Inorganic Chemicals Industry ›› 2022, Vol. 54 ›› Issue (12): 148-154.doi: 10.19964/j.issn.1006-4990.2022-0181

• Catalytic Materials • Previous Articles    

Effect of copper-based catalyst structure on olefin aldehyde hydrogenation in trickle bed and fixed bubbling bed

SONG Bingjie1,2(),CHEN He3,SUN Peiyong1,2,CHAI Wenzheng3,ZHANG Shenghong1,2,FU Songbao3,YAO Zhilong1,2()   

  1. 1. College of New Materials and Chemical Engineering,Beijing Institute of Petrochemical Technology,Beijing 102617,China
    2. Beijing Key Laboratory of Enze Biomass Fine Chemical
    3. Research Institute of Refining and Petrochemicals,CNOOC
  • Received:2022-06-01 Online:2022-12-10 Published:2022-12-19
  • Contact: YAO Zhilong E-mail:516821902@qq.com;yaozl@bipt.edu.cn

Abstract:

Copper-silicon,copper-chromium and copper-zinc composite oxide catalysts with different compositions were prepared by coprecipitation method.The physicochemical properties and pore structure of the copper-based composite oxide catalysts were characterized by X-ray diffraction(XRD),temperature-programmed reduction by H2(H2-TPR),N2 adsorption-desorption(BET) and potentiometric titration with n-butylamine.The hydrogenation of 2-propyl-2-heptenal catalyzed by the three copper-based composite oxide catalysts with different compositions in trickle bed and fixed bubbling bed was investigated.The results showed that there was no positive correlation between the difference of copper crystal size and surface acid content on the three copper-based composite oxide catalysts and the catalytic performance of 2-propyl-2-heptenal hydrogenation.The fixed bubbling bed reactor was better than trickle bed reactor for olefin aldehyde hydrogenation catalyzed by catalysts with abundant macropore.

Key words: olefin aldehyde, hydrogenation, trickle bed reactor, fixed bubbling bed, copper-based catalyst

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