Preparation of Pd/γ-Al<sub>2</sub>O<sub>3</sub>/nickel foam monolithic catalyst and its performance for selective hydrogenation in a rotating packed bed reactor

Hai-Long Liao; Bao-Ju Wang; Ya-Zhao Liu; Yong Luo; Jie-Xin Wang; Guang-Wen Chu; Jian-Feng Chen

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Preparation of Pd/γ-Al₂O₃/nickel foam monolithic catalyst and its performance for selective hydrogenation in a rotating packed bed reactor

Catalysis, Kinetics and Reaction Engineering | Updated：2026-01-06

- Preparation of Pd/γ-Al₂O₃/nickel foam monolithic catalyst and its performance for selective hydrogenation in a rotating packed bed reactor
- Preparation of Pd/γ-Al₂O₃/nickel foam monolithic catalyst and its performance for selective hydrogenation in a rotating packed bed reactor
- 中国化学工程学报（英文版） 2022年41卷第1期页码：311-319
- Affiliations：
  
  1. State Key Laboratory of Organic-Inorganic Composites, Beijing University of Chemical Technology,Beijing,China,100029
  2. Research Center of the Ministry of Education for High Gravity Engineering and Technology, Beijing University of Chemical Technology,Beijing,China,100029
- Author bio：
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  中图分类号：
- 纸质出版：2022
- Accepted：
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Hai-Long Liao, Bao-Ju Wang, Ya-Zhao Liu, 等. Preparation of Pd/γ-Al₂O₃/nickel foam monolithic catalyst and its performance for selective hydrogenation in a rotating packed bed reactor[J]. 中国化学工程学报（英文版）, 2022,41(1):311-319.

O
Hai-Long Liao, Bao-Ju Wang, Ya-Zhao Liu, 等. Preparation of Pd/γ-Al₂O₃/nickel foam monolithic catalyst and its performance for selective hydrogenation in a rotating packed bed reactor[J]. 中国化学工程学报（英文版）, 2022,41(1):311-319. DOI：

O DOI：

摘要

Abstract

Selective hydrogenation plays an important role in chemical industries

yet its selectivity is usually limited by the mass transfer. In this work

the enhanced hydrogenation selectivity was achieved in a rotating packed bed (RPB) reactor with excellent mass transfer efficiency. Aiming to be used under the centrifugal filed

a monolithic catalyst Pd/γ-Al

/nickel foam suiting for the shape and size of the rotor of RPB reactor was prepared by the electrophoretic deposition method. The mechanical strength of the catalyst can meet the requirement of high centrifugal force in the RPB. The hydrogenation selectivity in the RPB reactor using the 3-methyl-1-pentyn-3-ol hydrogenation system was 3–8 times higher than that in a stirred tank reactor under similar conditions. This work proves the feasibility of intensifying the selectivity of hydrogenation process in the RPB reactor.

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Preparation of Pd/γ-Al2O3/nickel foam monolithic catalyst and its performance for selective hydrogenation in a rotating packed bed reactor

Preparation of Pd/γ-Al2O3/nickel foam monolithic catalyst and its performance for selective hydrogenation in a rotating packed bed reactor

DOI：

摘要

Abstract

关键词

Keywords

references

Preparation of Pd/γ-Al₂O₃/nickel foam monolithic catalyst and its performance for selective hydrogenation in a rotating packed bed reactor

Preparation of Pd/γ-Al₂O₃/nickel foam monolithic catalyst and its performance for selective hydrogenation in a rotating packed bed reactor