a third-generation dry gas-to-ethylbenzene process in a factory of PetroChina is considered.For the gradual catalyst deactivation in the alkylation reactor
a model is established with the parameters estimated from the reaction rate equation of alkylation based on the on-site data and those from laboratory analysis. The real-time dynamic simulation of the alkylation process is carried out
in which the module accuracy is ensured by using OPC(Object linking and embedding for Process Control)technique and adaptive correction of model parameters.Both the current and future operation temperature can be predicted.
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Hydrodechlorination of trifluoro-trichloroethane to chlorotrifluoroethylene: Revealing the deactivation mechanism and regeneration strategy of Pd-Cu/AC catalyst
Application of kinetics and computational fluid dynamics in pinene isomerization
Catalytic behavior in propane aromatization using GA-MFI catalyst
Deactivation mechanism of beta-zeolite catalyst for synthesis of cumene by benzene alkylation with isopropanol
Estimation of catalytic activity using an unscented Kalman filtering in condensation reaction
Related Author
Xiaonian Li
Qunfeng Zhang
Qingtao Wang
Feng Feng
Zile Li
Jian Lu
Bingcheng Li
Xiaoyu Wen
Related Institution
State Key Laboratory of Fluorine & Nitrogen Chemicals, Xi'an Modern Chemistry Research Institute
State Key Laboratory Breeding Base of Green Chemistry Synthesis Technology, Institute of Industrial Catalysis of Zhejiang University of Technology
Department of Chemical Engineering, School of Chemistry and Chemical Engineering, State Key Laboratory of Metal Matrix Composites, Shanghai Jiao Tong University
University of Calabria, Department of Environmental and Chemical Engineering, Via P. Bucci,- Rende, CS
State Key Laboratory of Materials-Oriented Chemical Engineering, Nanjing Tech University