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METHOD FOR PRODUCING ACETYLENE ACCORDING TO THE SACHSSE-BARTHOLOME METHOD

机译:根据萨克斯-巴顿法的乙炔生产方法

摘要

1. A process for the preparation of acetylene by the method Sakse Bartolome (Sachsse-Bartholome) by burning a mixture of natural gas / oxygen in one or more burners to obtain pyrolysis gas which is in two or more stages cooled in the distillation columns, wherein each burner is connected to respectively one or more distillation columns, and wherein the pyrolysis gas in the first cooling step is quenched via pyrolysis oil to give a low-boiling fraction comprising styrene, indene, benzene, toluene and xylene, of one or more Negotia nnyh columns, which is cooled by direct cooling with water and in the phase separator is separated into an aqueous phase and an organic phase comprising styrene, indene, benzene, toluene and xylene, is fed to the head of one or more distillation columns as reflux, characterized in that the organic phase comprising styrene, indene, benzene, toluene and xylene from the phase separator is fed to a selective hydrogenation on a catalyst which contains at least one platinum group metal on an inorganic metal oxide achestve medium containing from 0.05 to 5% by weight. platinum group metal based on total catalyst weight, and wherein the selective hydrogenation is carried out at a pressure in the range from 1 to 40 bar and a temperature in the range from 25 to 150 ° C.2. A method according to claim 1, characterized in that the organic phase from the phase separator comprising styrene, indene, benzene, toluene and xylene, has the following composition: from 8 to 18% by weight. styrene, from 5 to 10 wt%. indene, a total of from 15 to 20 wt%. amount ortho-, para- and meta-xylene, 15 to 20% by weight. toluene OTH 8 to 10 wt%. benzene, and
机译:1.一种通过萨克斯·巴托洛姆法(Sachsse-Bartholome)方法制备乙炔的方法,该方法是在一个或多个燃烧器中燃烧天然气/氧气的混合物,以得到在两个或更多个阶段在蒸馏塔中冷却的热解气体,其中每个燃烧器分别连接至一个或多个蒸馏塔,并且其中在第一冷却步骤中的热解气体通过热解油骤冷,以得到包含一种或多种的苯乙烯,茚,苯,甲苯和二甲苯的低沸点馏分。 Negotia nnyh柱通过水直接冷却而冷却,并在相分离器中分离为水相,并将包含苯乙烯,茚,苯,甲苯和二甲苯的有机相作为一个或多个蒸馏塔的塔顶进料。回流,其特征在于将来自相分离器的包含苯乙烯,茚,苯,甲苯和二甲苯的有机相进料到含有至少一种催化剂的催化剂上进行选择性氢化。在无机金属氧化物载体上的铂族金属含量为0.05-5重量%。铂族金属,基于总催化剂重量,其中选择性氢化在1至40 bar的压力和25至150°C.2的温度下进行。 2.根据权利要求1的方法,其特征在于来自分相器的包含苯乙烯,茚,苯,甲苯和二甲苯的有机相具有以下组成:8至18重量%。 5至10重量%的苯乙烯。茚,总计15至20重量%。邻二甲苯,对二甲苯和间二甲苯的用量为15至20%(重量)。甲苯OTH 8至10 wt%。苯和

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