A new approach to estimate parameters of a lumped kinetic model for hydroconversion of heavy residue

被引:27
作者
Asaee, Seyed Danial Seyed [1 ]
Vafajoo, Leila [1 ]
Khorasheh, Farhad [2 ]
机构
[1] Islamic Azad Univ, Tehran South Branch, Chem Engn Grp, Tehran, Iran
[2] Sharif Univ Technol, Dept Chem & Petr Engn, Tehran, Iran
关键词
Hydroconversion; Heavy residue; Lumped kinetic model; Kinetic parameters; MODERATE HYDROCRACKING; VACUUM RESIDUE; OIL; BITUMEN;
D O I
10.1016/j.fuel.2014.05.079
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
The effect of complexity level of a lumped kinetic model for heavy residue hydroconversion on estimated values of kinetic parameters was investigated in this work by imposing constraints for the parameter estimation algorithm of a complex six-lump kinetic model and deriving a simpler modified model from the complex model. Kinetic analysis was performed using available experimental data reported in the literature from a study on hydrocracking of Chinese Gudao vacuum residue in a bench-scale reactor using ammonium phosphomolybdate (APM) as a dispersed catalyst. The kinetic models also included coke formation reactions that had previously been ignored by most investigators due to the rather small amounts of coked formed under moderate reaction temperatures. Three constrained levels were incorporated into the parameters estimation algorithm of the kinetic model and the Average Absolute Errors (AAE) between experimental and predicted product mass fractions for each model were compared. It was found that while AAE increased by imposing additional constraints, more logical kinetic parameters were obtained. The AAE% of the last constrained level of the complex model was 9.2%. A simpler modified model was then defined based on the results of the original complex model. The AAE% after sensitivity analysis of the estimated Arrhenius parameters for the modified model without imposing any restrictions on parameter values was 8.8%. (C) 2014 Elsevier Ltd. All rights reserved.
引用
收藏
页码:343 / 353
页数:11
相关论文
共 18 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]   Kinetic modeling of hydrocracking of heavy oil fractions:: A review [J].
Ancheyta, J ;
Sánchez, S ;
Rodríguez, MA .
CATALYSIS TODAY, 2005, 109 (1-4) :76-92
[3]   Lumped kinetics of hydrocracking of bitumen [J].
Ayasse, AR ;
Nagaishi, H ;
Chan, EW ;
Gray, MR .
FUEL, 1997, 76 (11) :1025-1033
[4]   Product selectivity during hydrotreating and mild hydrocracking of bitumen-derived gas oil [J].
Botchwey, C ;
Dalai, AK ;
Adjaye, J .
ENERGY & FUELS, 2003, 17 (05) :1372-1381
[5]   Hydroconversion kinetics of Marlim vacuum residue [J].
de Almeida, RM ;
Guirardello, R .
CATALYSIS TODAY, 2005, 109 (1-4) :104-111
[6]  
Galarraga CE, 2009, 8 WORLD C CHEM ENG M
[7]   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
[8]  
Ho TehC., 2006, Practical Advances in Petroleum Processing, P653, DOI DOI 10.1007/978-0-387-25789-1_21
[9]   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
[10]   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