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This paper developed a new clean continuous process for the hydrogenation of 3,5-dimethylpyridine(DPY) to 3,5-dimethylpiperidine (DPI) without solvent.A series of Ru/C catalysts were prepared by impregnation method,which were characterized by the BET,ICP,CO chemisorptions,XRD,SEM,EDS,TEM and TG.The effect of active species,loading,catalyst support,reaction temperature and pressure on the catalytic performance was investigated.The influence of internal and external diffusion in the trickle-bed reactor (TBR) was basically eliminated by adjusting the particle size and dosage of the Ru/C catalyst.The reaction performance of the hydrogenation of DPY to DPI in the TBR and kettle reactor(KR) was compared,and the superiority of the TBR process was analyzed.The results show that this new continuous process developed in this study is an efficient way to realize the hydrogenation of DPY to DPI,and has a good industrial application prospect.
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篇名 Development of a new continuous process for the production of 3,5-dimethylpiperidine
来源期刊 中国化学工程学报(英文版) 学科
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年,卷(期) 2022,(1) 所属期刊栏目 Catalysis,Kinetics and Reaction Engineering
研究方向 页码范围 374-383
页数 10页 分类号
字数 语种 英文
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中国化学工程学报(英文版)
月刊
1004-9541
11-3270/TQ
大16开
北京东城区青年湖南街13号
80-448
1982
eng
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4237
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1
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