Sensitivity analysis of kinetic parameters for heavy oil hydrocracking

被引:41
作者
Felix, Guillermo [1 ,2 ]
Ancheyta, Jorge [2 ]
Trejo, Fernando [1 ]
机构
[1] Inst Politecn Nacl, Ctr Invest Ciencia Aplicada & Tecnol Avanzada, Unidad Legaria, Legaria 694, Mexico City 11500, DF, Mexico
[2] Inst Mexicano Petr, Eje Cent Lazaro Cardenas 152, Mexico City 07730, DF, Mexico
关键词
Sensitivity analysis; Kinetic parameters; Regression analysis; Heavy oil hydrocracking; MODEL;
D O I
10.1016/j.fuel.2018.12.058
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Sensitivity analysis is an important tool commonly used for confirming the achievement of the optimum set of parameter values obtained by regression analysis. To highlight this importance, two cases reported in the literature for the kinetic modeling of hydrocracking of heavy oils were selected, and sensitivity analysis was performed for the reported parameters. It was found that the values of the reported kinetic parameters do not reach the minimization of the objective function based on the sum of squares errors between predicted and experimental product yields, so that the reported set of kinetic parameters is not the optimal one. The calculated optimized reaction rate coefficients fitted better to experimental data than those reported in the literature. It was demonstrated that sensitivity analysis is of great relevance for determining the best set of parameters, and thus establishing proper reaction pathways, values of reaction rate coefficients, and activation energies, whereby reactor modeling, simulation, design and optimization can be done in an effective manner.
引用
收藏
页码:836 / 844
页数:9
相关论文
共 9 条
[1]   Sensitivity analysis based methodology to estimate the best set of parameters for heterogeneous kinetic models [J].
Alcazar, Luis A. ;
Ancheyta, Jorge .
CHEMICAL ENGINEERING JOURNAL, 2007, 128 (2-3) :85-93
[2]   A new approach to estimate parameters of a lumped kinetic model for hydroconversion of heavy residue [J].
Asaee, Seyed Danial Seyed ;
Vafajoo, Leila ;
Khorasheh, Farhad .
FUEL, 2014, 134 :343-353
[3]   Kinetic Models for Upgrading Athabasca Bitumen Using Unsupported NiWMo Catalysts at Low Severity Conditions [J].
Galarraga, Carmen E. ;
Scott, Carlos ;
Loria, Herbert ;
Pereira-Almao, Pedro .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2012, 51 (01) :140-146
[4]   Modelling and parameter estimation of ultra-dispersed in situ catalytic upgrading experiments in a batch reactor [J].
Hassanzadeh, Hassan ;
Abedi, Jalal .
FUEL, 2010, 89 (10) :2822-2828
[5]   Kinetic parameter estimation and simulation of trickle-bed reactor for hydrodesulfurization of crude oil [J].
Jarullah, Aysar T. ;
Mujtaba, Iqbal M. ;
Wood, Alastair S. .
CHEMICAL ENGINEERING SCIENCE, 2011, 66 (05) :859-871
[6]   Kinetic Modeling of Bitumen Hydroprocessing at In-Reservoir Conditions Employing Ultradispersed Catalysts [J].
Loria, Herbert ;
Trujillo-Ferrer, Gustavo ;
Sosa-Stull, Clementina ;
Pereira-Almao, Pedro .
ENERGY & FUELS, 2011, 25 (04) :1364-1372
[7]   Kinetic model for hydrocracking of heavy oil in a CSTR involving short term catalyst deactivation [J].
Martinez, Jeremias ;
Ancheyta, Jorge .
FUEL, 2012, 100 :193-199
[8]   Kinetic analysis of vacuum residue hydrocracking in early reaction stages [J].
Puron, H. ;
Arcelus-Arrillaga, P. ;
Chin, K. K. ;
Pinilla, J. L. ;
Fidalgo, B. ;
Millan, M. .
FUEL, 2014, 117 :408-414
[9]   Kinetic model for moderate hydrocracking of heavy oils [J].
Sánchez, S ;
Rodríguez, MA ;
Ancheyta, J .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2005, 44 (25) :9409-9413