The kinetics of methanol to olefins in the fixed-bed isothermal integral reactor was studied. The lumping idea was introduced into the kinetics study
in which the influence of water and coke deposition was taken into consideration.The equations of kinetics on fresh and deactivated catalyst were calculated with the help of the simplex optimization and Runge-Kutta methods.The obtained general kinetics equations could be used to calculate the reaction rates of corresponding lump. Subsequently
the respective reaction rate of ethylene
propylene
butene in any conditions were calculated based on the relation of ratios between olefins (ethylene/propylene and propylene/butene) and reaction temperature.The results showed that the error of statistical test and comparison of calculated values with the experimental values was in the allowable range.
Analysis of enzymatic hydrolysis process for preparing active peptides based on protein structure(Ⅱ) Lumping kinetic model for enzymatic hydrolysis reaction
溶液初始pH值对2,4-D臭氧直接反应动力学的影响
Kinetic model on ozonation of p-toluene sulfonic acid
Degradation of perfluorobutyric acid in aqueous solution by ultrasound irradiation
Kinetics of advanced treatment of high-viscosity petrochemical wastewater with oxidation by Fenton’s reagent