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This information is required to determine the appropriate operating conditions for achieving maximum syngas yields from these fuels.
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The reactor design was shown to be effective for the pyrolysis and catalytic steam reforming of biomass with a maximum syngas yield of 54.0 wt.% produced when the sol gel prepared NiO/SiO2 catalyst was used, which had the highest surface area of 765 m2 g−1.
Gasification temperature has been optimized for maximum syngas production.
Study shows that the best performance in term of CHP does not simultaneously ensure maximum syngas production.
The catalysts show syngas yields significantly exceeding the yields over conventional catalysts.
However, lower than equilibrium methane conversions and syngas yields were observed because of heat losses in the freeboard.
The preheat temperature of the reactants was shown to have little impact on syngas yields beyond extending the limits of stable operation.
Then a central composite experimental design (CCD) was used to optimize the upgraded bio-oil and syngas yields with 0.5% Zn loaded in ZSM-5.
In addition to carbon deposition, DRM is highly endothermic reaction (∆H298K = 59.1 kcal mol−1) and requires temperatures approaching 900 1,000 °C to reach high equilibrium syngas yields.
Because temperatures well above 700 °C are required to reach high syngas yields, traditional supported metals are not stable, suggesting the need to develop an inherently stable material that is catalytically active.
Accumulative yield of carbon monoxide was maximum for oxygen concentration of 9% (dry basis) above which extra oxygen concentration caused further oxidation of the syngas components to decrease the energy content of syngas yield.
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