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    • 1. 发明申请
    • COMBINED PREPARATION OF AT LEAST BUTENE AND OCTENE FROM ETHENE
    • 从乙烯组合制备最小的泡沫和硬度
    • US20160207849A1
    • 2016-07-21
    • US15000837
    • 2016-01-19
    • Guido STOCHNIOLStephan PEITZDietrich MASCHMEYERHelene REEKERJoerg SCHALLENBERG
    • Guido STOCHNIOLStephan PEITZDietrich MASCHMEYERHelene REEKERJoerg SCHALLENBERG
    • C07C2/24
    • C07C2/24C07C2/10C07C7/04C07C2521/12C07C2523/755C07C11/08C07C11/107C07C11/02
    • A process for the combined preparation of at least butene and octene from ethane, proceeds by a) providing an inert solvent having a boiling point or boiling range below the boiling point of butene; b) providing a first feed mixture comprising at least the inert solvent and ethene dissolved therein; c) converting the first feed mixture in a first synthesis; d) in the first synthesis, oligomerizing at least a portion of the ethene present in the first feed mixture in the presence of a first heterogeneous catalyst and in the presence of the inert solvent to obtain a first reaction mixture comprising at least the inert solvent, butene, hexene and octene; e) working-up of the first reaction mixture and/or a substance stream based thereon into a low boiler fraction comprising the inert solvent, at least one C4-fraction comprising butenes, a C6-fraction comprising hexenes, a C8-fraction comprising octenes and into a C8+-fraction comprising hydrocarbons having more than eight carbon atoms; f) using at least a portion of the low boiler fraction for providing the first feed mixture; g) providing a second feed mixture comprising at least hexene and ethene dissolved in the hexene using at least a portion of the C6-fraction; h) converting the second feed mixture in a second synthesis, wherein the second synthesis is spatially separated from the first synthesis; i) in the second synthesis, reacting at least a portion of the ethene present in the second feed mixture with at least a portion of the hexene present in the second feed mixture in the presence of a second heterogeneous catalyst to obtain a second reaction mixture comprising at least octene; and k) joint working-up of the second reaction mixture with the first reaction mixture or with the substance stream based thereon.
    • 从乙烷中至少组合制备丁烯和辛烯的方法是:a)提供沸点或沸点低于丁烯沸点的惰性溶剂; b)提供至少包含溶解在其中的惰性溶剂和乙烯的第一进料混合物; c)在第一合成中转化第一进料混合物; d)在第一种合成中,在存在第一种非均相催化剂的情况下和在惰性溶剂存在下使存在于第一进料混合物中的至少一部分乙烯低聚,得到包含至少惰性溶剂的第一反应混合物, 丁烯,己烯和辛烯; e)将第一反应混合物和/或基于其的物质流加工到包含惰性溶剂的低沸点馏分中,至少一种包含丁烯的C 4馏分,包含己烯的C 6馏分,包含辛烯的C 8馏分 并进入包含具有多于8个碳原子的烃的C8 +分馏; f)使用低沸点馏分的至少一部分来提供第一进料混合物; g)使用C 6馏分的至少一部分提供包含至少己烯和溶解在己烯中的乙烯的第二进料混合物; h)在第二合成中转化所述第二进料混合物,其中所述第二合成在空间上与所述第一合成分离; i)在第二合成中,使第二进料混合物中存在的乙烯的至少一部分与存在于第二进料混合物中的至少一部分己烯存在于第二种非均相催化剂中,以获得第二反应混合物, 至少辛烯; 和k)第二反应混合物与第一反应混合物或其上的物质流的联合处理。
    • 6. 发明授权
    • Process for the production of acrylic acid
    • 丙烯酸生产工艺
    • US07294741B2
    • 2007-11-13
    • US10498852
    • 2002-12-13
    • Gunther BubJurgen MoslerDietrich MaschmeyerAndreas SabbaghRoland FornikaMatthias Peuckert
    • Gunther BubJurgen MoslerDietrich MaschmeyerAndreas SabbaghRoland FornikaMatthias Peuckert
    • C07C51/16
    • C07C51/252C07C57/04
    • The present invention relates to a process for the production of acrylic acid (AA) comprising the steps wherein: a) a 1st gas mixture comprising propylene, oxygen, an inert gas and steam is subjected to a 1st catalytic oxidation reaction stage thereby converting the propylene in the presence of a catalyst mainly into acrolein being contained in a 2nd gas mixture from said 1st catalytic oxidation reaction, b) said 2nd gas mixture from the 1st catalytic oxidation reaction stage is subjected to a 2nd catalytic oxidation reaction stage thereby converting the acrolein in the presence of a catalyst mainly into AA, being contained in a product gas, c) said product gas is subjected to a quench tower, wherein said AA is recovered as an aqueous solution comprising said AA being contained in the process water, wherein a process vent gas is obtained at the top of said quench tower, wherein, said 1st gas mixture has a steam/propylene ratio of >0.3 and
    • 本发明涉及一种生产丙烯酸(AA)的方法,包括以下步骤:a)将包含丙烯,氧气,惰性气体和蒸汽的第一气体混合物进行第一催化氧化反应阶段,由此将丙烯 在主催化剂存在下,由所述第一催化氧化反应产生的第二气体混合物中含有丙烯醛,b)将来自第一催化氧化反应阶段的所述第二气体混合物进行第二催化氧化反应阶段,由此将丙烯醛转化为 催化剂主要以AA形式存在于产物气体中,c)将所述产物气体进行骤冷塔,其中所述AA作为包含所述AA的水溶液被回收,所述水溶液包含在工艺用水中,其中过程 在所述骤冷塔的顶部获得排出气体,其中所述第一气体混合物具有> 0.3和<2的蒸汽/丙烯比,并且所述处理水的量为 s或等于从骤冷塔抽出的所述水溶液中的水量。