Production of hydrogen and nanofibrous carbon by selective catalytic decomposition of propane

2009 ◽  
Vol 34 (3) ◽  
pp. 1310-1323 ◽  
Author(s):  
E SOLOVYEV ◽  
D KUVSHINOV ◽  
D ERMAKOV ◽  
G KUVSHINOV
Materials ◽  
2021 ◽  
Vol 14 (12) ◽  
pp. 3258
Author(s):  
Hamed M. Alshammari ◽  
Mohammad Hayal Alotaibi ◽  
Obaid F. Aldosari ◽  
Abdulellah S. Alsolami ◽  
Nuha A. Alotaibi ◽  
...  

The present study investigates a process for the selective production of hydrogen from the catalytic decomposition of formic acid in the presence of iridium and iridium–palladium nanoparticles under various conditions. It was found that a loading of 1 wt.% of 2% palladium in the presence of 1% iridium over activated charcoal led to a 43% conversion of formic acid to hydrogen at room temperature after 4 h. Increasing the temperature to 60 °C led to further decomposition and an improvement in conversion yield to 63%. Dilution of formic acid from 0.5 to 0.2 M improved the decomposition, reaching conversion to 81%. The reported process could potentially be used in commercial applications.


2017 ◽  
Vol 197 ◽  
pp. 41-57 ◽  
Author(s):  
Saeedeh S. Tafreshi ◽  
Alberto Roldan ◽  
Nora H. de Leeuw

Hydrazine (N2H4) is produced at industrial scale from the partial oxidation of ammonia or urea. The hydrogen content (12.5 wt%) and price of hydrazine make it a good source of hydrogen fuel, which is also easily transportable in the hydrate form, thus enabling the production of H2in situ. N2H4 is currently used as a monopropellant thruster to control and adjust the orbits and altitudes of spacecrafts and satellites; with similar procedures applicable in new carbon-free technologies for power generators, e.g. proton-exchange membrane fuel cells. The N2H4 decomposition is usually catalysed by the expensive Ir/Al2O3 material, but a more affordable catalyst is needed to scale-up the process whilst retaining reaction control. Using a complementary range of computational tools, including newly developed micro-kinetic simulations, we have derived and analysed the N2H4 decomposition mechanism on the Cu(111) surface, where the energetic terms of all states have been corrected by entropic terms. The simulated temperature-programmed reactions have shown how the pre-adsorbed N2H4 coverage and heating rate affect the evolution of products, including NH3, N2 and H2. The batch reactor simulations have revealed that for the scenario of an ideal Cu terrace, a slow but constant production of H2 occurs, 5.4% at a temperature of 350 K, while the discharged NH3 can be recycled into N2H4. These results show that Cu(111) is not suitable for hydrogen production from hydrazine. However, real catalysts are multi-faceted and present defects, where previous work has shown a more favourable N2H4 decomposition mechanism, and, perhaps, the decomposition of NH3 improves the production of hydrogen. As such, further investigation is needed to develop a general picture.


In recent years hydrogen production received enormous attention, since it is an environmentally friendly, energy source. The aim of this research was to examine the hydrogen production with the help of methane’s catalytic decomposition. 30% Fe coupled with different % of Co over alumina support, were examined by catalytic decomposition of methane for the production of hydrogen. The catalysts were prepared by impregnation method. The catalytic activity results revealed that the catalysts, coupled 15% Co gave the highest conversion of 72.5% as depicted by the three hour time on stream profile. The fresh and spent catalysts were characterized using different techniques such as BET, H2-TPR, and XRD.


2014 ◽  
Vol 625 ◽  
pp. 275-279 ◽  
Author(s):  
Wasim Ullah Khan ◽  
Anis Hamza Fakeeha ◽  
Ahmed Sadeq Al-Fatish ◽  
Muhammad Awais Naeem ◽  
Ahmed Ibrahim Aidid ◽  
...  

Catalytic decomposition of methane was investigated over nickel and cobalt based mono-and bimetallic catalysts for the production of hydrogen and filamentous carbon. Catalysts with different Ni to Co ratios supported on La2O3were prepared by co-precipitation method. The activity test and characterization results revealed that the catalyst containing 15wt% Ni and 10wt% Co over La2O3support presented relatively better catalytic performance among all the tested catalyst. The catalysts were characterized by BET, TGA and temperature programmed reduction (TPR).


2015 ◽  
Vol 2 (1) ◽  
pp. 71-82 ◽  
Author(s):  
Anis Hamza Fakeeha ◽  
Ahmed Aidid Ibrahim ◽  
Muhammad Awais Naeem ◽  
Wasim Ullah Khan ◽  
Ahmed Elhag Abasaeed ◽  
...  

AbstractProduction of hydrogen, being an environmentally friendly energy source, has gained a lot of attention in the recent years. In this article, iron-based catalysts, with different active metal loadings, supported over magnesia and titania are investigated for hydrogen production via catalytic decomposition of methane. The catalytic activity and stability results revealed that magnesia supported catalysts performed better than titania supported catalysts. Hydrogen reduction temperature of 500°C was obtained suitable for catalyst activation. For magnesia supported catalysts, only higher loadings i.e., 30% and 40% Fe-Mg catalysts showed reasonable activity, while all titania supported catalysts presented less activity as well as deactivation. Among all the catalysts, 30% Fe/MgO catalyst displayed better activity. The formation of carbon nanofibers was evidenced from morphological analysis. FESEM and TEM images showed the generation of nonuniform carbon nanofibers with broader diameter. The catalysts were characterized using different techniques such as BET, H2-TPR, O2-TPO, XRD, TGA, FESEM and TEM.


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