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    • 8. 发明公开
    • PROCÉDÉ CONTINU DE CARBONYLATION D'ALCOOLS, ET NOTAMMENT DE PHÉNYLALCOOLS
    • 连续法进行羰基化醇,尤其是苯基醇
    • EP2651870A2
    • 2013-10-23
    • EP11811095.6
    • 2011-12-13
    • Aet Group
    • PILIA, RaimondoTRANI, AlexandreMARIE, SabrinaDE PANTHOU, Fabrice
    • C07C51/12C07C51/14C07C61/08
    • C07C51/12C07C57/30C07C57/32C07C57/58C07C61/135
    • The invention relates to a continuous method for the carbonylation of an (R
      1 R
      3 )C - X alcohol in acid, where: R
      1 and R
      3 are radicals bonded to the carbon atom by means of a single covalent bond, or an aliphatic cyclic compound that integrates the central carbon atom and bonds to the latter on each side by means of a single covalent bond; and C - X is C(R) - OH, where R is (Z
      1 Z
      2 )HC- or (Z
      1 Z
      2 )C-, it being a given that said radical (Z
      1 Z
      2 )C- can be a substituted or unsubstituted unsaturated cyclic compound such as a benzene cyclic compound. Said method is carried out in a piston reactor provided with a mechanical axial agitation means, and in said method: a) at least one liquid phase comprising said raw alcohol is continuously added, optionally into an appropriate solvent, and a strong acid is also continuously added; b) said at least one liquid phase is subjected to mechanically axially agitated under the influence of a CO pressure of 2 to 250 bar during a transit time t of between 10 seconds and 10 minutes; and c) the liquid phase is removed from said reactor, and in said method, the temperature increase ΔT of the liquid, between the input thereof and removal thereof in/from the reactor, is controlled such that the ratio ΔΤ/AT
      ad (where AT
      ad is the adiabatic temperature increase) is between 0.02 and 0.6 when the ratio between the characteristic heat transfer time t
      therm and the characteristic matter transfer time t
      mat is between 1 and 50.