化工学报 ›› 2015, Vol. 66 ›› Issue (8): 3057-3063.DOI: 10.11949/j.issn.0438-1157.20150553

• 催化、动力学与反应器 • 上一篇    下一篇

己二酸氨化制己二腈的宏观动力学

冯赛平, 程党国, 陈丰秋, 詹晓力   

  1. 浙江大学化学工程与生物工程学院联合化学反应工程研究所, 浙江 杭州 310027
  • 收稿日期:2015-05-04 修回日期:2015-05-25 出版日期:2015-08-05 发布日期:2015-08-05
  • 通讯作者: 陈丰秋

Apparent kinetics of adipic acid ammoniation to adiponitrile

FENG Saiping, CHENG Dangguo, CHEN Fengqiu, ZHAN Xiaoli   

  1. UNILAB Research Center for Chemical Reaction Engineering, College of Chemical and Biological Engineering, Zhejiang University, Hangzhou 310027, Zhejiang China
  • Received:2015-05-04 Revised:2015-05-25 Online:2015-08-05 Published:2015-08-05

摘要:

己二酸氨化法是工业上生产己二腈的重要方法之一,其中和反应步骤受气液相传质影响很大。采用体积为1 L的半间歇式反应釜,对己二酸中和反应的宏观动力学进行了研究。在磷酸质量分数为0.2%、搅拌速率为1800 r·min-1、氨气流量为600 L·h-1的条件下,实验考察了210~260℃范围内温度对己二酸浓度随时间变化的影响。由实验数据拟合结果表明:在250℃己二酸浓度大于0.1 mol·L-1时为传质控制阶段,中和反应对于己二酸为一级,反应活化能为42.9 kJ·mol-1;在250℃己二酸浓度小于0.1 mol·L-1时为反应控制阶段,中和反应对于己二酸为二级,反应活化能为52.7 kJ·mol-1。模型计算值与实验值相吻合,并结合理论模型得出对己二酸的本征反应级数为二级。保持总压(略大于常压)、温度260℃、搅拌速率1800 r·min-1和磷酸质量分数0.2%保持不变,在氨气流量为200~600 L·h-1的范围内考察了氨气分压对己二酸浓度随时间变化的影响,动力学拟合结果表明对氨气分压的本征反应级数为一级。

关键词: 己二酸, 氨气, 己二腈, 反应动力学, 气液相反应, 传质

Abstract:

Ammoniation of adipic acid is an important method for the production of adiponitrile in industry. The neutralization reaction step is largely affected by the gas-liquid phase mass transfer. The neutralization reaction macrokinetic experiments were conducted in a 1 L semi-continuous stirred reactor. The variation of adipic acid concentration with reaction time was investigated from 210 to 260℃ with 0.2% (mass) phosphoric acid, 600 L·h-1 ammonia and 1800 r·min-1 stirring speed. When the concentration of adipic acid was higher than or equal to 0.1 mol·L-1 at 250℃, the neutralization reaction was controlled by mass transfer and it was first-order with respect to adipic acid with activation energy of 42.9 kJ·mol-1. When the concentration of adipic acid in the reactor was lower than 0.1 mol·L-1 at 250℃, the reaction was controlled by reaction and it was second-order under reaction control with activation energy of 52.7 kJ·mol-1. The calculation values and experimental results were matched well, and the intrinsic reaction kinetic order with respect to adipic acid was two according to the theoretical model. Besides, at 260℃, 0.2% (mass) phosphoric acid, 1800 r·min-1 stirring speed and the same total pressure (slightly greater than the atmospheric pressure), the variation of adipic acid concentration with reaction time was investigated at a volume flow rate of ammonia between 200 to 600 L·h-1. The results uncovered that the intrinsic reaction kinetic order with respect to ammonia was one.

Key words: adipic acid, ammonia, adiponitrile, reaction kinetics, multiphase reaction, mass transfer

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