High-temperature air and steam gasification of densified biofuels

被引:118
作者
Lucas, C
Szewczyk, D
Blasiak, W
Mochida, S
机构
[1] Royal Inst Technol, Div Energy & Furnace Technol, S-10044 Stockholm, Sweden
[2] Nippon Furnace Kogyo Kaisha Ltd, Yokohama, Kanagawa, Japan
关键词
high-temperature gasification; fixed bed; updraft; pellets;
D O I
10.1016/j.biombioe.2003.08.015
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
An experimental study was carried out to investigate gasification of densified biofuels using highly preheated air and steam as a gasifying agent. Preheat of air and steam is realised by means of the newly developed high-cycle regenerative air/steam preheater. Use of highly preheated feed gas provides additional energy into the gasification process, which enhances the thermal decomposition of the gasified solids. For the same type of feedstock the operating parameters, temperature, composition and amount of gasifying agent, were varied over a wide range. Results of experiments conducted in. a high-temperature air/steam fixed bed updraft gasifier show the capability of this technology of maximising the gaseous product yield as a result of the high heating rates involved, and the efficient tar reduction. Increase of the feed gas temperature reduces production of tars, soot and char residue as well as increases heating value of the dry fuel gas produced. Overall, it has been seen that the yield and the lower heating value of the dry fuel gas increase with increasing temperature. (C) 2004 Elsevier Ltd. All rights reserved.
引用
收藏
页码:563 / 575
页数:13
相关论文
共 32 条
[1]   Thermal gasification of biomass technology developments: End of task report for 1992 to 1994 [J].
Babu, SP .
BIOMASS & BIOENERGY, 1995, 9 (1-5) :271-285
[2]  
BEENACKERS A, 1996, P C 5 EUR BIOEN C
[3]   Biomass gasification in moving beds, a review of European technologies [J].
Beenackers, AACM .
RENEWABLE ENERGY, 1999, 16 (1-4) :1180-1186
[4]  
BLASIAK W, 2002, KTHMSE0216SE ENERGYT
[5]  
BLASIAK W, 2002, P C 21 INT C INC THE
[6]   The influence of feedstock drying on the performance and economics of a biomass gasifier-engine CHP system [J].
Brammer, JG ;
Bridgwater, A .
BIOMASS & BIOENERGY, 2002, 22 (04) :271-281
[7]   THE TECHNICAL AND ECONOMIC-FEASIBILITY OF BIOMASS GASIFICATION FOR POWER-GENERATION [J].
BRIDGWATER, AV .
FUEL, 1995, 74 (05) :631-653
[8]   STEAM GASIFICATION OF CELLULOSIC WASTES IN A FLUIDIZED-BED WITH DOWNSTREAM VESSELS [J].
CORELLA, J ;
AZNAR, MP ;
DELGADO, J ;
ALDEA, E .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1991, 30 (10) :2252-2262
[9]   Ancillary equipment for biomass gasification [J].
Cummer, KR ;
Brown, RC .
BIOMASS & BIOENERGY, 2002, 23 (02) :113-128
[10]   Air gasification of biomass in a downdraft fixed bed: A comparative study of the inorganic and organic products distribution [J].
De Bari, I ;
Barisano, D ;
Cardinale, M ;
Matera, D ;
Nanna, F ;
Viggiano, D .
ENERGY & FUELS, 2000, 14 (04) :889-898