Supported Catalyst Comprising Delta- Or Theta-Modified Aluminium Oxide Supports
    3.
    发明申请
    Supported Catalyst Comprising Delta- Or Theta-Modified Aluminium Oxide Supports 审中-公开
    负载型催化剂包括三角形或者改性氧化铝载体

    公开(公告)号:US20080045766A1

    公开(公告)日:2008-02-21

    申请号:US10590979

    申请日:2005-02-24

    摘要: Process for producing a supported catalyst which comprises at least 75% by weight of Al2O3, whose proportion of Al2O3 in the delta or theta modification is, based on the proportion of Al2O3, at least 1% and which comprises a rhenium compound and, if appropriate, a promoter as active component (A), which comprises a) converting a customary support (S) which comprises at least 75% by weight of Al2O3 and to which a promoter may, if appropriate, have been applied is converted into a modified support (S) whose proportion of Al2O3 in the delta or theta modification is, based on the proportion of Al2O3, at least 1% by calcining the customary support (S) at a temperature of from 750 to 1100°C., b) producing a supported catalyst precursor from the modified support (S) by applying the active component (A) comprising the rhenium compound to the modified support (S) and c) calcining the supported catalyst precursor at a temperature of from 500 to 750° C.

    摘要翻译: 负载催化剂的制备方法,其包含至少75重量%的Al 2 O 3 O 3,其比例为Al 2 O 3 O 3, δ或θ改性中的3 N是基于Al 2 O 3 3 3%至少1%的比例,并且其包含铼化合物,如果 合适的作为活性组分(A)的促进剂,其包括a)转化常规载体(S),其包含至少75重量%的Al 2 O 3 3和 如果合适的话,启动子可以被施加到其上,转化成其在δ或θ改性中的Al 2 O 3 O 3比例为的改性载体(S) 基于Al 2 O 3 3 3%的比例,通过在750至1100℃的温度下煅烧常规载体(S)至少1%,b) 通过将包含铼化合物的活性组分(A)施加到改性载体(S)上,由改性载体(S)制备负载型催化剂前体, 和c)在500-750℃的温度下煅烧负载的催化剂前体

    Method For Producing Propene From 2-Butene And Isobutene-Rich Feeding Flows
    10.
    发明申请
    Method For Producing Propene From 2-Butene And Isobutene-Rich Feeding Flows 审中-公开
    从2-丁烯和异丁烯丰富的进料流中生产丙烯的方法

    公开(公告)号:US20080200745A1

    公开(公告)日:2008-08-21

    申请号:US11817250

    申请日:2006-02-24

    IPC分类号: C07C2/00

    摘要: Process for preparing a stream consisting essentially of ethene (stream C2=), a stream consisting essentially of propene (stream C3=), a stream consisting essentially of isobutene and possibly other olefins having 4 carbon atoms (stream C4=) and a stream consisting essentially of 2-methyl-2-butene and possibly 2-butene (stream C5=), and, if appropriate, a stream which comprises other hydrocarbons (stream Cx) and may consist of a plurality of separate substreams, which comprises a metathesis step in which a C4-hydrocarbon stream comprising at least 15% by weight of 2-butenes, at least 5% by weight of isobutene and not more than 5% by weight of 1-butene (feed stream) is brought into contact with ethene in the presence of a customary metathesis catalyst and the resulting hydrocarbon stream is fractionated to give the streams C2=, C3=, C4= and, if appropriate, Cx and all or part of the stream C5= is recirculated to the metathesis step.

    摘要翻译: 用于制备基本上由乙烯(料流C 2 H 2)组成的料流的方法,基本上由丙烯(料流C 3 H 3) =基本上由异丁烯和可能的具有4个碳原子的其它烯烃(流C 4 H 4)组成的料流)和基本上由2-甲基 -2-丁烯和可能的2-丁烯(流C 5 H 5),以及如果合适的话,包含其它烃(流C 1 H 2 O) SUB>),并且可以由多个单独的子流组成,其包括复分解步骤,其中包含至少15重量%的2-丁烯的C 4 - 烃烃流,至少5%的 在常规复分解催化剂的存在下,异丁烯的重量和不超过5%(重量)的1-丁烯(进料流)与乙烯接触,并将所得烃流分馏,得到料流C 2, / SUB> = ,C 3 = 并且如果合适的话,C> x>和全部或部分流C< 5>< / SUP>再循环到复分解步骤。