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    VERFAHREN ZUR GEWINNUNG VON (CHLOR)KOHLENWASSERSTOFFFREIEM CHLORWASSERSTOFF UND PHOSGENFREIEN (CHLOR)KOHLENWASSERSTOFFEN AUS EINEM (CHLOR)KOHLENWASSERSTOFFE UND PHOSGEN ENTHALTENDEN CHLORWASSERSTOFFSTROM
    21.
    发明公开
    VERFAHREN ZUR GEWINNUNG VON (CHLOR)KOHLENWASSERSTOFFFREIEM CHLORWASSERSTOFF UND PHOSGENFREIEN (CHLOR)KOHLENWASSERSTOFFEN AUS EINEM (CHLOR)KOHLENWASSERSTOFFE UND PHOSGEN ENTHALTENDEN CHLORWASSERSTOFFSTROM 有权
    一种获得（氯）油气游离盐酸和光气（氯）碳氢化合物A（氯）烃和光气含有盐酸电源

    公开(公告)号：EP1981619A1

    公开(公告)日：2008-10-22

    申请号：EP07712101.0

    申请日：2007-01-25

    Applicant: BASF SE

    Inventor： SESING, Martin ,  SCHELLING, Heiner ,  CIPRIAN, Jürgen ,  DEBERDT, Filip ,  KARCHES, Martin ,  SCHUBERT, Olga

    IPC: B01D53/68 ,  B01D53/70 ,  B01D53/75 ,  C01B7/07

    CPC classification number: C01B7/0718

    Abstract: In a process for extracting (chlorinated) hyrocarbon-free hydrogen chloride and phosgene-free (chlorinated) hydrocarbons from a hydrogen chloride stream containing (chlorinated) hydrocarbons and phosgene, (i) the fresh hydrogen chloride stream containing phosgene and (chlorinated) hydrocarbons is led in a first step first through a first adsorber and then through a second adsorber interconnected in series, until essentially no more (chlorinated) hydrocarbon is adsorbed by the first adsorber; (ii) the fresh hydrogen chloride stream is led in a second step through the second adsorber, while the first adsorber is regenerated, substantially phosgene-free (chlorinated) hydrocarbon being produced during regeneration; (iii) the fresh hydrogen chloride stream is led in a third step first through the second adsorber and then through the regenerated first adsorber, until substantially no more (chlorinated) hydrocarbon is adsorbed by the second adsorber; (iv) the fresh hydrogen chloride stream is led in a fourth step through the first adsorber, while the second adsorber is regenerated, a substantially phosgene-free (chlorinated) hydrocarbon being produced during regeneration, and steps (i) to (iv) can be successively repeated one or more times.

    VERFAHREN ZUR HERSTELLUNG VON BENZOL AUS METHAN
    25.
    发明公开
    VERFAHREN ZUR HERSTELLUNG VON BENZOL AUS METHAN 审中-公开
    VERFAHREN ZUR HERSTELLUNG冯BENZOL AUS METHAN

    公开(公告)号：EP2473463A2

    公开(公告)日：2012-07-11

    申请号：EP10747846.3

    申请日：2010-08-23

    Applicant: BASF SE

    Inventor： SCHNEIDER, Christian ,  KARCHES, Martin ,  TSOU, Joana, Coelho ,  AHRENS, Sebastian ,  STÜTZER, Dieter

    IPC: C07C2/76 ,  C07C15/02

    CPC classification number: C07C2/76 ,  Y02P20/584 ,  C07C15/02

    Abstract: The present invention relates to a process for the non-oxidative dehydroaromatization of a feed stream containing C1-C4 aliphatics comprising the steps I, feeding the feed stream E into a reaction zone 1, reacting the feed stream E under non-oxidative conditions in the presence of a particulate catalyst to give a product stream P containing aromatic hydrocarbons, and removing the product stream P from the reaction zone 1; II, transferring the catalyst that is reduced in its activity by deposited coke into a reaction zone 2; III, at least partial regeneration of the catalyst with feed of a hydrogen-containing gas stream H in a reaction zone 2, wherein at least some of the deposited coke is converted into methane and a methane-containing gas stream M is formed that is fed at least in part to the reaction zone 1; IV, removing the catalyst from the reaction zone 2 and V, recirculating at least some of the catalyst that is removed to the reaction zone 1, wherein reaction zone 1 and reaction zone 2 are arranged spatially adjacently in the same reactor.

    Abstract translation: 本发明涉及一种使含有C 1 -C 4脂族化合物的反应物流非氧化脱氢芳构化的方法，包括以下步骤：将反应物流E加入到反应区1中，在非氧化条件下在颗粒催化剂存在下将反应物流E转化 涉及包含芳烃并从反应区1排出产物流P的产物流P，II。 由于沉积的焦炭进入反应区域2，III而导致活性降低的催化剂。 在反应区2中供应含氢气流H至少部分地再生催化剂，至少部分沉积的焦炭转化成甲烷以形成含甲烷的气流M，其至少部分地进料至反应 区域1，IV。 将催化剂从反应区2排出，并将至少一部分排出的催化剂再循环到反应区1中，反应区1和反应区2在相同的反应器中彼此空间上相邻布置。

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