Selective oxidation of glycerol over carbon nanofibers supported Pt catalysts in a base-free aqueous solution

2015 ◽  
Vol 59 ◽  
pp. 5-9 ◽  
Author(s):  
Mengyuan Zhang ◽  
Renfeng Nie ◽  
Lina Wang ◽  
Juanjuan Shi ◽  
Weichen Du ◽  
...  
Keyword(s):  
Aqueous Solution ◽  
Carbon Nanofibers ◽  
Selective Oxidation ◽  
Pt Catalysts ◽  
Supported Pt Catalysts

Selective oxidation of glycerol with oxygen in a base-free aqueous solution over MWNTs supported Pt catalysts

2011 ◽  
Vol 106 (3-4) ◽  
pp. 423-432 ◽  
Author(s):  
Dan Liang ◽  
Jing Gao ◽  
Hui Sun ◽  
Ping Chen ◽  
Zhaoyin Hou ◽  
...  
Keyword(s):  
Aqueous Solution ◽  
Selective Oxidation ◽  
Pt Catalysts ◽  
Supported Pt Catalysts

Selective oxidation of glycerol in base-free conditions over N-doped carbon film coated carbon supported Pt catalysts

2017 ◽  
Vol 101 ◽  
pp. 107-110 ◽  
Author(s):  
Lihua Yang ◽  
Xuewen Li ◽  
Yanyan Sun ◽  
Linhai Yue ◽  
Jie Fu ◽  
...  
Keyword(s):  
Selective Oxidation ◽  
Carbon Film ◽  
Pt Catalysts ◽  
Supported Pt Catalysts ◽  
Coated Carbon

Remarkable promoting effects of BiOCl on the room-temperature selective oxidation of benzyl alcohol over supported Pt catalysts

2018 ◽  
Vol 42 (11) ◽  
pp. 8979-8984 ◽  
Author(s):  
Juanjuan Liu ◽  
Feng Han ◽  
Lingze Chen ◽  
Linfang Lu ◽  
Shihui Zou ◽  
...  
Keyword(s):  
Benzyl Alcohol ◽  
Selective Oxidation ◽  
Room Temperature ◽  
Catalytic Performance ◽  
Pt Catalysts ◽  
Oxidation Of Benzyl Alcohol ◽  
Supported Pt Catalysts

BiOCl, in addition to traditional Bi metal, could remarkably promote the catalytic performance of Pt/MOx in the selective oxidation of benzyl alcohol.

Selective oxidation of glycerol in a base-free aqueous solution over different sized Pt catalysts

2009 ◽  
Vol 10 (12) ◽  
pp. 1586-1590 ◽  
Author(s):  
Dan Liang ◽  
Jing Gao ◽  
Junhua Wang ◽  
Ping Chen ◽  
Zhaoyin Hou ◽  
...  
Keyword(s):  
Aqueous Solution ◽  
Selective Oxidation ◽  
Pt Catalysts

Metal foam supported Pt catalysts for the selective oxidation of CO in hydrogen

2005 ◽  
Vol 281 (1-2) ◽  
pp. 1-9 ◽  
Author(s):  
Amornmart Sirijaruphan ◽  
James G. Goodwin ◽  
Richard W. Rice ◽  
Dongguang Wei ◽  
Kenneth R. Butcher ◽  
...  
Keyword(s):  
Selective Oxidation ◽  
Metal Foam ◽  
Pt Catalysts ◽  
Oxidation Of Co ◽  
Supported Pt Catalysts

scholarly journals Influence of the Reduction Temperature and the Nature of the Support on the Performance of Zirconia and Alumina-Supported Pt Catalysts for n-Dodecane Hydroisomerization

Catalysts ◽  
2021 ◽  
Vol 11 (1) ◽  
pp. 88
Author(s):  
Diana García-Pérez ◽  
Maria Consuelo Alvarez-Galvan ◽  
Jose M. Campos-Martin ◽  
Jose L. G. Fierro
Keyword(s):  
Catalytic Activity ◽  
Surface Area ◽  
Catalytic Properties ◽  
Catalytic Performance ◽  
Major Influence ◽  
Pt Catalysts ◽  
Reduction Temperature ◽  
Metal Dispersion ◽  
Tungsten Oxides ◽  
Supported Pt Catalysts

Catalysts based on zirconia- and alumina-supported tungsten oxides (15 wt % W) with a small loading of platinum (0.3 wt % Pt) were selected to study the influence of the reduction temperature and the nature of the support on the hydroisomerization of n-dodecane. The reduction temperature has a major influence on metal dispersion, which impacts the catalytic activity. In addition, alumina and zirconia supports show different catalytic properties (mainly acid site strength and surface area), which play an important role in the conversion. The NH3-TPD profiles indicate that the acidity in alumina-based catalysts is clearly higher than that in their zirconia counterparts; this acidity can be attributed to a stronger interaction of the WOx species with alumina. The PtW/Al catalyst was found to exhibit the best catalytic performance for the hydroisomerization of n-dodecane based on its higher acidity, which was ascribed to its larger surface area relative to that of its zirconia counterparts. The selectivity for different hydrocarbons (C7–10, C11 and i-C12) was very similar for all the catalysts studied, with branched C12 hydrocarbons being the main products obtained (~80%). The temperature of 350 °C was clearly the best reduction temperature for all the catalysts studied in a trickled-bed-mode reactor.

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