SCI和EI收录∣中国化工学会会刊

Chin.J.Chem.Eng. ›› 2018, Vol. 26 ›› Issue (7): 1499-1507.DOI: 10.1016/j.cjche.2018.01.020

• Catalysis, kinetics and reaction engineering • Previous Articles     Next Articles

Optimal reaction conditions for pyridine synthesis in riser reactor

Shuaishuai Zhou1, Zelong Liu2, Xiao Yan1, Qin Di1, Mengxi Liu1, Chunxi Lu1, Guangzhou Jin2   

  1. 1 State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing 102249, China;
    2 Department of Chemical Engineering, Beijing Institute of Petro-Chemical Technology, Beijing 102617, China
  • Received:2017-11-04 Revised:2018-01-30 Online:2018-08-16 Published:2018-07-28
  • Contact: Chunxi Lu,E-mail addresses:lcx725@sina.com;Guangzhou Jin,E-mail addresses:jinguangzhou@bipt.edu.cn
  • Supported by:

    Supported by the National Basic Research Program of China (973 Program, 2012CB215000).

Optimal reaction conditions for pyridine synthesis in riser reactor

Shuaishuai Zhou1, Zelong Liu2, Xiao Yan1, Qin Di1, Mengxi Liu1, Chunxi Lu1, Guangzhou Jin2   

  1. 1 State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing 102249, China;
    2 Department of Chemical Engineering, Beijing Institute of Petro-Chemical Technology, Beijing 102617, China
  • 通讯作者: Chunxi Lu,E-mail addresses:lcx725@sina.com;Guangzhou Jin,E-mail addresses:jinguangzhou@bipt.edu.cn
  • 基金资助:

    Supported by the National Basic Research Program of China (973 Program, 2012CB215000).

Abstract: Pyridine has been generally synthesized by aldehydes and ammonia in a turbulent fluidized-bed reactor. In this paper, a novel riser reactor was proposed for pyridine synthesis. Experiment result showed that the yield of pyridine and 3-picoline decreased, but the selectivity of pyridine over 3-picoline increased compared to turbulent fluidized-bed reactor. Based on experimental data, a modified kinetic model was used for the determination of optimal operating condition for riser reactor. The optimal operating condition of riser reactor given by this modified model was as follows:The reaction temperature of 755 K, catalyst to feedstock ratio (CTFR) of 87, residence time of 3.8 s and initial acetaldehydes concentration of 0.0029 mol·L-1 (acetaldehydes to formaldehydes ratio by mole (ATFR) of 0.65 and ammonia to aldehydes ratio by mole (ATAR) of 0.9, water contention of 63wt% (formaldehyde solution)).

Key words: Pyridine synthesis, Riser reactor, Optimal operating condition

摘要: Pyridine has been generally synthesized by aldehydes and ammonia in a turbulent fluidized-bed reactor. In this paper, a novel riser reactor was proposed for pyridine synthesis. Experiment result showed that the yield of pyridine and 3-picoline decreased, but the selectivity of pyridine over 3-picoline increased compared to turbulent fluidized-bed reactor. Based on experimental data, a modified kinetic model was used for the determination of optimal operating condition for riser reactor. The optimal operating condition of riser reactor given by this modified model was as follows:The reaction temperature of 755 K, catalyst to feedstock ratio (CTFR) of 87, residence time of 3.8 s and initial acetaldehydes concentration of 0.0029 mol·L-1 (acetaldehydes to formaldehydes ratio by mole (ATFR) of 0.65 and ammonia to aldehydes ratio by mole (ATAR) of 0.9, water contention of 63wt% (formaldehyde solution)).

关键词: Pyridine synthesis, Riser reactor, Optimal operating condition