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method for producing 1,1,2 - trichloräthan from 1.2 - dichloräthan and chlorine

机译:从1.2-二氯甲烷和氯气生产1,1,2-三氯甲烷的方法

摘要

1458338 Preparation of 1,1,2-trichloroethane SOLVAY & CIE 7 March 1975 [8 March 1974] 9602/75 Heading C2C 1,1,2-Trichloroethane is obtained by reacting liquid 1,2-dichloroethane with chlorine under boiling conditions in one or more consecutive reactors, each having a peroxide supply and a chlorine inlet, in the presence of one or more of the following peroxides: propionyl, isobutyryl, capriloyl, 3,5,5-trimethyl hexanoyl, decanoyl, lauroyl and 2,4-dichlorobenzoyl peroxides, isopropyl and cyclohexyl percarbonates, and t-butyl perpivalate. The reaction is suitably conducted at a temperature of 80-110‹ C. at pressures which are close to atmospheric pressure. From 10SP-4/SP to 2 Î 10SP-2/SP mol of peroxide per litre of reaction mixture may be introduced into the, or each, reactor, and the molar ratio of total chlorine to 1,2- dichloroethane is preferably from 0À1 to 1 : 1 to 1À1 : 1. The reaction is preferably carried out in the presence of less than 10SP-3/SP mol of oxygen per mol of chlorine and less than 15 parts of ferric ions per million parts of 1,2- dichloroethane. The dwell time of the reactants in the (or each) reactor is generally from 1 to 60 minutes at 80‹ C., 0À25 to 40 minutes at 110‹ C., or certain defined values within these two limits. The process may be carried out either batchwise or continuously, suitable flow diagrams being described.
机译:1458338制备1,1,2-三氯乙烷SOLVAY&CIE 1975年3月7日[1974年3月8日] 9602/75标题C2C 1,1,2-三氯乙烷是通过使1,2-二氯乙烷与氯在沸腾条件下反应一在以下一种或多种过氧化物的存在下,具有一个或多个连续的反应器,每个反应器均具有过氧化物供应源和氯入口:丙酰基,异丁酰基,癸酰基,3,5,5-三甲基己酰基,癸酰基,月桂酰基和2,4-过氧化二氯苯甲酰,过碳酸异丙酯和环己基酯以及过新戊酸叔丁酯。该反应合适地在80-110℃的温度下在接近大气压的压力下进行。每升反应混合物从10 -4 到2Î10 -2 摩尔过氧化物可以引入反应器中,或每个反应器中,总氯的摩尔比相对于1,2-二氯乙烷,优选1∶1至1∶1至1∶1∶1。该反应优选在每摩尔氯小于10 SP -3 SP的氧存在下进行。每百万份1,2-二氯乙烷中的铁离子含量不到15份。在(或每个)反应器中反应物的停留时间通常在80°C下为1至60分钟,在110°C下为0-25至40分钟,或这两个范围内的某些定义值。该过程可以分批或连续地进行,描述了合适的流程图。

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