Decomposition of NOxwith Low-Temperature Plasmas at Atmospheric Pressure:  Neat and in the Presence of Oxidants, Reductants, Water, and Carbon Dioxide

1998 ◽  
Vol 102 (41) ◽  
pp. 7954-7963 ◽  
Author(s):  
Jian Luo ◽  
Steven L. Suib ◽  
Manuel Marquez ◽  
Yuji Hayashi ◽  
Hiroshige Matsumoto
Open Physics ◽  
2011 ◽  
Vol 9 (1) ◽  
Author(s):  
Agnieszka Bartecka ◽  
Adam Bacławski ◽  
Józef Musielok

AbstractExperimental Stark broadening studies of the infrared CI transition 3s 1 P 1o − 3p 1 S 0 at 833.5 nm are reported for the first time. A high-current wall-stabilized arc, operated in a mixture of helium, argon, carbon dioxide and hydrogen, was applied as the plasma source. Radiation emitted from homogeneous and optically thin plasma layers was analyzed. Stark broadening studies of the selected CI transition and the hydrogen Balmer β line were performed. As expected from theoretical considerations, the CI line width depends linearly on the electron density of the plasma. Applying theoretical Stark broadening data for the Hgb line, the measured Stark widths of the CI line were calibrated for the purpose of electron density determination in low temperature plasmas.


2021 ◽  
Author(s):  
Jiajie Wang ◽  
Mohammad S. AlQahtani ◽  
Xiaoxing Wang ◽  
Sean D. Knecht ◽  
Sven G. Bilén ◽  
...  

C2+ hydrocarbons are selectively produced in one-step catalytic CO2 conversion via designing the catalyst-bed configuration under non-thermal DBD plasma operating at low temperature and atmospheric pressure.


2013 ◽  
Vol 28 (2) ◽  
pp. 123-135 ◽  
Author(s):  
Mohammed Yousfi ◽  
Nofel Merbahi ◽  
Atul Pathak ◽  
Olivier Eichwald

Author(s):  
P. Ruterana ◽  
P-A. Buffat (I2M) ◽  
K.R Thampi ◽  
M. Graetzel (ICP)

The Ru-RuOx/TiO2 catalyst has been shown to be able to produce methane from hydrogen and carbon dioxide at room temperature and atmospheric pressure at reasonably high rates (TOF: 10-6 at 25C and 10-4 at 90C). The best results were obtained using the P25 support (Degussa 80% anatase and 20% rutile) in the 55-60 m2/g surface area range. The optimal loading for the metal is 3.8% Ru metal.We found that in the most active catalysts, the metal (>90%) is selectively loaded on the rutile crystallites. This distribution shows up clearly in a 500C reduced sample (fig.l) in which the size of the metal particles has increased.


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