Kinetic models, for following one-dimensional

Kinetic Models for Following One-Dimensional Growth and Gelation I 51... 

The experimental setup has been modeled as pseudohomogeneous one-dimensional reactor. The classical continuous kinetic model (Laxminarasimhan et al., 1996) was used for hydrocracking reactions thus, the mass balance into the reactor can be represented by an integrodifferential equation as in Equation 11.55. This equation and the following equations are similar to Equations 11.8 through 11.15 in which k has been replaced by 1 hdc (Elizalde and Ancheyta, 2012) ... 

The process is described by an one-dimensional, pseudohomogeneous, non-steady state dispersion model for an adiabatic fixed bed reactor. The kinetics are modelled by a re-versibll reaction system where each reaction step follows a power law with a reaction order of one in the gas and in the solid component. The temperature dependency of the reaction rate constant follows the Arrhenius law. The equilibrium constant is set to be independent of temperature. 

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