Biomass Gasification in Supercritical Water - A Review

被引:111
作者
Basu, Prabir [1 ]
Mettanant, Vichuda [1 ]
机构
[1] Dalhousie Univ, Halifax, NS B3H 3J5, Canada
关键词
SCW; gasification; biomass; review; exergy analysis; PRESSURE PHASE-EQUILIBRIA; HYDROGEN-PRODUCTION; THERMODYNAMIC ANALYSIS; HIGH-TEMPERATURE; PVT-DATA; GLUCOSE; CELLULOSE; LIGNIN; SYSTEM; MODEL;
D O I
10.2202/1542-6580.1919
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Supercritical water possesses a number of important characteristics that make it suitable for oxidation, synthesis and gasification reactions. It is especially advantageous for very wet biomass whose gasification in this medium avoids the large expense of energy required for drying. Although the process is in laboratory scale it has a great potential for production of hydrogen and other gases from biomass. This paper reviews the present state of the art and summarizes major observations arrived at in small scale laboratory flow and batch reactors. Effects of operating parameters like, pressure, temperature, etc., on the yield and conversion are discussed. Catalysts appear to play an important role in increasing the conversion rate and decreasing the reaction temperature for gasification. Heat recovery from the product stream holds key to making the gasification process auto-thermal. Heat exchanger efficiency, therefore, plays an important role in this process. Several investigators have used the equilibrium model and exergy analysis for thermodynamic analysis of supercritical gasification plants. Energy efficiency of such a plant could be around 50%.
引用
收藏
页数:63
相关论文
共 96 条
[31]   Exergetic efficiency and options for improving sewage sludge gasification in supercritical water [J].
Gasafi, Edgar ;
Meyer, Lutz ;
Schebek, Liselotte .
INTERNATIONAL JOURNAL OF ENERGY RESEARCH, 2007, 31 (04) :346-363
[32]  
*GEN AT SCW3, 2008, GEN AT AFF CO
[33]  
[关宇 GUAN Yu], 2007, [高校化学工程学报, Journal of Chemical Engineering of Chinese Universities], V21, P436
[34]   Hydrogen production by biomass gasification in supercritical water: A systematic experimental and analytical study [J].
Guo, L. J. ;
Lu, Y. J. ;
Zhang, X. M. ;
Ji, C. M. ;
Guan, Y. ;
Pei, A. X. .
CATALYSIS TODAY, 2007, 129 (3-4) :275-286
[35]   Hydrogen production from catalytic gasification of cellulose in supercritical water [J].
Hao, XH ;
Guo, LJ ;
Zhang, XM ;
Guan, Y .
CHEMICAL ENGINEERING JOURNAL, 2005, 110 (1-3) :57-65
[36]   Hydrogen production from glucose used as a model compound of biomass gasified in supercritical water [J].
Hao, XH ;
Guo, LJ ;
Mao, X ;
Zhang, XM ;
Chen, XJ .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2003, 28 (01) :55-64
[37]   Selective promotion of catalytic reactions during biomass gasification to hydrogen [J].
Hashaikeh, R. ;
Butler, I. S. ;
Kozinski, J. A. .
ENERGY & FUELS, 2006, 20 (06) :2743-2747
[38]   HIGH-PRESSURE PHASE-EQUILIBRIA AND PVT-DATA OF THE WATER-OXYGEN SYSTEM INCLUDING WATER-AIR TO 673-K AND 250-MPA [J].
JAPAS, ML ;
FRANCK, EU .
BERICHTE DER BUNSEN-GESELLSCHAFT-PHYSICAL CHEMISTRY CHEMICAL PHYSICS, 1985, 89 (12) :1268-1275
[39]   HIGH-PRESSURE PHASE-EQUILIBRIA AND PVT-DATA OF THE WATER-NITROGEN SYSTEM TO 673-K AND 250 MPA [J].
JAPAS, ML ;
FRANCK, EU .
BERICHTE DER BUNSEN-GESELLSCHAFT-PHYSICAL CHEMISTRY CHEMICAL PHYSICS, 1985, 89 (07) :793-800
[40]   Thermodynamic equilibrium model and second law analysis of a downdraft waste gasifier [J].
Jarungthammachote, S. ;
Dutta, A. .
ENERGY, 2007, 32 (09) :1660-1669