其过程及其应用

    公开(公告)号:US20020016258A1

    公开(公告)日:2002-02-07

    申请号:US09255973

    申请日:1999-02-23

    摘要: A catalyst composition and a process for hydrodealkylating a C9null aromatic compound such as, for example, 1,2,4-trimethylbenzene to a C6 to C8 aromatic hydrocarbon such as a xylene are disclosed. The composition comprises an alumina, a metal oxide, and a coke suppressor selected from the group consisting of silicon oxides, phosphorus oxides, boron oxides, magnesium oxides, tin oxides, titanium oxides, zirconium oxides, molybdenum oxides, germanium oxides, indium oxides, lanthanum oxides, cesium oxides, and combinations of any two or more thereof. The process comprises contacting a fluid which comprises a C9null aromatic compound with the catalyst composition under a condition sufficient to effect the conversion of a C9null aromatic compound to a C6 to C8 aromatic hydrocarbon.

    摘要翻译: 公开了一种催化剂组合物和将C 9+芳族化合物例如1,2,4-三甲基苯加氢脱烷基化成C6-C8芳族烃如二甲苯的方法。 该组合物包含氧化铝,金属氧化物和选自氧化硅,氧化磷,氧化硼,氧化镁,氧化锡,氧化钛,氧化锆,氧化钼,氧化锗,氧化铟, 氧化镧,氧化铯及其任意两种以上的组合。 该方法包括在足以使C 9+芳族化合物转化为C 6至C 8芳族烃的条件下使包含C 9+芳族化合物的流体与催化剂组合物接触。

    Process for producing aromatic hydrocarbon compounds and liquefied petroleum gas from hydrocarbon feedstock
    3.
    发明申请
    Process for producing aromatic hydrocarbon compounds and liquefied petroleum gas from hydrocarbon feedstock 失效
    从烃原料生产芳烃化合物和液化石油气的方法

    公开(公告)号:US20020092797A1

    公开(公告)日:2002-07-18

    申请号:US09989624

    申请日:2001-11-20

    IPC分类号: C10G035/085 C07C004/12

    摘要: Disclosed are a process for producing aromatic hydrocarbon compounds and liquefied petroleum gas (LPG) from a hydrocarbon feedstock having boiling points of 30-250null C. and a catalyst useful therefor. In the presence of said catalyst, aromatic components in the hydrocarbon feedstock are converted to BTX-enriched components of liquid phase through hydrodealkylation and/or transalkylation, and non-aromatic components are converted to LPG-enriched gaseous materials through hydrocracking. The products of liquid phase may be separated as benzene, toluene, xylene, and C9 or higher aromatic compounds, respectively according to their different boiling points, while LPG is separated from the gaseous products, in a distillation tower.

    摘要翻译: 公开了一种由沸点为30-250℃的烃原料生产芳族烃化合物和液化石油气(LPG)的方法和一种可用于此的催化剂。 在所述催化剂的存在下,烃原料中的芳族组分通过加氢脱烷基化和/或烷基转移转化为液相的富含BTX的组分,非芳族组分通过加氢裂化转化为富含LPG的气态物质。 在蒸馏塔中,液相的产物可以根据沸点不同而分离成苯,甲苯,二甲苯和C9或更高级的芳族化合物,同时将LPG与气态产物分离。

    Method for producing hydrocarbons having a modified carbon skeleton
    4.
    发明申请
    Method for producing hydrocarbons having a modified carbon skeleton 失效
    具有改性碳骨架的烃的制造方法

    公开(公告)号:US20040059169A1

    公开(公告)日:2004-03-25

    申请号:US10451739

    申请日:2003-06-25

    CPC分类号: C07C6/10 C07C6/08 C07C2531/12

    摘要: The invention relates to a method for producing hydrocarbons having a modified carbon skeleton by reacting aliphatic hydrocarbons a) with themselves, b) with another aliphatic hydrocarbon or c) with aromatic alkyl substituted hydrocarbons, in the presence of a metal organic catalyst or the hybrid thereof, at a temperature of between 20-400null C. and a pressure of between 0.2-100 bars, wherein the reaction takes place in the presence of hydrogen.

    摘要翻译: 本发明涉及一种生产具有改性碳骨架的碳氢化合物的方法,该方法通过使脂族烃a)与其自身反应,b)与另一种脂族烃或c)与芳族烷基取代的烃在金属有机催化剂或其混合物存在下反应 在20-400℃的温度和0.2-100巴的压力之间,其中反应在氢的存在下进行。