Hydrodeoxygenation of stearic acid using Mo modified Ni and Co/alumina catalysts: Effect of calcination temperature

2019 ◽  
Vol 207 (7) ◽  
pp. 904-919 ◽  
Author(s):  
Pankaj Kumar ◽  
Sunil K. Maity ◽  
Debaprasad Shee
1995 ◽  
Vol 12 (3) ◽  
pp. 221-229 ◽  
Author(s):  
S.A. El-Hakam

The effect of heat treatment of manganese oxide/alumina catalysts of various manganese content on the structural and textural properties and the catalytic decomposition of hydrogen peroxide were investigated. The FT-IR results have shown that depending on the calcination temperature and metal loading MnO2 and MnO3 are formed on the investigated samples. No spinel structure was detected under the experimental conditions. The surface areas were found to decrease with increasing calcination temperature and metal content up to 30 wt.% Mn. The mean pore radius increased with both calcination temperature and Mn content. The rate of catalytic decomposition of H2O2 was found to depend on the pH, the calcination temperature and the state of Mn on the catalyst surface.


2017 ◽  
Vol 316 ◽  
pp. 401-409 ◽  
Author(s):  
Klara Jeništová ◽  
Imane Hachemi ◽  
Päivi Mäki-Arvela ◽  
Narendra Kumar ◽  
Markus Peurla ◽  
...  

1996 ◽  
Vol 59 (1) ◽  
pp. 15-18 ◽  
Author(s):  
Katsuhiko Tahara ◽  
Eiji Nagahara ◽  
Yasushi Itoi ◽  
Satoru Nishiyama ◽  
Shigeru Tsuruya ◽  
...  

1986 ◽  
Vol 3 (2) ◽  
pp. 95-108 ◽  
Author(s):  
J. R. González-Velasco ◽  
J. A. González-Marcos ◽  
J. I. Gutiérrez-Ortiz ◽  
A. Romero

Factorial and rotational designs have been used to analyse the effect of each preparative variable on the surface acid strength distribution in silica-alumina catalysts. Relationships between the surface acidities at p Ka = 2·8, 3·3 and 4·8 and the most important variables, namely precipitation rate and temperature, drying pressure and temperature, impregnation concentration and calcination temperature have been obtained.


1992 ◽  
Vol 57 (10) ◽  
pp. 2073-2077 ◽  
Author(s):  
Khaliq Ahmed ◽  
Pronab Mistry

Alumina-supported nickel catalysts prepared by the methods of impregnation and coprecipitation and heated at four different temperatures showed that the optimal calcination temperature for both types of catalysts lies in the region of 623-673 K. Crystallite size measurements by XRD revealed that coprecipitated samples have larger crystallites than the impregnated samples. The total surface areas measured by nitrogen adsorption and the results of metal area measurements made by hydrogen adsorption are in agreement with the crystallite size results.


2015 ◽  
Vol 30 (2) ◽  
pp. 189
Author(s):  
LIU Shi-Xin ◽  
LI Xiao-Song ◽  
DENG Xiao-Qing ◽  
SUN Zhi-Guang ◽  
ZHU Ai-Min

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