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There were two important zones in CVD reactor first one is precursor vaporization zone and second one is coating zone.
Obtained results predicted by the models could be used to aid design of the FCC feed vaporization zone.
Different homogeneous models duly validated for various pure component droplets were applied to predict the vaporization time of the feed droplets typically expected in FCC feed vaporization zone.
Enthalpy at vaporization zone (kJ/kg).
The thermal demand can be calculated by the difference between the enthalpy at the vaporization zone (H vap) and the enthalpy at the condensation zone (H cond) multiplied by the C3R cycle flow (F C3R), as showed on the Eq. 2 and the Fig. 5: Open image in new window Fig. 5 Coefficient of performance and thermal demand Q = left( {H_{text{vap}} - H_{text{cond}} } right) times F_{text{C3R}}.
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Liquid feed vaporization and vapor cracking reaction in the feed zone plays an important role in the overall reaction performance of fluid catalytic cracking (FCC), an important petroleum refining process for converting heavy hydrocarbon feed stocks to high-value products such as gasoline and light olefins.
The high concentration of fine droplets, along with the high vapor pressure and high activity coefficient of ethanol, lead to extremely rapid vaporization of ethanol in the inner recirculation zone.
In this study, we have developed a theoretical framework for quantifying the liquid feed transport, vaporization and cracking in the feed injection zone.
Vaporization – the solid sample vaporizes to a gas.
The main advantages of the proposed approach relate to continuous input of carbon feedstock materials into plasma zone, relatively low energy cost of carbon vaporization and usage of low cost carbon black produced from waste hydrocarbons.
The high temperature produced due to EDM action thermally softens the work material in the grinding zone in addition to partial melting and vaporization.
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