Heterogeneous Catalytic Reduction of Tertiary Amides with Hydrosilanes Using Unsupported Nanoporous Gold Catalyst

2019 ◽  
Vol 361 (20) ◽  
pp. 4817-4824
Author(s):  
Yuhui Zhao ◽  
Sheng Zhang ◽  
Yoshinori Yamamoto ◽  
Ming Bao ◽  
Tienan Jin ◽  
...  
2020 ◽  
Vol 9 (2) ◽  
pp. 99-104
Author(s):  
Zhen Qi ◽  
Monika M. Biener ◽  
Ajay R. Kashi ◽  
Sara Hunegnaw ◽  
Alvin Leung ◽  
...  

RSC Advances ◽  
2017 ◽  
Vol 7 (72) ◽  
pp. 45344-45350 ◽  
Author(s):  
C. Rumancev ◽  
A. R. von Gundlach ◽  
S. Baier ◽  
A. Wittstock ◽  
J. Shi ◽  
...  

Soft X-ray SAXS and ASAXS reveal nanostructural properties and temperature induced morphological changes in catalyst materials. The stabilizing effect of cerium oxide deposits on the gold catalyst and the morphological properties of the cerium oxide were determined.


2020 ◽  
Vol 11 (1) ◽  
Author(s):  
Yafei Sun ◽  
Yueqiang Cao ◽  
Lili Wang ◽  
Xiaotong Mu ◽  
Qingfei Zhao ◽  
...  

Abstract Supported gold nanoparticles are emerging catalysts for heterogeneous catalytic reactions, including selective hydrogenation. The traditionally used supports such as silica do not favor the heterolytic dissociation of hydrogen on the surface of gold, thus limiting its hydrogenation activity. Here we use gold catalyst particles partially embedded in the pore walls of mesoporous carbon with carbon atoms occupying interstitial sites in the gold lattice. This catalyst allows improved electron transfer from carbon to gold and, when used for the chemoselective hydrogenation of 3-nitrostyrene, gives a three times higher turn-over frequency (TOF) than that for the well-established Au/TiO2 system. The d electron gain of Au is linearly related to the activation entropy and TOF. The catalyst is stable, and can be recycled ten times with negligible loss of both reaction rate and overall conversion. This strategy paves the way for optimizing noble metal catalysts to give an enhanced hydrogenation catalytic performance.


2018 ◽  
Vol 24 (59) ◽  
pp. 15777-15780 ◽  
Author(s):  
Rahul D. Kavthe ◽  
Yoshifumi Ishikawa ◽  
Indra Kusuma ◽  
Naoki Asao

2019 ◽  
Vol 6 (4) ◽  
pp. 595-602
Author(s):  
Wei Xie ◽  
Daming Liang ◽  
Lanting Li ◽  
Sijian Qu ◽  
Wu Tao

Abstract In order to study the mechanism of selective catalytic reduction of activated coke to remove NO in low-temperature flue gas and provide some theoretical basis for the development of related technologies. The pore size distribution and BET specific surface area of AC were obtain by data analyzing of N2 adsorption/desorption isotherm at − 196 °C and carbon matrix and surface chemistry of virgin activated coke samples were characterized by acid–base titration and XPS. The process of selective catalytic reduction of activated coke (AC) samples with NH3 as reducing agent was studied in a fixed bed reactor at 150 °C. The result shows that pore size distribution or BET specific surface of activated cokes have not correlation with denitrification activity for SCR. The NO reduction activities of the activated cokes are apparent to increase with their surface oxygen element content and total amount of acidic sites. Obviously there is good linear relationship between the NH3 adsorption capacity and activity for SCR with linear correlation coefficient 0.943. It has been presented that adsorption of NH3 on acidic functional groups in the edge of large polycyclic aromatic ring of activated coke is key rate controlling step in the SCR heterogeneous catalytic reaction.


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