Methodology for inferring kinetic parameters of diesel oil HDS reactions based on scarce experimental data
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Maria do Carmo Nicoletti | João Roberto Bertini | Roberto de Campos Giordano | M. C. Nicoletti | A. S. Ferreira | R. Giordano | A. S. Ferreira | J. R. Bertini
[1] Sandro Ridella,et al. Minimizing multimodal functions of continuous variables with the “simulated annealing” algorithmCorrigenda for this article is available here , 1987, TOMS.
[2] Marcio Schwaab,et al. Optimum reference temperature for reparameterization of the Arrhenius equation. Part 1 : Problems involving one kinetic constant , 2007 .
[3] G. D. Bellos,et al. The use of a three phase microreactor to investigate HDS kinetics , 2003 .
[4] William L. Goffe,et al. SIMANN: FORTRAN module to perform Global Optimization of Statistical Functions with Simulated Annealing , 1992 .
[5] Maria do Carmo Nicoletti,et al. A Heuristic Search for Optimal Parameter Values of Three Biokinetic Growth Models for Describing Batch Cultivations of Streptococcus Pneumoniaein Bioreactors , 2008, IEA/AIE.
[6] D. Resasco,et al. Inhibition of the Hydrogenation and Hydrodesulfurization Reactions by Nitrogen Compounds over NiMo/Al2O3 , 2008 .
[7] David Mautner Himmelblau,et al. Process analysis by statistical methods , 1970 .
[8] Marcio Schwaab,et al. Optimum reference temperature for reparameterization of the Arrhenius equation. Part 2: Problems involving multiple reparameterizations , 2008 .
[9] C. D. Gelatt,et al. Optimization by Simulated Annealing , 1983, Science.
[10] M. R. Wolf-Maciel,et al. A cape of HDT industrial reactor for middle distillates , 2000 .
[11] D. Marquardt. An Algorithm for Least-Squares Estimation of Nonlinear Parameters , 1963 .
[12] G. Hutchings,et al. Hydrodesulfurization of hindered dibenzothiophenes: an overview , 2000 .
[13] A. Meenakshisundaram,et al. APPLICATION OF A THREE PHASE HETEROGENEOUS MODEL TO ANALYSE THE PERFORMANCE OF A PILOT PLANT TRICKLE BED REACTOR , 2002 .
[14] Egon Eckert,et al. New approach to the characterisation of petroleum mixtures used in the modelling of separation processes , 2005, Comput. Chem. Eng..
[15] Rainer Reimert,et al. Trickle‐bed reactor model for desulfurization and dearomatization of diesel , 2002 .
[16] Mohan S. Rana,et al. Recent advances in the science and technology of ultra low sulfur diesel (ULSD) production , 2010 .
[17] F. Jiménez,et al. Modeling of industrial reactor for hydrotreating of vacuum gas oils Simultaneous hydrodesulfurization, hydrodenitrogenation and hydrodearomatization reactions , 2007 .
[18] Georgina C. Laredo,et al. Inhibition effects of nitrogen compounds on the hydrodesulfurization of dibenzothiophene: Part 2 , 2001 .
[19] I. Babich. Science and technology of novel processes for deep desulfurization of oil refinery streams: a review☆ ☆ , 2003 .
[20] I. Jolliffe. Principal Component Analysis , 2002 .
[21] Tomáš Vaněk,et al. Improvements in the selection of real components forming a substitute mixture for petroleum fractions , 2009 .
[22] S. Eijsbouts,et al. How a 70-year-old catalytic refinery process is still ever dependent on innovation , 2008 .
[23] D. Himmelblau,et al. Optimization of chemical process , 2001 .
[24] Enrique Arce-Medina,et al. Artificial neural network modeling techniques applied to the hydrodesulfurization process , 2009, Math. Comput. Model..
[25] Ulrich Hoffmann,et al. Three‐phase reactor model for hydrotreating in pilot trickle‐bed reactors , 1996 .