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Numerical Modeling of Drying Kinetics

Numerous other models have been proposed to explain the deviation of dry oxidation from linear-parabolic kinetics. For example, field-assisted oxidant diffiision during the oxidation of metals was proposed by Cabrera and Mott (75) and used by Deal and Grove (69) to explain the results for thin oxides. Ghez and van der Meulen (76) proposed the dissociation of molecular oxygen into atomic oxygen at the Si-Si02 interface and the re-... [Pg.321]

A model for transient simulation of radial and axial composition and temperature profiles In pressurized dry ash and slagging moving bed gasifiers Is described. The model Is based on mass and energy balances, thermodynamics, and kinetic and transport rate processes. Particle and gas temperatures are taken to be equal. Computation Is done using orthogonal collocation In the radial variable and exponential collocation In time, with numerical Integration In the axial direction. [Pg.359]

Numerical simulation results of batch and continuous drying models for slices of peppers in packed beds were presented in this work. The reported models were based on differential mass and energy balances in the dryer along with kinetic equations describing transport phenomena in individual particles and product quality deterioration. The shrinkage problem was... [Pg.540]


See other pages where Numerical Modeling of Drying Kinetics is mentioned: [Pg.1323]    [Pg.1351]    [Pg.30]    [Pg.1322]    [Pg.1350]    [Pg.30]    [Pg.1323]    [Pg.1351]    [Pg.30]    [Pg.1322]    [Pg.1350]    [Pg.30]    [Pg.27]    [Pg.238]    [Pg.49]    [Pg.574]    [Pg.585]    [Pg.27]    [Pg.229]    [Pg.979]    [Pg.508]    [Pg.452]    [Pg.452]    [Pg.273]   


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