Kinetic modeling of hydrocracking of heavy oil fractions:: A review

被引:185
作者
Ancheyta, J
Sánchez, S
Rodríguez, MA
机构
[1] Inst Mexicano Petr, Mexico City 07730, DF, Mexico
[2] Univ Nacl Autonoma Mexico, Fac Ingn, Mexico City 04510, DF, Mexico
[3] ESIQIE IPN, IPN, UPALM, Mexico City 07738, DF, Mexico
关键词
hydrocracking; heavy oil; kinetics;
D O I
10.1016/j.cattod.2005.08.015
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
An exhaustive review of the scientific literature on kinetic modeling of heavy petroleum fraction hydrocracking is reported in this paper. Kinetic models for hydrocracking of model compounds were not analyzed. The review includes models based on the lumping technique, continuous mixtures, structure oriented lumping, and single event models. Experimental data, reaction networks, main characteristics of kinetic approaches, and kinetic parameter values are also reported. In some cases when detailed experimental data were available, kinetic parameters were re-estimated and some differences were found in comparison with original reported values. One representative model of each kinetic approach was selected, and parameter estimation was done with reported experimental values in order to establish the capability and accuracy in the prediction of conversion and product yields. Advantages and disadvantages of the models are discussed in terms of their capability to predict detailed product composition, difficulty for parameter estimation, dependency of rate coefficient with feed properties, and required experimental data. (c) 2005 Elsevier B.V. All rights reserved.
引用
收藏
页码:76 / 92
页数:17
相关论文
共 39 条
[1]   Changes in apparent reaction order and activation energy in the hydrodesulfurization of real feedstocks [J].
Ancheyta, J ;
Angeles, MJ ;
Macías, MJ ;
Marroquín, G ;
Morales, R .
ENERGY & FUELS, 2002, 16 (01) :189-193
[2]   Estimation of kinetic constants of a five-lump model for fluid catalytic cracking process using simpler sub-models [J].
Ancheyta, J ;
Sotelo-Boyás, R .
ENERGY & FUELS, 2000, 14 (06) :1226-1231
[3]   A strategy for kinetic parameter estimation in the fluid catalytic cracking process [J].
AncheytaJuarez, J ;
LopezIsunza, F ;
AguilarRodriguez, E ;
MorenoMayorga, JC .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1997, 36 (12) :5170-5174
[4]  
[Anonymous], ERDOL ERDGAS KOHLE
[5]   Kinetics of hydrocracking and hydrotreating of coker and oilsands gas oils [J].
Aoyagi, K ;
McCaffrey, WC ;
Gray, MR .
PETROLEUM SCIENCE AND TECHNOLOGY, 2003, 21 (5-6) :997-1015
[6]   Lumped kinetics of hydrocracking of bitumen [J].
Ayasse, AR ;
Nagaishi, H ;
Chan, EW ;
Gray, MR .
FUEL, 1997, 76 (11) :1025-1033
[7]   Industrial hydrocracker model based on novel continuum lumping approach for optimization in petroleum refinery [J].
Basak, K ;
Sau, M ;
Manna, U ;
Verma, RP .
CATALYSIS TODAY, 2004, 98 (1-2) :253-264
[8]  
Bennett R.N., 1972, P ACS S ADV DIST RES
[9]  
Botchwey C, 2004, CAN J CHEM ENG, V82, P478
[10]   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