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    • 8. 发明授权
    • Process for manufacturing alkanes by reacting other alkanes with methane
    • 通过使其他烷烃与甲烷反应制备烷烃的方法
    • US07378564B2
    • 2008-05-27
    • US10502845
    • 2003-01-22
    • Jean-Marie BassetChristophe CoperetRichard PardyDaravong SoulivongJohn Glenn SunleyJean Thivolle-Cazat
    • Jean-Marie BassetChristophe CoperetRichard PardyDaravong SoulivongJohn Glenn SunleyJean Thivolle-Cazat
    • C07C6/08
    • C07C6/10B01J21/08B01J31/121B01J37/0209C07C2531/12Y10S585/943
    • The present invention relates to a process for the manufacture of alkanes comprising a catalytic reaction resulting from contacting methane with at least one other starting alkane (I) in the presence of a metal compound (C) capable of catalysing a reaction for the splitting and/or recombination of a carbon-carbon bond and/or of a carbon-hydrogen bond and/or of a carbon-metal bond, which catalytic reaction results in the formation of at least one final alkane (II) having a number of carbon atoms equal to or greater than (2). In the process, the contacting operation is carried out under a methane partial pressure equal to or greater than 0.1 MPa, preferably in the range from 0.1 to 100 MPa. The metal compound (C) can be chosen from metal compounds supported on and dispersed over a solid support, metal compounds supported on and grafted to a solid support and non-supported metal compounds. Under these conditions, it was found that the yield of the catalytic reaction was improved, and that the catalytic stability and activity of the metal compound (C) over timer were greatly enhanced.
    • 本发明涉及一种制备烷烃的方法,其包括由甲烷与至少一种其它起始烷烃(I)在能够催化分解和/或反应的反应的金属化合物(C)存在下使甲烷接触而产生的催化反应, 或碳 - 碳键和/或碳 - 氢键和/或碳 - 金属键的重组,该催化反应导致至少一个具有多个碳原子的最终烷烃(II)的形成相等 至(2)以上。 在该过程中,接触操作在等于或大于0.1MPa,优选在0.1至100MPa范围内的甲烷分压下进行。 金属化合物(C)可以选自负载在固体载体上并分散在固体载体上的金属化合物,负载在和接枝到固体载体上的金属化合物和非负载的金属化合物。 在这些条件下,发现催化反应的产率提高,金属化合物(C)超过定时器的催化稳定性和活性大大提高。
    • 10. 发明授权
    • Process for converting methane into ethane
    • 将甲烷转化为乙烷的方法
    • US07473814B2
    • 2009-01-06
    • US10517212
    • 2003-06-04
    • Jean-Marie BassetPhilippe BresChristophe CoperetBarry Martin MaundersDaravong SoulivongMostafa TaoufikJean Thivolle-Cazat
    • Jean-Marie BassetPhilippe BresChristophe CoperetBarry Martin MaundersDaravong SoulivongMostafa TaoufikJean Thivolle-Cazat
    • C07C2/00
    • C07C2/76C07C2531/12Y10S585/943C07C9/06
    • The invention relates to a process for producing ethane comprising contacting methane with a metal catalyst selected from metal hydrides, metal organic compounds and mixtures thereof. It also relates to a process for the conversion of methane to carbon-containing products comprising contacting methane with a metal catalyst comprising at least one metal, Me, chosen from the lanthanides, the actinides and the metals from Groups 2 to 12 of the Periodic Table of the Elements, so as to produce ethane in a proportion of at least 65%, especially at least 98% or 99% by weight with respect to carbon-containing products formed in the process. The process can be a single-step process, preferably carried out under conditions involving a non-oxidative catalytic coupling of methane, in particular under operating conditions maintained substantially constant, preferably continuously, during the ethane production, e.g. at a temperature ranging from −30° C. to +80° C., preferably from 20° C. to 500° C., under a total absolute pressure ranging from 10−3 to 100 MPa, preferably from 0.1 to 50 MPa. The metal catalyst may be chosen from metal catalysts supported on and preferably grafted to a solid support. One of the main advantages of the present invention is to produce ethane with a very high selectivity.
    • 本发明涉及一种生产乙烷的方法,包括使甲烷与选自金属氢化物,金属有机化合物及其混合物的金属催化剂接触。 它还涉及将甲烷转化为含碳产物的方法,包括使甲烷与包含至少一种金属的金属催化剂接触,所述金属催化剂选自镧系元素,锕系元素和元素周期表第2至12族中的金属 的元素,以便相对于在该方法中形成的含碳产品,以至少65重量%,特别是至少98重量%或99重量%的比例制备乙烷。 该方法可以是单步骤方法,优选在涉及甲烷的非氧化催化偶合的条件下进行,特别是在乙烷生产期间,优选连续保持基本上恒定的操作条件下,例如乙烷生产。 在-30℃至+ 80℃,优选20℃至500℃的温度下,在绝对压力范围为10-3-100MPa,优选0.1-50MPa的温度下进行。 金属催化剂可以选自负载在并优选接枝到固体载体上的金属催化剂。 本发明的主要优点之一是以非常高的选择性生产乙烷。