Methodology for inferring kinetic parameters of diesel oil HDS reactions based on scarce experimental data

Abstract Nowadays environmental regulations of fossil fuels emissions impose stricter limits for contaminants such as sulfur, nitrogen and aromatics from middle distillate petroleum fractions. The most important process used in oil refineries to reach the required specifications is catalytic hydrogenation. A key issue to optimize these units is the availability of reliable kinetic models for this complex, tri-phase reaction. A detailed, phenomenological model of the reactor would demand an exceeding experimental effort for consistently estimating all the necessary kinetic and transport parameters. Thus, a simplified approach is generally used for routine assessment of new catalysts and/or new streams to be processed. Due to the difficulty of characterization of these streams, which are very complex mixtures of numerous species, most models are based on pseudo-components. This approach, however, does not allow for model generalization with respect to feed composition. This paper presents and discusses a new methodology for dealing with this problem. Conventional neural network (NN) training algorithms are used for inducing NNs to predict kinetic parameters of simplified models for the catalytic hydrodesulfurization (HDS) reaction, using macro properties of the feed as input. As in practice there are rarely enough experimental data to subsidize empirical learning algorithms, the paper proposes and describes an ad hoc methodology for artificially enlarging the initial scarce experimental data. Results from inferring kinetic parameters of the catalytic removal of sulfur using NNs, based on macro-properties of oil middle distillates, are presented and discussed.

[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 .