CIESC Journal

• 化工学报 • 上一篇    下一篇

甲基叔丁基醚合成反应动力学研究

张维轲   

  1. 吉林化学工业公司研究院
  • 出版日期:1985-09-25 发布日期:1985-09-25

Synthesis Kinetics of Methyl Tertbutyl Ether

Zhang Weike (Jilin Research Institute of chemical Technology)   

  • Online:1985-09-25 Published:1985-09-25

摘要: 本文用新颖的液固相微型反应器对甲基叔丁基醚合成反应动力学作了研究.证明这一可逆过程的正反应在不同醇烯比时会发生反应级数的改变.决定反应级数改变的醇烯比又与温度有关,归纳出描述这一关系的经验方程.考察了逆反应速度,提出合成甲基叔丁基醚反应在两种情况下的可逆反应动力学模型.文中还讨论了反应机理,并为解释反应级数改变提出了部分新的假设.

Abstract: Experiments proved that the etherification between methanol and iso-butene catalyzed by a macroporous sulfonic acid resin in producing methyl tertbutyj ether is a reversible reaction. At a certain temperature, there is a definite methanol/isobutene molal ratio (Rao), below which the etherification rate is second-order on isobutene concentration and negative first-order on rnethanol. When the ratio is higher than Rao, the reaction becomes first-order on isobutene concentration and zero-order on methanol. The dependence of Rao on temperature can be expressed as follows: The disether ification (reverse reaction) rate is first-order on MTBE concentration. The reaction rate equations may be given as when Ra is smaller than Rao, and when Ra is larger than Rao. The reaction is as taking place with the electrophilic mechanism. The solvated proton hypothesis suggested by other authors cannot explain the transition rates at methanol/isobutene ratio = Rao. A novel liquid-solid microreactor containing about 50 mg of catalyst was used in carrying out the experiments.