Gas-phase pyrolyses of 1,1-dichlorobutane and 1,1-dichloropropane

K. A. Holbrook, K. Parry
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引用次数: 2

Abstract

The gas-phase pyrolysis of 1,1-dichlorobutane has been studied at initial pressures of 5–150 Torr between 416 and 460°C. Analysis by g.l.c. shows that the amount of dichlorobutane removed is equal to the pressure increase as would be expected for the elimination (i). The pressure increase was used to determine the first-order rate PrnCHCl2→cis- and trans-EtCHCHCl + HCl (i) constant for this reaction which is expressed by equation (ii), where the error limits are the 95% confidence limits. log10(k/s–1)=(13·68 ± 0·27)–(53,872 ± 715)/4·576T(ii)The observed cis:trans-ratio for the 1-chlorobutene was 1·00 ± 0·02 at these temperatures compared with an equilibrium value of 1·60 ± 0·08 which was found independently. No cis–trans-isomerisation occurred under these conditions.The gas-phase pyrolysis of 1,1-dichloropropane was reinvestigated at pressures of 9–185 Torr between 389·2 and 456·5°C. The observed cis:trans-ratio of the 1-chloropropene produced was 1·20 ± 0·02 under these conditions and cis–trans-isomerisation is negligible. The comparable equilibrium cis:trans-ratio at these temperatures is 1·90 ± 0·08. The pressure change obeys first-order kinetics and the rate constant is expressed by equation (iii) where the error limits are the 95% confidence limits. log10(k/s–1)=(14·32 ± 0·30)–(56,679 ± 821)/4·576T(iii)Both pyrolyses have also been briefly studied in packed reaction vessels. The resulting cis:trans-ratios observed then favour the cis-product olefins.
1,1-二氯丁烷和1,1-二氯丙烷的气相热解
研究了1,1-二氯丁烷在416 ~ 460℃、5 ~ 150 Torr的初始压力下的气相热解过程。通过g.l.c.分析表明,去除的二氯丁烷的量等于消除(i)所期望的压力增加。压力增加用于确定该反应的一级速率PrnCHCl2→顺式和反式etchchcl + HCl (i)常数,该常数由式(ii)表示,其中误差限为95%置信限。log10(k/ s-1)=(13.68±0.27)-(53,872±715)/ 4.5776 t (ii)在这些温度下,1-氯丁烯的顺反比为1.00±0.02,而独立发现的平衡值为1.60±0.08。在这些条件下没有发生顺式-反式异构化。研究了1,1-二氯丙烷在389·2 ~ 456·5℃、9 ~ 185 Torr压力下的气相热解过程。在此条件下,1-氯丙烯的顺反比为1.20±0.02,顺反异构化可以忽略不计。在这些温度下,平衡的顺反比为1.90±0.08。压力变化服从一级动力学,速率常数由式(iii)表示,其中误差限为95%置信限。log10(k/ s-1)=(14·32±0·30)-(56,679±821)/4·576T(iii)这两种热解过程也在填充反应容器中进行了简要研究。由此观察到的顺反比有利于顺式产物烯烃。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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