546681 Improved Stability of Ptsn for Propane Dehydrogenation By Boron-Modified ZrO2 Support

Monday, June 3, 2019: 11:51 AM
Republic ABC (Grand Hyatt San Antonio)
Zhonghai Ji, Xiulian Pan and Xinhe Bao, Dalian Institute of Chemical Physics, Chinese Academy of Sciences, Dalian, China

Improved stability of PtSn for propane dehydrogenation by boron-modified ZrO2 support

Zhonghai Ji, Xiulian Pan, Xinhe Bao,

State Key Laboratory of Catalysis, Dalian Institute of Chemical Physics, Chinese Academy of Sciences, Dalian 116023, Peoples Republic of China. Email: panxl@dicp.ac.cn; xhbao@dicp.ac.cn 

PtSn based catalysts are widely used in propane dehydrogenation (PDH)[1-5]. Since it involves noble metal, it is highly desirable to reduce the usage of Pt without degrading the catalytic performance. However, the catalyst stability is apt to deterioration with decreasing Pt content [1]. In this contribution, we demonstrate that the B modified ZrO2 as a support can enhance the stability of PtSn catalyst.

Boron modified ZrO2 (B-ZrO2) was prepared by co-precipitation. PtSn/B-ZrO2 and PtSn/Al2O3 was prepared by the incipient-wetness impregnation method. Reaction was conducted under nonoxidative conditions at 550 oC, weight hourly space velocity (WHSV) of propane 3 h-1. Results in Fig. 1 show that the initial propane conversion is 32.4% for PtSn/ZrO2, 36.0% for PtSn/B-ZrO2 and 42.2% for PtSn/Al2O3. However, the propylene selectivity is lowest on PtSn/Al2O3. The deactivation rate constant (kd) is 0.08 h-1 over PtSn/ZrO2 and 0.04 h-1 over PtSn/Al2O3 whereas it is only 0.01 h-1 over PtSn/B-ZrO2. The stability of PtSn/B-ZrO2 is obviously better than that of 0.35wt% PtSn/Al2O3 and PtSn/ZrO2. Characterization by NH3-TPD and pyridine IR shows that Lewis acid is present on B-ZrO2. XPS indicates that the presence of even a small amount of boron stabilizes the oxidation state of Sn, which may play an important role. More detailed discussions will be given in the presentation.

Fig. 1 Catalytic performance in propane dehydrogenation on various catalysts.

References

[1] X. Liu, W.-Z. Lang, L.-L. Long, C.-L. Hu, L.-F. Chu, Y.-J. Guo, Chem. Eng. J. 247 (2014). 183-192.

[2] J. Li, J. Li, Z. Zhao, X. Fan, J. Liu, Y. Wei, A. Duan, Z. Xie, Q. Liu, J. Catal., 352 (2017). 361-370.

[3] A. Iglesias-Juez, A.M. Beale, K. Maaijen, T.C. Weng, P. Glatzel, B.M. Weckhuysen, J. Catal., 276 (2010). 268-279.

[4] G.-Q. Ren, G.-X. Pei, Y.-J. Ren, K.-P. Liu, Z.-Q. Chen, J.-Y. Yang, Y. Su, X.-Y. Liu, W.-Z. Li, T. Zhang, J. Catal., 366 (2018).115-126.

[5 L. Shi, G.-M. Deng, W.-C. Li, S. Miao, Q.-N. Wang, W.-P. Zhang, A.-H. Lu, Angew. Chem.

Int. Ed.ion, 54 (2015). 13994-13998.


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