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Simultaneously, the C2 C5 hydrocarbon yield increased to approximately 8%.
Though dealumination only changed the acid distribution, it increased the hydrocarbon yield and introduced different chemical component of active coke.
The catalyst has a high hydrocarbon yield of 0.6 g (of hydrocarbon)/h-g Fe at high CO conversions (>85%).
The roles of key parameters such as types of reductant, reduction potential, pH of mixture, metal-loaded and supported catalyst on hydrocarbon yield and selectivity are also investigated.
Within the thermal wave pyrolysis regime these effects significantly reduce the light hydrocarbon yield, increase the tar yield, and reduce the pyrolysis time.
Hydro-catalytic pyrolysis of waste cooking oil at 400 °C, H2 pressure of 15 bars, and catalyst to oil ratio of 0.25 g/100 cm3 resulted in highest hydrocarbon yield (41.98%).
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Zr-promoted catalyst materials exhibited enhanced CO2 adsorption and improved hydrocarbon yields.
Hydrocarbon yields as high as 28% are observed over 1% Li2O-doped TiO2 at 800°C.
Nevertheless MDF, MDF-FR and PS show reasonable agreement for CO, CO2, HCN and hydrocarbon yields between the scales.
The responses analyzed were as follows: Y1: conversionion (mol% C) and Y2: aromatic hydrocarbon yields (mol% C).
The increasing of hydrogen and gaseous hydrocarbon yields also confirms that cracking of oil is enhanced during this pressure range.
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