Hydrogenation of high-concentration monovinylacetylene for butadiene production over Pd-Pb/SiO2 catalysts

被引:0
|
作者
Zhang Y. [1 ]
Jia Z. [1 ]
Zhang S. [1 ]
Zhen B. [1 ,2 ]
Han M. [1 ]
机构
[1] Department of Chemical Engineering, Tsinghua University, Beijing
[2] College of Chemistry and Chemical Engineering, Tianjin University of Technology, Tianjin
来源
Han, Minghan (hanmh@tsinghua.edu.cn) | 2016年 / Materials China卷 / 67期
关键词
Butadiene; Catalysis; Catalysts; Hydrogenation; Monovinylacetylene;
D O I
10.11949/j.issn.0438-1157.20160160
中图分类号
学科分类号
摘要
The hydrogenation of high-concentration monovinylacetylene over silica supported Pd-Pb bimetallic catalysts was investigated. It showed that the appropriate presence of Pb can prevent Pd nanoparticles from aggregation, hence facilitated the improvement of catalytic activity, i.e. the optimal molar ratio of Pb to Pd of 0.2. With the molar ratio of Pb to Pd above 0.2, Pd-Pb alloy can be formed, which causes catalytic activity loss. The positive correlation between the catalytic activity and the electron bonding energy of Pd 3d was manifested by X-ray photoelectron spectra. The temperature for PdO reduction exhibited a remarkable influence on the structure and the activity of the catalysts. The PdO reduction at 350℃ of the catalyst was incomplete thus with low activity. At 450℃ of the reduction temperature, it caused Pd nanoparticle sintering, hence with low activity and low butadiene selectivity. As a result, the optimal reduction temperature was 400℃. After 40 h, the catalyst was deactivated due to the blockage of pore by coke formation on catalyst surface. Subsequently, the improvement of anti-coking ability and the lifetime of the catalyst will be of interest. © All Right Reserved.
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页码:2793 / 2798
页数:5
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共 24 条
  • [1] Zhang L., Tian J., Liu B., Study on reaction process for oxidative dehydrogenation of 1-butene to butadiene, Nat. Gas. Chem. Ind., 40, 4, pp. 15-18, (2015)
  • [2] Zeng S.J., Tian X., Dong H.F., Et al., Selection and separation performance of ionic liquid as additive in butadiene extraction with CAN, CIESC Journal, 65, 6, pp. 2120-2129, (2014)
  • [3] Chang H., Tong L., Li G.R., Et al., Suggestions for application and development of butadiene production technology, Mod. Chem. Ind., 33, 5, pp. 8-12, (2013)
  • [4] Lynch M., Manufacture and use of chloroprene monomer, Chem-Biol. Interact., 135-136, pp. 155-167, (2001)
  • [5] Liu J.G., Zuo Y.Z., Han M.H., Et al., Stability improvement of the Nieuwland catalyst in the dimerization of acetylene to monovinylacetylene, J. Nat. Gas Chem., 21, 5, pp. 495-500, (2012)
  • [6] Liu J.G., Zuo Y.Z., Han M.H., Et al., Improvement of anhydrous catalyst stability in acetylene dimerization by regulating acidity, J. Chem. Technol. Biotechnol., 88, 3, pp. 408-414, (2013)
  • [7] Liu J.G., Han M.H., Wang Z.W., Effect of solvent on catalytic performance of anhydrous catalyst in acetylene dimerization to monovinylacetylene, J. Energy Chem., 22, 4, pp. 599-604, (2013)
  • [8] Molnar A., Sarkany A., Monika V., Hydrogenation of carbon-carbon multiple bonds: chemo-, regio-and stereo-selectivity, J. Mol. Catal. A-Chem., 173, 1-2, pp. 185-221, (2001)
  • [9] Bridier B., Karhanek D., Perez-Ramirez J., Et al., Molecular understanding of enyne hydrogenation over palladium and copper catalysts, ChemCatChem, 4, 9, pp. 1420-1427, (2012)
  • [10] Crespo-Quesada M., Cardenas-Lizana F., Dessimoz A.L., Et al., Modern trends in catalyst and process design for alkyne hydrogenations, ACS Catal., 2, 8, pp. 1773-1786, (2012)