Ni as the promoter on hydrogen spillover for better hydrogenative regeneration on Pt/Y based catalysts

被引:26
作者
Ren, Kui [1 ]
Jia, Fuxian [1 ]
Zhang, Chengxi [1 ]
Xing, Enhui [1 ]
Li, Yongxiang [1 ]
机构
[1] Sinopec, Res Inst Petr Proc, State Key Lab Catalyt Mat & React Engn, Beijing 100083, Peoples R China
基金
中国国家自然科学基金; 国家重点研发计划;
关键词
Isobutane; Butene; Solid acid alkylation; Hydrogen spillover; Hydrogenative regeneration; HIGHLY DISPERSED NOBLE; ETHYLENE-GLYCOL; REDUCTIVE AMINATION; CARBON NANOTUBES; LOW-TEMPERATURE; X ZEOLITES; METAL; ADSORPTION; CO2; DEACTIVATION;
D O I
10.1016/j.fuel.2022.127047
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Hydrogenative regeneration of Pt/YA catalysts is vital to continuous operation of solid acid isobutane/butene alkylation. From the view of H2 activation, the mechanism of hydrogenative regeneration was investigated experimentally and theoretically. Herein with Pt/YA as reference, (Ni-Pt)/YA catalysts were prepared with almost identical cell parameter and different Ni/Pt contents by wet impregnation method following by several characterization methods, such as XPS, H2-TPR, H2-TPD, STEM-CS and Elemental mapping. Strong interactions between Ni and Pt were proven by XPS and H2-TPR. Moreover Ni can increase the capability of hydrogen spillover, which could be observed by H2-TPD, with the higher desorption temperature and more desorbed H2. DFT calculations revealed that hydrogen spillover is the rate determining step for the overall H2 activation over Pt/YA, and Ni as the hydrogen spillover promoter could couple with Pt to enhance the overall H2 activation because of almost 30% lower energy barrier for hydrogen spillover. With rather low Pt content, no obvious loss in lifetime in the 10 cycles of reaction-regeneration was observed over (5Ni-0.1Pt)/YA with rather stable product distribution.
引用
收藏
页数:9
相关论文
共 62 条
[31]   Hydrogen production from glycerol steam reforming over nickel catalysts supported on alumina and niobia: Deactivation process, effect of reaction conditions and kinetic modeling [J].
Menezes, Joao Paulo da S. Q. ;
Manfro, Robinson L. ;
Souza, Mariana M. V. M. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2018, 43 (32) :15064-15082
[32]   HYDROGEN TEMPERATURE-PROGRAMMED DESORPTION (H-2 TPD) OF SUPPORTED PLATINUM CATALYSTS [J].
MILLER, JT ;
MEYERS, BL ;
MODICA, FS ;
LANE, GS ;
VAARKAMP, M ;
KONINGSBERGER, DC .
JOURNAL OF CATALYSIS, 1993, 143 (02) :395-408
[33]   Ethanol conversion at low temperature over CeO2-Supported Ni-based catalysts. Effect of Pt addition to Ni catalyst [J].
Moraes, Tamara Siqueira ;
Rabelo Neto, Raimundo Crisostomo ;
Ribeiro, Mauro Celso ;
Mattos, Lisiane Veiga ;
Kourtelesis, Marios ;
Ladas, Spyros ;
Verykios, Xenophon ;
Noronha, Fabio B. .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2016, 181 :754-768
[34]   Hydrogen spillover in the Fischer-Tropsch synthesis: An analysis of gold as a promoter for cobalt-alumina catalysts [J].
Nabaho, Doreen ;
Niemantsverdriet, J. W. ;
Claeys, Michael ;
van Steen, Eric .
CATALYSIS TODAY, 2016, 275 :27-34
[35]   New mechanism insights into methane steam reforming on Pt/Ni from DFT and experimental kinetic study [J].
Niu, Juntian ;
Wang, Yalan ;
Qi, Yanying ;
Dam, Anh H. ;
Wang, Hongmin ;
Zhu, Yi-An ;
Holmen, Anders ;
Ran, Jingyu ;
Chen, De .
FUEL, 2020, 266
[36]  
Nivarthy G.S., 2000, STUDIES SURFACE SCI, P2561, DOI DOI 10.1016/S0167-2991(00)80855-1
[37]   Contribution of spillover effects to heterogeneous catalysis [J].
Pajonk, GM .
APPLIED CATALYSIS A-GENERAL, 2000, 202 (02) :157-169
[38]   CO2 adsorption and activation over γ-Al2O3-supported transition metal dimers: A density functional study [J].
Pan, Yun-xiang ;
Liu, Chang-jun ;
Wiltowski, Tomasz S. ;
Ge, Qingfeng .
CATALYSIS TODAY, 2009, 147 (02) :68-76
[39]   Adsorption and Protonation Of CO2 on Partially Hydroxylated γ-Al2O3 Surfaces: A Density Functional Theory Study [J].
Pan, Yunxiang ;
Liu, Chang-jun ;
Ge, Qingfeng .
LANGMUIR, 2008, 24 (21) :12410-12419
[40]  
Perdew JP, 1997, PHYS REV LETT, V78, P1396, DOI 10.1103/PhysRevLett.77.3865