Performance evaluation of hydroprocessing catalysts - A review of experimental techniques

被引:51
作者
Bej, SK [1 ]
机构
[1] Univ Michigan, Dept Chem Engn, Ann Arbor, MI 48109 USA
关键词
D O I
10.1021/ef010254l
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 selection of an appropriate reactor for hydroprocessing catalysis research primarily depends on the type of information to be generated, the reliability and reproducibility of the information required, and the cost involved to generate such information. In this article, the various reactors and approaches that. have been used at different stages of hydroprocessing catalysis research and process development are reviewed. With the development of the dilution technique, substantial progress has taken place in reducing the size of reactor used for hydroprocessing process development studies. This has decreased the cost of catalyst evaluation as well as increased the operating safety. However, the selection of an appropriate size of diluent is very important. Studies comparing the differences in the behavior between up-flow and down-flow modes of operation of a fixed bed reactor are analyzed. An attempt has been made to provide guidelines for selecting the appropriate reactor and methodology to evaluate hydroprocessing catalysts. Reactors that are commonly used for the kinetic studies of hydroprocessing reactions are also reviewed in this article.
引用
收藏
页码:774 / 784
页数:11
相关论文
共 88 条
[1]   Catalyst bed dilution for improving catalyst wetting in laboratory trickle-bed reactors [J].
AlDahhan, MH ;
Dudukovic, MP .
AICHE JOURNAL, 1996, 42 (09) :2594-2606
[2]   REPRODUCIBLE TECHNIQUE FOR PACKING LABORATORY-SCALE TRICKLE-BED REACTORS WITH A MIXTURE OF CATALYST AND FINES [J].
ALDAHHAN, MH ;
WU, YX ;
DUDUKOVIC, MP .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1995, 34 (03) :741-747
[3]  
[Anonymous], 2000, DESULFURIZATION HEAV
[4]   Lumped kinetics of hydrocracking of bitumen [J].
Ayasse, AR ;
Nagaishi, H ;
Chan, EW ;
Gray, MR .
FUEL, 1997, 76 (11) :1025-1033
[5]   Effect of hydrotreating conditions on the conversion of residual fraction and microcarbon residue present in oil sands derived heavy gas oil [J].
Bej, SK ;
Dalai, AK ;
Adjaye, J .
ENERGY & FUELS, 2001, 15 (05) :1103-1109
[6]   Effect of diluent size on the performance of a micro-scale fixed bed multiphase reactor in up flow and down flow modes of operation [J].
Bej, SK ;
Dalai, AK ;
Maity, SK .
CATALYSIS TODAY, 2001, 64 (3-4) :333-345
[7]   Comparison of hydrodenitrogenation of basic and nonbasic nitrogen compounds present in oil sands derived heavy gas oil [J].
Bej, SK ;
Dalai, AK ;
Adjaye, J .
ENERGY & FUELS, 2001, 15 (02) :377-383
[8]   Studies on the performance of a microscale trickle bed reactor using different sizes of diluent [J].
Bej, SK ;
Dabral, RP ;
Gupta, PC ;
Mittal, KK ;
Sen, GS ;
Kapoor, VK ;
Dalai, AK .
ENERGY & FUELS, 2000, 14 (03) :701-705
[9]  
Berger RJ, 2001, CATTECH, V5, P30
[10]  
Berty J. M., 1999, Experiments in Catalytic Reaction Engineering