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Producing Ethylene from Natural Gas via the Synthesis and Subsequent Pyrolysis of Methyl Chloride: Increasing Selectivity by Introducing a Stage of Polychloromethane Hydrodechlorination

机译:通过合成和随后的氯甲烷热解从天然气中生产乙烯:通过引入一阶段的二氯甲烷加氢脱氯来提高选择性

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摘要

Comparative tests of palladium, nickel-molybdenum, and lanthanum-magnesium-nickel catalyst samples with aluminium oxide are performed to select an effective catalyst for the hydrodechlorination of methylene chloride and chloroform. The tests are conducted in a flow reactor with a fixed catalyst layer at 300°C with a contact time of 3.8 s and a hydrogen-to-methylene chloride molar ratio of 3 : 1. The nickel- molybdenum catalyst is found to be the one most effective. Improvements to the technological process scheme for the priority production of ethylene to be used in obtaining vinyl chloride are proposed. These improvements require the production of ethylene via an additional stage of the pyrolysis of methane homologues isolated from natural gas and formed in the pyrolysis of methyl chloride, along with a stage of polychloromethane hydrodechlorination.
机译:进行了钯,镍-钼和镧-镁-镍催化剂样品与氧化铝的对比试验,以选择有效的催化剂用于二氯甲烷和氯仿的加氢脱氯。该测试是在流动反应器中进行的,该反应器在300°C下具有固定的催化剂层,接触时间为3.8 s,氢与二氯甲烷的摩尔比为3:1。发现镍钼催化剂是一种最有效率。提出了对用于获得氯乙烯的优先生产乙烯的工艺方法的改进。这些改进要求通过从天然气中分离并在氯甲烷的热解中形成的甲烷同系物的热解的附加阶段以及聚氯甲烷加氢脱氯的阶段来生产乙烯。

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