Modeling of Autocyclic Reactor for the Removal of Unburned Methane from Emissions of Natural Gas Engines

被引:6
作者
Zanoletti, Massimiliano [1 ]
Klvana, Danilo [1 ]
Kirchnerova, Jitka [1 ]
Perrier, Michel [1 ]
机构
[1] Ecole Polytech, Dept Chem Engn, Montreal, PQ H3C 3A7, Canada
关键词
AUTO-CYCLIC REACTOR; CATALYTIC COMBUSTION; MONOLITH CATALYSTS; COMPLETE OXIDATION; HEAT-TRANSFER; CONVERTER; PERFORMANCE; EXHAUST; DESIGN;
D O I
10.1021/ie900701h
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Natural gas represents an environmentally attractive alternative to diesel and gasoline fuels to reduce all automotive emissions. However, a relatively high content of unburned methane in the exhaust gases outweighs these benefits. To treat Such emissions, a counter-current type fixed bed autocyclic reactor (ACR) was designed and built for laboratory testing. The efficiency of the ACR, loaded with palladium based catalysts (pellets and monoliths) was evaluated experimentally under a wide range of conditions. As a first step in modeling the ACR performance, it HTI-D model was developed to Suit the actual reactor configuration. This model reproduced adequately the axial temperature profiles and methane conversion, but tuning Parameters had to be used to account for heat transfer. To permit investigation of radial heat transfer and thus better understanding of the ACR behavior, a two-dimensional model was developed, and Successfully validated against experimental data. The new HT2-Dt model allowed it full range of the ACR performance simulations.
引用
收藏
页码:1063 / 1070
页数:8
相关论文
共 25 条
[1]   Engines and exhaust after treatment systems for future automotive applications [J].
Alkemade, Ulrich G. ;
Schumann, Bemd .
SOLID STATE IONICS, 2006, 177 (26-32) :2291-2296
[2]   Mathematical modeling of monolith catalysts and reactors for gas phase reactions [J].
Chen, Jinwen ;
Yang, Hong ;
Wang, Neil ;
Ring, Zbigniew ;
Dabros, Tadeusz .
APPLIED CATALYSIS A-GENERAL, 2008, 345 (01) :1-11
[3]   MODELING OF HEAT-TRANSFER IN NONADIABATIC MONOLITH REACTORS AND EXPERIMENTAL COMPARISONS OF METAL MONOLITHS WITH PACKED-BEDS [J].
FLYTZANI-STEPHANOPOULOS, M ;
VOECKS, GE ;
CHARNG, T .
CHEMICAL ENGINEERING SCIENCE, 1986, 41 (05) :1203-1212
[4]   Complete oxidation of methane at low temperature over noble metal based catalysts:: a review [J].
Gélin, P ;
Primet, M .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2002, 39 (01) :1-37
[5]   A COMPARISON OF LUMPED AND DISTRIBUTED MODELS OF MONOLITH CATALYTIC COMBUSTORS [J].
GROPPI, G ;
BELLOLI, A ;
TRONCONI, E ;
FORZATTI, P .
CHEMICAL ENGINEERING SCIENCE, 1995, 50 (17) :2705-2715
[6]   Continuous vs discrete models of nonadiabatic monolith catalysts [J].
Groppi, G ;
Tronconi, E .
AICHE JOURNAL, 1996, 42 (08) :2382-2387
[7]  
Hayes R.D., 1997, INTRO CATALYTIC COMB
[8]   Performance of auto-cyclic reactor in catalytic combustion of lean fuel mixtures [J].
Klvana, D ;
Chaouki, J ;
Guy, C ;
Kirchnerova, J ;
Zanoletti, M .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2005, 44 (25) :9676-9682
[9]   MODELING OF HEAT-TRANSFER IN NON-ADIABATIC MONOLITHIC REACTORS [J].
KOLACZKOWSKI, ST ;
CRUMPTON, P ;
SPENCE, A .
CHEMICAL ENGINEERING SCIENCE, 1988, 43 (02) :227-231
[10]   Modelling channel interactions in a non-adiabatic multichannel catalytic combustion reactor [J].
Kolaczkowski, ST ;
Worth, DJ .
CATALYSIS TODAY, 1995, 26 (3-4) :275-282