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A method for the production of mono chlorine acetylene and vinyl chloride, in addition to 1, 2 - dichlorobenzene acetylene

机译:除1,2-二氯苯乙炔外,还生产一氯乙炔和氯乙烯的方法

摘要

Chlorinated hydrocarbons are produced by contacting a feed containing ethane, hydrogen chloride and molecular oxygen in the vapour phase at elevated temperature with a catalyst comprising copper deposited on activated alumina, the alumina having been subjected prior to deposition, to a heat treatment at a temperature between 500 DEG and 1,400 DEG C. The catalyst may be copper, copper oxide or copper chloride which may be applied to the support in any suitable manner. The catalyst/alumina mixture should preferably contain 0.5-10% by weight of copper in free or combined form. The catalyst may also contain an alkali and/or alkaline earth metal in combined form in an amount preferably of 0.5-5% by weight. Suitable compounds are, for example, the hydroxides, chlorides, carbonates, aluminates or nitrates of sodium, potassium or magnesium. The catalysts may also contain iron or a rare earth metal. The reaction temperature is preferably in the range 200-500 DEG C. The main products are vinyl chloride, ethyl chloride and 1,1 and 1,2-dichlorethanes. The dichlorethanes may be further pyrolyzed to give vinyl chloride and hydrogen chloride which may be recycled to the process. By-products include dichlorethylenes, trichloroethanes, tetrachloroethane and pentachloroethane.
机译:氯化烃是通过在高温下使包含乙烷,氯化氢和分子氧的气相进料与包含沉积在活性氧化铝上的铜的催化剂接触而制得的,该氧化铝在沉积之前已经进行了热处理,其温度为500℃和1,400℃。催化剂可以是铜,氧化铜或氯化铜,它们可以以任何合适的方式施加到载体上。催化剂/氧化铝混合物应优选含有0.5-10重量%的游离或结合形式的铜。催化剂也可以以优选0.5-5重量%的量包含结合形式的碱金属和/或碱土金属。合适的化合物是例如钠,钾或镁的氢氧化物,氯化物,碳酸盐,铝酸盐或硝酸盐。催化剂也可以包含铁或稀土金属。反应温度优选在200-500℃的范围内。主要产物是氯乙烯,氯乙烷和1,1和1,2-二氯乙烷。可以将二氯乙烷进一步热解,得到氯乙烯和氯化氢,它们可以再循环到该方法中。副产物包括二氯乙烯,三氯乙烷,四氯乙烷和五氯乙烷。

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