HERSTELLUNG VON PHTHALSÄUREANHYDRID DURCH GASPHASENOXIDATION VON O-XYLOL
    21.
    发明公开
    HERSTELLUNG VON PHTHALSÄUREANHYDRID DURCH GASPHASENOXIDATION VON O-XYLOL 有权
    通过邻二甲苯的气相氧化制备邻苯二甲酸酐

    公开(公告)号:EP2024351A1

    公开(公告)日:2009-02-18

    申请号:EP07729285.2

    申请日:2007-05-18

    Applicant: BASF SE

    CPC classification number: C07D307/89 C07C51/265 C07C63/16

    Abstract: The invention relates to a method for producing phthalic anhydride by catalytic gas phase oxidation of o-xylol. According to said method, a gaseous mixture of o-xylol and an oxygen-containing gas is guided through at least two reaction zones in a main reactor, the temperature of said reaction zones being adjustable independently of each other, and is reacted to give a gaseous intermediate reaction product which contains unreacted o-xylol, phthalic anhydride reaction products with a lower oxidation state and phthalic anhydride, and the intermediate reaction product is introduced into a secondary reactor. The temperature in the reaction zones in the primary reactor is controlled in such a manner that the concentration of the unreacted o-xylol in the intermediate reaction product is at least 0.5% by weight. The method according to the invention allows an increase in total yield of phthalic anhydride without any or without substantial decrease in product quality.

    VERFAHREN ZUR HERSTELLUNG VON ETHYLENOXID IN EINEM MIKROKANALREAKTOR
    22.
    发明公开
    VERFAHREN ZUR HERSTELLUNG VON ETHYLENOXID IN EINEM MIKROKANALREAKTOR 审中-公开
    用于在微通道反应器生产乙烯

    公开(公告)号:EP2013194A2

    公开(公告)日:2009-01-14

    申请号:EP07727831.5

    申请日:2007-04-05

    Applicant: BASF SE

    CPC classification number: C07D301/10 B01J2219/00781

    Abstract: Method for production of ethylene oxide in a microchannel reactor, wherein an ethylene-containing material stream and an oxygen- or oxygen-source-containing material stream are fed to the microchannel reactor and the reaction to give ethylene oxide takes place in the catalyst-containing microchannel reactor. Alkyl halides are continuously fed to the microchannel reactor at a concentration of 0.3 to 50 ppm by volume with respect to the total volume stream of all material streams fed to the reactor.

Patent Agency Ranking