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    METHOD FOR PRODUCING PROPENE FROM PROPANE
    5.
    发明申请
    METHOD FOR PRODUCING PROPENE FROM PROPANE 审中-公开
    用于生产丙烯丙烷

    公开(公告)号：WO2006094938A3

    公开(公告)日：2006-11-02

    申请号：PCT/EP2006060436

    申请日：2006-03-03

    Applicant: BASF AG ,  CRONE SVEN ,  MACHHAMMER OTTO ,  SCHINDLER GOETZ-PETER ,  BORGMEIER FRIEDER

    Inventor： CRONE SVEN ,  MACHHAMMER OTTO ,  SCHINDLER GOETZ-PETER ,  BORGMEIER FRIEDER

    IPC: C07C5/48 ,  C07C11/06

    CPC classification number: C07C5/327 ,  C07C5/48 ,  C07C11/06

    Abstract: The invention concerns a method for producing propene from propane, said method consisting in: A) preparing an input gas stream (a) containing propane; B) introducing the input gas stream (a), containing propane, optionally water vapour and optionally an oxygen-containing gas stream, into a dehydrogenation zone then dehydrogenating propane to form propene, a product gas stream (b), containing propane, propene, methane, ethane, ethene, nitrogen, carbon monoxide, carbon dioxide, water vapour, optionally hydrogen and optionally oxygen, being obtained; C) cooling and optionally compressing the product gas stream (b) then separating water vapour by condensing a product gas stream (c) depleted in water vapour (c) being obtained; D) separating the non-condensable gas constituents or with low boiling point by contacting the product gas stream (c) with an inert absorbent then by desorbing the gases dissolved in said inert absorbent, a C 3 hydrocarbon stream (d1) and a residual gas stream (d2) containing methane, ethane, ethene, nitrogen, carbon monoxide, carbon dioxide, optionally hydrogen and optionally oxygen, being obtained; E) cooling and optionally compressing the C 3 hydrocarbon stream (d1), a gaseous or liquid C 3 hydrocarbon stream (e1) being obtained; F) optionally introducing the C 3 hydrocarbon stream (e1) into a first distillation zone then separating same by distillation into a propane and propene stream (f1) and a stream (f2) containing ethane and ethene; G) introducing the stream (e1) or (f1) into a (second) distillation zone then separating by distillation into a propene stream (g1) and a propane stream (g2), the stream (g2) being recycled at least partly to the dehydrogenation zone.

    Abstract translation: 本发明涉及一种方法，用于从丙烷制备丙烯的方法，包括以下步骤：提供一种含丙烷的原料气流的A）; B）包含（a），任选的蒸汽和任选的含氧气体流中的丙烷进料气流被送入脱氢区和丙烷经受脱氢成丙烯，得到产物气流（b）包含丙烷，丙烯，甲烷，乙烷，乙烯，氮气， 一氧化碳，二氧化碳，水蒸汽，任选的氢气和任选的氧获得; C）的产物气流（B）被冷却，冷凝，任选地，这将允许水蒸气通过冷凝分离，得到一个蒸汽贫化产物气流（获得的C）; D）不可冷凝的或低沸点的气体成分是通过产物气体流（c）与的溶解在惰性吸收介质气体的惰性吸收剂和随后解吸分离，由此一个C 3 烃流（d1）和一个接触制备 废气流的含甲烷，乙烷，乙烯，氮气，一氧化碳，二氧化碳，任选的氢气和任选的氧（D2）得到; E）与c 3 烃流（D1）被冷却和任选地被压缩，其特征在于，气态或液C 3 得到烃流（E1）; F）的C 3 烃流（E1）任选地进料至丙烷和丙烯以及包含乙烷和乙烯流（F2）中的第一蒸馏区和蒸馏（在流F1）; 电源（E1）或（F1）的G）被供给到蒸馏区中的（第二）和蒸馏分离成从丙烷中分离丙烯的产物料流（GL）和流（G2），所述电流（G2）至少部分地在 脱氢区返回。

    METHOD FOR THE SYNTHESIS OF AROMATIC HYDROCARBONS FROM C1-C4 ALKANES, AND UTILIZATION OF A C1-C4 ALKANE-CONTAINING PRODUCT FLOW
    8.
    发明申请
    METHOD FOR THE SYNTHESIS OF AROMATIC HYDROCARBONS FROM C1-C4 ALKANES, AND UTILIZATION OF A C1-C4 ALKANE-CONTAINING PRODUCT FLOW 审中-公开
    METHOD FOR芳香族烃的选自C1-C4烷烃合成及处置C1-C4的烷将含有产物的流动的

    公开(公告)号：WO2007048853A2

    公开(公告)日：2007-05-03

    申请号：PCT/EP2006067938

    申请日：2006-10-30

    Applicant: BASF AG ,  KIESSLICH FRANK ,  CRONE SVEN ,  MACHHAMMER OTTO ,  VAN LAAR FREDERIK ,  SCHWAB EKKEHARD ,  SCHINDLER GOETZ-PETER

    Inventor： KIESSLICH FRANK ,  CRONE SVEN ,  MACHHAMMER OTTO ,  VAN LAAR FREDERIK ,  SCHWAB EKKEHARD ,  SCHINDLER GOETZ-PETER

    IPC: C07C2/84 ,  C07C15/00

    CPC classification number: B01J29/46 ,  C01B3/50 ,  C01B2203/048 ,  C01B2203/0495 ,  C01C3/0212 ,  C07C2/84 ,  C07C2529/06 ,  C07C2529/48 ,  Y02P20/13 ,  C07C15/00

    Abstract: The invention relates to a method for producing aromatic hydrocarbons from a C 1 -C 4 alkane or a mixture of C 1 -C 4 alkanes. Said method is characterized in that a) an educt flow A containing a C 1 -C 4 alkane or a mixture of C 1 -C 4 alkanes is brought in contact with a catalyst, and some of the C 1 -C 4 alkane or some of the mixture of C 1 -C 4 alkanes is reacted to aromatic hydrocarbon/s, b) the product flow B resulting from step a) is separated into a low-boiling flow C containing the main portion of the hydrogen and the non-reacted C 1 -C 4 alkane or mixture of C 1 -C 4 alkanes, and a high-boiling flow D or several high-boiling flows D' containing the main portion of the obtained aromatic hydrocarbon, and c) the low-boiling flow C is fed to another process consuming C 1 -C 4 alkane, the hydrogen contained in the low-boiling flow C being optionally eliminated beforehand.

    Abstract translation: 本发明涉及一种用于从C 1 -C 4 烷烃，或C的混合物 1 -C生产芳烃 4 烷烃，其特征在于，a）一种反应物流A，其为C 1 -C 4 烷烃或的混合物 ç 1 -C 4 包含烷烃，被带入与催化剂接触，而C的一部分 1 -C 4 烷烃或C的混合物的一部分 1 -C 4 烷烃芳烃（S），进行反应; b）由步骤a）的产品流B产生，成低沸流C是氢的主要部分和所述未反应的C 1 -C 4 烷烃，或混合 ç 1 -C 4 包含烷烃，和高沸点流D或多种高沸点流D”，其是，或包含所形成的芳香族烃的主要部分或包含导出; 和c）将低沸点流C 4 供给下一个C 1 -C 烷烃耗时的过程，其中，如果必要的话，包含在低锅炉流C的氢被预先分离。

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