Steam gasification of refuse-derived fuel (RDF): Influence of process temperature on yield and product composition

被引:45
作者
Galvagno, Sergio [1 ]
Casu, Stefania [1 ]
Casciaro, Giovanni [1 ]
Martino, Maria [1 ]
Russo, Antonio [1 ]
Portofino, Sabrina [1 ]
机构
[1] ENEA, Environm Div, Thermal Proc Dev Lab, I-75026 Rotondella, MT, Italy
关键词
D O I
10.1021/ef060239m
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 opportunity of using refuse-derived fuel (RDF) to produce fuel gas seems to be promising, and particular attention has been focused on alternative process technologies such as pyrolysis and gasification. Within this frame, present work relates to experimental tests and obtained results of a series of experimental surveys on RDF gasification with steam, performed by means of a bench-scale rotary kiln plant at different process temperatures, using thermogravimetry (TG) and infrared spectrometry (Fourier transform infrared, FTIR) to characterize the incoming material and online gas chromatography to qualify the gaseous stream. Experimental data show that the gas yield increases with temperature and, with respect to the gas composition, the hydrogen content increases, mainly at the expense of the other gaseous compounds, which highlights the major extension of secondary cracking reactions into the gaseous fraction at higher temperature. Syngas obtained at processing temperatures of 950 degrees C or higher seems to be suitable for producing hydrogen for ammonia synthesis or for fuel cell applications, whereas, at lower processing temperatures, it seems usable for Fischer-Tropsch synthesis. The low organic content of solid residue does not suggest any other exploitation of the char apart from the landfilling.
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收藏
页码:2284 / 2288
页数:5
相关论文
共 21 条
[1]   HETEROGENEOUS CRACKING OF WOOD PYROLYSIS TARS OVER FRESH WOOD CHAR SURFACES [J].
BOROSON, ML ;
HOWARD, JB ;
LONGWELL, JP ;
PETERS, WA .
ENERGY & FUELS, 1989, 3 (06) :735-740
[2]   Upgrading of waste derived solid fuel by steam gasification [J].
Braekman-Danheux, C ;
D'haeyere, A ;
Fontana, A ;
Laurent, P .
FUEL, 1998, 77 (1-2) :55-59
[3]   An overview of fast pyrolysis of biomass [J].
Bridgwater, AV ;
Meier, D ;
Radlein, D .
ORGANIC GEOCHEMISTRY, 1999, 30 (12) :1479-1493
[4]  
Casu S, 2005, J THERM ANAL CALORIM, V80, P477, DOI 10.1007/s10973-005-0680-z
[5]   Steam gasification of biomass-derived char for the production of carbon monoxide-rich synthesis gas [J].
Chaudhari, ST ;
Bej, SK ;
Bakhshi, NN ;
Dalai, AK .
ENERGY & FUELS, 2001, 15 (03) :736-742
[6]   Steam gasification of Cynara cardunculus L.:: influence of variables [J].
Encinar, JM ;
González, JF ;
González, J .
FUEL PROCESSING TECHNOLOGY, 2002, 75 (01) :27-43
[7]   The study of reactions influencing the biomass steam gasification process [J].
Franco, C ;
Pinto, F ;
Gulyurtlu, I ;
Cabrita, I .
FUEL, 2003, 82 (07) :835-842
[8]   Production of FT transportation fuels from biomass; technical options, process analysis and optimisation, and development potential [J].
Hamelinck, CN ;
Faaij, APC ;
den Uil, H ;
Boerrigter, H .
ENERGY, 2004, 29 (11) :1743-1771
[9]   Mechanisms and kinetics of thermal reactions of aromatic hydrocarbons from pyrolysis of solid fuels [J].
Jess, A .
FUEL, 1996, 75 (12) :1441-1448
[10]   Recycling of plastic wastes via pyrolysis [J].
Kiran, N ;
Ekinci, E ;
Snape, CE .
RESOURCES CONSERVATION AND RECYCLING, 2000, 29 (04) :273-283