scholarly journals Ethane Dehydrogenation on Single and Dual Centers of Ga-modified γ-Al2O3

ACS Catalysis ◽  
2021 ◽  
Vol 11 (3) ◽  
pp. 1380-1391
Author(s):  
Sai Praneet Batchu ◽  
Hsuan-Lan Wang ◽  
Weiqi Chen ◽  
Weiqing Zheng ◽  
Stavros Caratzoulas ◽  
...  
2010 ◽  
Vol 65 (8) ◽  
pp. 2472-2480 ◽  
Author(s):  
N. Hansen ◽  
R. Krishna ◽  
J.M. van Baten ◽  
A.T. Bell ◽  
F.J. Keil

2020 ◽  
Vol 63 (7-8) ◽  
pp. 700-713
Author(s):  
Jinwoong Nam ◽  
Fuat E. Celik

1994 ◽  
Vol 43 (4) ◽  
pp. 555-558
Author(s):  
T. V. Vasina ◽  
O. V. Masloboyshchikova ◽  
O. V. Chetina ◽  
E. G. Khelkovskaya-Sergeeva

Catalysts ◽  
2020 ◽  
Vol 10 (7) ◽  
pp. 807
Author(s):  
Zen Maeno ◽  
Xiaopeng Wu ◽  
Shunsaku Yasumura ◽  
Takashi Toyao ◽  
Yasuharu Kanda ◽  
...  

In this study, the characterization of In-exchanged CHA zeolite (In-CHA (SiO2/Al2O3 = 22.3)) was conducted by in-situ X-ray diffraction (XRD) and ammonia temperature-programmed desorption (NH3-TPD). We also prepared other In-exchanged zeolites with different zeolite structures (In-MFI (SiO2/Al2O3 = 22.3), In-MOR (SiO2/Al2O3 = 20), and In-BEA (SiO2/Al2O3 = 25)) and different SiO2/Al2O3 ratios (In-CHA(Al-rich) (SiO2/Al2O3 = 13.7)). Their catalytic activities in nonoxidative ethane dehydrogenation were compared. Among the tested catalysts, In-CHA(Al-rich) provided the highest conversion. From kinetic experiments and in-situ Fourier transform infrared (FTIR) spectroscopy, [InH2]+ ions are formed regardless of SiO2/Al2O3 ratio, serving as the active sites.


ACS Catalysis ◽  
2020 ◽  
Vol 10 (12) ◽  
pp. 6952-6968 ◽  
Author(s):  
Rui Yao ◽  
José E. Herrera ◽  
Lihang Chen ◽  
Ya-Huei Cathy Chin

Catalysts ◽  
2018 ◽  
Vol 8 (8) ◽  
pp. 296 ◽  
Author(s):  
Shuqi Fang ◽  
Kang Bi ◽  
Qiao Zhang ◽  
Lingpeng Chen ◽  
Yongming Sun ◽  
...  

Layered double hydroxide (LDH) is a layered solid containing positively charged layers with negatively charged anions as an interchangeable interlayer. In this research, Mg(Al)O supports were synthesized with three different Mg:Al molar ratios, and bimetallic PtSn catalysts were loaded onto the supports via the anion exchange method. The properties of ethane dehydrogenation of the PtSn/Mg(Al)O catalysts were investigated. The results show that the structure and properties of the PtSn/Mg(Al)O catalysts were influenced by the Mg:Al molar ratio of the hydrotalcites, which consequently influenced the ethane dehydrogenation performance. When the Mg:Al ratio was 5:1, the ethane dehydrogenation performance was optimal, relative to the Mg:Al ratios of 2:1 and 10:1.


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