PROCESS FOR THE PRODUCTION OF HYDROGEN PEROXIDE
    3.
    发明公开
    PROCESS FOR THE PRODUCTION OF HYDROGEN PEROXIDE 有权
    生产过氧化氢的方法

    公开(公告)号:EP1307399A1

    公开(公告)日:2003-05-07

    申请号:EP01969572.5

    申请日:2001-08-03

    IPC分类号: C01B15/029 C01B15/013

    CPC分类号: C01B15/013 C01B15/029

    摘要: Process for the production of concentrated aqueous solutions of hydrogen peroxide, comprising the following steps: (a) feeding to a reactor containing a catalyst based on palladium and platinum, heterogeneous and maintained in dispersion in a liquid reaction medium: (i) a liquid stream consisting of an alcohol or a mixture of C1-C3 alcohols or a mixture of said alcohols with water containing at least 50% by weight of alcohol, also containing an acid promoter and a halogenated promoter, the alcohol and optionally all or part of the water contained in the stream being recycled from the subsequent phase d); (ii) a gaseous stream containing hydrogen, oxygen and an inert gas, characterized in that the concentration of the hydrogen is less than 4.5 % by volume and the concentration of the oxygen is less than 21 % by volume, the complement to 100 being an inert gas; (b) removing from the reactor: (iii) a liquid stream consisting of stream (i) and also containing the hydrogen peroxide and water produced by the reaction, characterized in that the concentration of hydrogen peroxide ranges from 2 % to 10 % by weight; and (iv) a gaseous stream essentially consisting of non-reacted hydrogen and oxygen and the inert gas, (c) optionally adding to (iii) water in such a quantity so that its content is at least equal to that of the final aqueous solution of hydrogen peroxide; (d) sending the stream deriving from (c) to a system consisting of one or more evaporators or distillation columns from which the following are removed: (v) one or more streams containing all the alcohol and possibly water, which are recycled to (a); (vi) a concentrated aqueous solution of H2O2 at a concentration ranging from 15 to 60 % by weight; (vii) optionally a stream containing the water fed in excess in (c).

    摘要翻译: 包括以下步骤:(a)加入到含有基于钯和铂的催化剂的反应器中,所述催化剂是非均相的并保持分散在液体反应介质中:(i)液体流 由醇或C1-C3醇的混合物或所述醇与含有至少50重量%醇的水的混合物组成,还含有酸促进剂和卤化促进剂,所述醇和任选的全部或部分水 包含在从后续阶段d)再循环的物流中; (ii)含有氢气,氧气和惰性气体的气态物流,其特征在于氢气的浓度小于4.5体积%,氧气的浓度小于21体积%,100的补充物为 惰性气体; (b)从反应器中除去:(iii)由物流(i)组成并且还含有过氧化氢和反应产生的水的液体物流,其特征在于过氧化氢的浓度为2重量%至10重量% ; 和(iv)主要由未反应的氢气和氧气和惰性气体组成的气流,(c)任选地向(iii)水中加入一定量的水以使其含量至少等于最终水溶液的含量 的过氧化氢; (d)将由(c)得到的料流输送到由一个或多个蒸发器或蒸馏塔组成的系统,从中除去以下物质:(v)含有所有醇和可能的水的一个或多个料流, 一个); (vi)浓度范围为15至60重量%的H 2 O 2浓缩水溶液; (vii)任选地包含在(c)中过量供给的水的流。

    PROCESS FOR THE PREPARATION OF 1-OCTENE
    4.
    发明授权
    PROCESS FOR THE PREPARATION OF 1-OCTENE 有权
    工艺生产1-辛烯

    公开(公告)号:EP1678103B1

    公开(公告)日:2009-06-03

    申请号:EP04765947.9

    申请日:2004-10-11

    IPC分类号: C07C2/40 C07C5/05

    摘要: Process in two steps for the preparation of 1-octene starting from butadiene which comprises: a first step (a) in which the bis-hydrodimerization of butadiene to 1,7-octadiene is effected in the presence of a catalyst based on a palladium complex containing one or more tri-substituted monodentate phosphines, in an aprotic polar solvent optionally containing an organic base; a second step (b) in which the partial catalytic hydrogenation of 1,7-octadiene to 1-octene is effected, the above process being characterized in that: (i) in the first step the aprotic polar solvent is selected from disubstituted cyclic ureas; (ii) in the second step the catalyst is selected from non­ supported ruthenium complexes having general formula (I I): RuXmLn (I I).

    PROCESS FOR THE RECYCLING OF EXPANDED POLYSTYRENE
    7.
    发明授权
    PROCESS FOR THE RECYCLING OF EXPANDED POLYSTYRENE 有权
    FOR聚苯乙烯回收利用方法扩增

    公开(公告)号:EP1907462B1

    公开(公告)日:2009-12-16

    申请号:EP06762235.7

    申请日:2006-06-28

    IPC分类号: C08J11/08 C08L25/06

    摘要: The invention relates to an enhanced process for the recycling of expanded polystyrene. Said process essentially comprises the reduction in volume of expanded polystyrene by means of dissolution in a solvent, separation of the insoluble components, selective precipitation of the polystyrene with an anti-solvent, separation, drying and extrusion of the precipitated polystyrene, recovery by distillation and recycling of the solvent. The process is characterized in that the anti-solvent is a butanol selected form n-butanol, iso-butanol or sec-butanol and the solvent is dimethyl carbonate, alone or in a mixture containing up to 25% by weight of butanol.