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    • 2. 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.
    • 3. 发明公开
    • DISPOSITIF ET PROCÉDÉ POUR LA PHOSGÉNATION EN CONTINU
    • DISPOSITIF ETPROCÉDÉPOUR LAPHOSGÉNATIONEN CONTINU
    • EP2621627A1
    • 2013-08-07
    • EP11771212.5
    • 2011-09-28
    • Aet Group
    • PILIA, RaimondoTRANI, AlexandreMARIE, SabrinaDE PANTHOU, Fabrice
    • B01J19/20C01B31/28
    • B01J19/0046B01J8/222B01J19/20B01J2219/0004B01J2219/00256C01B32/80C07C68/02C07C249/02C07D233/60Y02P20/149
    • Continuous process for catalytic phosgenation of an organic compound E to a product P, said process being carried out in a plug-flow reactor R2, preferably of cylindrical shape, said reactor R2 being provided with a mechanical means for axial stirring, and in which process the phosgene consumed in said reactor R2 is generated continuously in a first reactor R1 located upstream of the reactor R2, and in which process: - phosgene is generated, in said first reactor R1, from CO and Cl
      2 , - at least one liquid phase comprising said organic compound E is sent into said reactor R2 continuously, preferably at the upstream end of said reactor R2, and the phosgene generated in said first reactor R1 is injected, preferably continuously, into said second reactor R2, preferably at its upstream end, - said liquid phase, preferably at a temperature between ‑25°C and +200°C and under axial mechanical stirring, is subjected to the influence of a phosgene pressure of between 1 and 10 bar, for a residence time t of between 1 second and 10 minutes, so that the phosgene reacts with said organic phase in order to form said product P, - the liquid phase comprising said product P is removed from said reactor.
    • 将有机化合物E催化光气化为产物P的连续方法,所述方法在活塞式流动反应器R2中进行,所述活塞式流动反应器R2优选为圆柱形,所述反应器R2具有用于轴向搅拌的机械装置,并且在该方法中 在所述反应器R2中消耗的光气在位于反应器R2上游的第一反应器R1中连续地产生,并且在该过程中: - 在所述第一反应器R1中由CO和Cl 2产生光气, - 至少一个液相 包括所述有机化合物E连续地,优选在所述反应器R2的上游端被送入所述反应器R2,并且优选在其上游端优选连续地将所述第一反应器R1中产生的光气注入到所述第二反应器R2中, - 所述液相优选在-25℃和+ 200℃之间的温度下并且在轴向机械搅拌下经受1-10巴的光气压力的影响, 理想时间t在1秒和10分钟之间,以便光气与所述有机相反应以形成所述产物P, - 从所述反应器中除去包含所述产物P的液相。