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    • 71. 发明申请
    • PROCESS FOR PRODUCING TRIPTANE
    • 生产TRIPTANE的方法
    • WO2009063177A1
    • 2009-05-22
    • PCT/GB2008/003772
    • 2008-11-07
    • BP P.L.C.DANIEL, Berian, JohnLAW, David, JohnMAUNDERS, Barry, MartinSUNLEY, John, GlennVAN DER WAAL, Jan, Cornelis
    • DANIEL, Berian, JohnLAW, David, JohnMAUNDERS, Barry, MartinSUNLEY, John, GlennVAN DER WAAL, Jan, Cornelis
    • C07C1/20C07C9/16C07C11/02B01J29/06
    • C07C29/151C07C1/20C07C2529/08C07C2529/12C07C2529/14C07C2529/16C07C2529/18C07C2529/40C07C2529/44C07C2529/46C07C2529/48C07C2529/70C07C2529/74C07C2529/76C07C2529/78Y02P20/52C07C9/16C07C11/02C07C31/04C07C31/08C07C31/10C07C31/12
    • A process for producing triptane and/or triptene from methanol and/or one or more derivatives thereof, and optionally one or more further alcohols and/or derivatives thereof at a temperature in the range of from 150 to 400 °C, in the presence of a zeolite catalyst having Brønsted acidity, in which all the carbon atoms in the triptane and/or triptene are derived from the methanol and/or one or more derivatives thereof and the optional further alcohols and/or derivatives thereof, the zeolite catalyst being selected from: i. zeolites having frameworks comprising silicon and aluminium atoms at a Si: Al mole ratio of greater than (2), which zeolites also have a channel structure comprising a ring size of (12) or more non-oxygen atoms in (2) or (3) dimensions; and ii. zeolites having frameworks comprising silicon and aluminium atoms, and which have a framework ring comprising (12) or more non-oxygen-atoms accessible on the external surface of the zeolite and a pore structure in which all of the channels have a ring-size of less than (12) non-oxygen atoms. There is also described a process for producing triptane and/or triptene wherein the zeolite catalyst is zeolite X, the reaction composition additionally comprises a C 3 alcohol and/or one or more derivatives thereof, in which the mole ratio of C 3 alcohol : methanol present in the reaction composition, or derivable from the one or more derivatives thereof present in the reaction composition, is greater than 0.23 : 10, and the temperature of the process is in the range of greater than 200° to 400 °C.
    • 在150-400℃的温度范围内,在甲醇和/或其一种或多种衍生物和任选的一种或多种其它醇和/或其衍生物的存在下,在 具有布朗斯台德酸性的沸石催化剂,其中所述三庚烷和/或三丁烯中的所有碳原子来自甲醇和/或其一种或多种衍生物和任选的其它醇和/或衍生物,所述沸石催化剂选自 : 一世。 具有Si:Al摩尔比大于(2)的硅和铝原子的骨架的沸石,该沸石还具有在(2)或(3)中具有包含(12)以上非氧原子的环尺寸的通道结构 )尺寸; 和ii。 具有包含硅和铝原子的框架的沸石,并且具有包含可在沸石的外表面上的(12)或更多个非氧原子的骨架环和其中所有通道的环状尺寸为 小于(12)个非氧原子。 还描述了一种制备三庚烷和/或三丁烯的方法,其中沸石催化剂是沸石X,反应组合物另外包含C3醇和/或其一种或多种衍生物,其中存在于C 3醇:甲醇中的摩尔比 反应组合物或衍生自反应组合物中的一种或多种衍生物的反应组合物大于0.23:10,并且该方法的温度在大于200-400℃的范围内。