ÜBERWACHUNG DES STÖCHIOMETRISCHEN VERHÄLTNISSES BEI DER UMSETZUNG VON NITROAROMATEN MIT WASSERSTOFF
    31.
    发明公开
    ÜBERWACHUNG DES STÖCHIOMETRISCHEN VERHÄLTNISSES BEI DER UMSETZUNG VON NITROAROMATEN MIT WASSERSTOFF 有权
    监测的化学计量比在氢气硝基芳烃的执行情况

    公开(公告)号:EP2812308A1

    公开(公告)日:2014-12-17

    申请号:EP13702651.4

    申请日:2013-02-07

    Applicant: BASF SE

    CPC classification number: C07C209/36 C07C211/47

    Abstract: The present invention relates to a continuous method for producing at least one aromatic amine by hydrogenation of at least one nitroaromatic with hydrogen, wherein a liquid phase containing at least the aromatic amine and a gaseous phase containing at least hydrogen are present, in the presence of a catalyst suspended in the liquid phase, at a temperature of 50-250°C and a pressure of 5-0 bar. The pressure in the reactor is held substantially constant by continuously adjusting the quantity of hydrogen supplied to the reactor, the total amount of hydrogen supplied to the reactor is monitored and the supply of the at least one nitroaromatic is interrupted if the hydrogen uptake of the reactor does not amount to at least 50 mol% of the hydrogen quantity required for stoichiometric reaction of the at least one nitroaromatic to form the at least one aromatic amine.

    VERFAHREN ZUR GEWINNUNG VON REIN-ANILIN
    35.
    发明公开
    VERFAHREN ZUR GEWINNUNG VON REIN-ANILIN 有权
    得到纯 - 苯胺

    公开(公告)号:EP2906528A1

    公开(公告)日:2015-08-19

    申请号:EP13774667.3

    申请日:2013-10-10

    Applicant: BASF SE

    CPC classification number: C07C209/84 C07C211/46

    Abstract: The invention relates to a method for obtaining pure aniline by catalytically hydrogenating nitrobenzene and reprocessing the reaction mixture obtained therefrom, having the following method steps: - the catalytic hydrogenation of nitrobenzene; - optionally the partial condensation of the reaction mixture of the catalytic hydrogenation in one or more stages; - the separation of the reaction mixture obtained after the catalytic hydrogenation or the condensation, which is optionally carried out, into a gas phase, which contains hydrogen, and a liquid phase; - the liquid-liquid phase separation of the liquid phase obtained in the separation step, thereby obtaining an aqueous phase, which is further reprocessed or discharged, and raw analine as an organic phase, said raw analine containing 90-95 wt.% aniline, 4-9 wt.% water, and residual high boilers relative to the analine, in each case based on the total weight of the raw analine, and the sum of the components of the raw analine equaling 100 wt.%; and - the pre-cleaning of the raw analine by partly or completely separating the water via the head stream of a first distillation column, thereby obtaining a bottom stream that is fed as a feed stream to a purification column from which a pure aniline stream containing at least 99.9 wt.% aniline based on the total weight of the pure analine stream is drawn via the head and a bottom stream containing high boilers is drawn and fed to a combustion process. The invention is characterized in that the weight ratio of the bottom stream from the purification column is limited to maximally 0.8% relative to the weight of the feed stream, thereby ensuring that said bottom stream can be pumped under the effect of a corresponding trace heating of the lines provided for this purpose, said trace heating ensuring that the temperature of the stream conducted in the lines is 45 °C or higher, wherein the bottom stream is exposed to methanol, ethanol, propanol, acetone, or mixtures thereof in a weight ratio of 5-30% based on the weight of the bottom stream.

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