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Microbial conversion of feedstocks (simple sugars, starches and other polysaccharides, and total biomass) to biofuels (primarily ethanol as of now, but preferably other alcohols and fatty acid esters in the future) promises a renewable and potentially globally distributed source of transportation fuel.
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Thermal cracking is beneficial to some degree for further conversion of feedstock.
The conversion of feedstock oils and model reactant increased with the presence of Mo catalyst.
Therefore, the dispersed catalyst obviously increased the conversion of feedstock oils, meanwhile, the serious cracking and coke formation were inhibited.
Moreover, the porthole is easily blocked up with the bigger molecules in severe and inferior feedstock, which deactivates the FCC catalyst quickly and reduces the conversion of feedstock.
Both show that new catalysts have better performance in improving conversion of feedstock and total yields, while reducing slurry and coke yields than industrial catalysts.
The FCC catalysts are easier to deactivate along with higher delta coke formation and metal deposition, leading to reduced conversion of feedstock.
Zhang et al. [30] reported the effect of dispersed catalyst in slurry-phase hydrocracking was to promote the conversion of feedstock oil and inhibit the formation of coke.
In addition, the blends of additive and base catalyst usually caused the decrease of the conversion of feedstock and the increase of coke formation to a certain degree because of the dilution effect of base catalysts and the enhanced Lewis acidity on additives.
Experimental data revealed that the conversion of feedstock oils and model reactant increased with the presence of catalyst, while the yields of light products (gas, naphtha) and heavy products (vacuum residue, coke) decreased, the yields of diesel and vacuum gas oil increased in the meantime.
Cost of ethanol and process energy use in cellulosic ethanol plants are dependent on technologies used for conversion of feedstock.
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