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    РЕАКТОР ДЛЯ ПРОВЕДЕНИЯ АВТОТЕРМИЧЕСКОЙ ДЕГИДРОГЕНИЗАЦИИ ГАЗОВОЙ ФАЗЫ
    1.
    发明专利
    РЕАКТОР ДЛЯ ПРОВЕДЕНИЯ АВТОТЕРМИЧЕСКОЙ ДЕГИДРОГЕНИЗАЦИИ ГАЗОВОЙ ФАЗЫ 未知

    公开(公告)号：EA024781B1

    公开(公告)日：2016-10-31

    申请号：EA201390915

    申请日：2011-12-13

    Applicant: BASF SE

    Inventor： OLBERT GERHARD ,  WEGERLE ULRIKE ,  KOLIOS GRIGORIOS ,  KOSTOVA ALBENA ,  KESSEL JASMINA ,  WECK ALEXANDER ,  REZAI ALIREZA

    IPC: B01J19/24 ,  C07C5/48

    Abstract: Предлагаетсяреактор (1) ввидегоризонтальногоцилиндрадляпроведенияавтотермическойдегидрогенизациигазовойфазыуглеводородсодержащегогазовогопотока (2) газовымпотоком (3), содержащимкислород, ссохранениемреакционнойгазовойсмеси, нагетерогенномкатализаторев видемонолита (4), причемс помощьюрасположенноговдольокружностиреактора (1) разборного, газонепроницаемогокорпуса G ввидекруговогоцилиндраилипризмыполостьреактора (1) поделенанавнутреннююобластьА, соднойилинесколькимикаталитическиактивнымизонами (5), гдесоответственноупаковкаизуложенныхдругнадруга, рядоми другзадругоммонолитов (4) изона (6) смешенияпередкаждойкаталитическиактивнойзоной (5) снабженасоответственнотвердымивстроеннымиэлементами, ивнешнююобластьВ, расположеннуюкоаксиальновнутреннейобластиА, причемнаконцереактора, присоединяяськ корпусу G, находитсятеплообменник (12), которыйотличаетсятем, чтов наружнуюобластьВ подаютинертныйгаз.

    REACTOR FOR CARRYING OUT AUTOTHERMAL GAS-PHASE DEHYDRATION
    4.
    发明专利
    REACTOR FOR CARRYING OUT AUTOTHERMAL GAS-PHASE DEHYDRATION 未知

    公开(公告)号：MY163217A

    公开(公告)日：2017-08-30

    申请号：MYPI2013002303

    申请日：2011-12-13

    Applicant: BASF SE

    Inventor： OLBERT GERHARD ,  WEGERLE ULRIKE ,  DR - ING KOLIOS GRIGORIOS ,  DR -ING KOSTOVA ALBENA ,  KESSEL JASMINA ,  WECK ALEXANDER ,  REZAI ALIREZA

    IPC: B01J19/24 ,  C07C5/48

    Abstract: THE INVENTION RELATES TO A REACTOR (1) IN THE FORM OF A HORIZONTAL CYLINDER (3) FOR CARRYING OUT AUTOTHERMAL GAS PHASE DEHYDRATION OF A HYDROCARBON-CONTAINING GAS FLOW (2) WITH AN OXYGEN-CONTAINING GAS FLOW (3), YIELDING A REACTION GAS MIXTURE, AT A HETEROGENEOUS CATALYST DESIGNED AS A MONOLITH (4), WHEREIN THE INNER CHAMBER OF THE REACTOR (1) IS DIVIDED BY A REMOVABLE, CIRCULAR CYLINDRICAL OR PRISMATIC HOUSING G, WHICH IS DISPOSED IN THE LONGITUDINAL DIRECTION OF THE REACTOR (1) AND IS GAS-TIGHT IN THE CIRCUMFERENTIAL DIRECTION, INTO AN INNER AREA A HAVING ONE OR MORE CATALYTICALLY ACTIVE ZONES (5), IN EACH OF WHICH A PACKAGE OF MONOLITHS (4) STACKED ON EACH OTHER, ADJACENT TO EACH OTHER, AND ARRANGED ONE BEHIND THE OTHER IS PROVIDED, A MIXING ZONE (6) HAVING FIXED INSTALLED FIXTURES BEING PROVIDED IN FRONT OF EACH ACTIVE ZONE (5), AND INTO AN OUTER AREA B DISPOSED COAXIALLY TO THE INNER AREA A, AND WHEREIN A HEAT EXCHANGER (12) CONNECTED TO THE HOUSING G IS PROVIDED AT AN END OF THE REACTOR, CHARACTERIZED IN THAT AN INERT GAS IS SUPPLIED TO THE OUTER AREA B. (FIGURE 1)

    REACTOR FOR CARRYING OUT AUTOTHERMAL GAS-PHASE DEHYDROGENATION
    7.
    发明专利
    REACTOR FOR CARRYING OUT AUTOTHERMAL GAS-PHASE DEHYDROGENATION 未知

    公开(公告)号：CA2782417A1

    公开(公告)日：2011-06-09

    申请号：CA2782417

    申请日：2010-11-30

    Applicant: BASF SE

    Inventor： KOLIOS GRIGORIOS ,  RUPPEL WILHELM ,  WEGERLE ULRIKE ,  KESSEL JASMINA ,  GERLINGER WOLFGANG ,  MABANDE GODWIN TAFARA PETER ,  SCHINDLER GOETZ-PETER ,  KOSTOVA ALBENA ,  OLBERT GERHARD ,  PFAB PETER

    IPC: B01J19/24

    Abstract: The invention relates to a reactor (1) in the form of a horizontal cylinder for carrying out autothermal gas phase dehydrogenbation of a hydrocarbon-containing gas flow (2) by means of an oxygen-containing gas flow (3), with a reaction mixture being obtained, on a heterogeneous catalyst in the form of a monolith (4), characterized in that the interior of the reactor (1) is divided by a detachable cylindrical or prismatic housing G, which is disposed in the longitudinal direction of the reactor (1), gastight in the circumferential direction and open at both end faces thereof, into an inner area A, having one or a plurality of catalytically active zones (5), in which are provided a packing of monoliths (4) stacked on, adjacent, and above one another, and, in front of each catalytically active zone (5), a mixing zone (6) having fixed installations, and an outer area B disposed coaxially to the inner area A.

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