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For almost a century vanadium oxide based catalysts have been the dominant materials in industrial processes for sulfuric acid production.
Co based catalysts have been widely investigated as the catalysts for carbon dioxide reforming of methane (CRM) reaction due to outstanding coke-resistant capacity.
Uranium oxide based catalysts have been investigated for the oxidative destruction of volatile organic compounds (VOCs) to carbon oxides and water.
A series of molybdena based catalysts have been tested for the selective oxidation of methane at ambient pressure, with N2O as oxidant.
Ru + Ag/US-Y and Ru + Co/US-Y based catalysts have been studied for their catalytic activity towards N2O decomposition, a reaction of current environmental importance.
Non-Pt based catalysts have been considered as the most promising materials to replace conventional catalysts, recent findings showed possibility to practical commercial applications such as Fe N/C, FePhen@MOF, and N-doped CNT.
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The Co-Ni bimetal based catalysts had been considered as promising candidates for the CO2 reforming of CH4 reaction due to the Co-Ni synergistic effect.
The reaction of n-butane with 'reactor-equilibrated' (VO 2P207 based catalysts has been investigated using a combination of low-pressure transient response experiments and atmospheric-pressure steady-flow reaction experiments.
Ageing tests of a La-Sr based catalyst have been performed at 870°C, at different apparent contact times, with a feed of the same composition.
A clearer understanding concerning the isospecific nature of active sites on the donor-free TiCl3 – based catalyst has been presented in this work in terms of both surface characteristics of the catalyst and microstructure of polypropylene (PP) produced.
In summary, a host of inorganic solid base catalysts have been developed for the low temperature transesterification of triglyceride components of bio-oil feedstocks, offering activities far superior to those achieved via alternative solid acid catalysts to date.
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