Ash Transformation Chemistry during Combustion of Biomass

被引:370
作者
Bostrom, Dan [1 ]
Skoglund, Nils [1 ]
Grimm, Alejandro [2 ]
Boman, Christoffer [1 ]
Ohman, Marcus [2 ]
Brostrom, Markus [1 ]
Backman, Rainer [1 ]
机构
[1] Umea Univ, SE-90187 Umea, Sweden
[2] Lulea Univ Technol, Div Energy Sci, SE-97187 Lulea, Sweden
基金
瑞典研究理事会;
关键词
FLUIDIZED-BED COMBUSTION; SYSTEM CAO-K2O-P2O5; PHASE-EQUILIBRIA; SLAGGING CHARACTERISTICS; INORGANIC CONSTITUENTS; GAS-PHASE; PART; RELEASE; PYROLYSIS; ELEMENTS;
D O I
10.1021/ef201205b
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
There is relatively extensive knowledge available concerning ash transformation reactions during combustion of woody biomass. In recent decades, the use of these energy carriers has increased, from a low-technology residential small-scale level to an industrial scale. Along this evolution, ash chemical-related phenomena for woody biomass have been observed and studied. Therefore, presently the understanding for these are, if not complete, fairly good. However, because the demand for CO2-neutral energy resources has increased recently and will continue to increase in the foreseeable future, other biomasses, such as, for instance, agricultural crops, have become highly interesting. The ash-forming matter in agricultural biomass is rather different in comparison to woody biomass, with a higher content of phosphorus as a distinctive feature. The knowledge about the ash transformation behavior in these systems is far from complete. Here, an attempt to give a schematic but general description of the ash transformation reactions of biomass fuels is presented in terms of a conceptual model, with the intention to provide guidance in the understanding of ash matter behavior in the use of any biomass fuel, primarily from the knowledge of the concentrations of ash-forming elements. The model was organized in primary and secondary reactions. Restrictions on the theoretical model in terms of reactivity limitations and physical conditions of the conversion process were discussed and exemplified, and some principal differences between biomass ashes dominated by Si and P, separately, were outlined and discussed.
引用
收藏
页码:85 / 93
页数:9
相关论文
共 41 条
[1]  
[Anonymous], J SOC GLASS TECHNOL
[2]  
[Anonymous], P 16 INT C FLUID BED
[3]  
[Anonymous], 2001, STUDIES PLANT SCI
[4]   FactSage thermochemical software and databases [J].
Bale, C ;
Chartrand, P ;
Degterov, SA ;
Eriksson, G ;
Hack, K ;
Ben Mahfoud, R ;
Melançon, J ;
Pelton, AD ;
Petersen, S .
CALPHAD-COMPUTER COUPLING OF PHASE DIAGRAMS AND THERMOCHEMISTRY, 2002, 26 (02) :189-228
[5]  
Baxter L., 1996, ALKALI DEPOSITS FOUN
[6]   COMPARISON OF INORGANIC CONSTITUENTS IN 3 LOW-RANK COALS [J].
BENSON, SA ;
HOLM, PL .
INDUSTRIAL & ENGINEERING CHEMISTRY PRODUCT RESEARCH AND DEVELOPMENT, 1985, 24 (01) :145-149
[7]   Ash Transformations in Fluidized-bed Combustion of Rapeseed Meal [J].
Bostrom, Dan ;
Eriksson, Gunnar ;
Boman, Christoffer ;
Ohman, Marcus .
ENERGY & FUELS, 2009, 23 (5-6) :2700-2706
[8]   Release of inorganic constituents from leached biomass during thermal conversion [J].
Dayton, DC ;
Jenkins, BM ;
Turn, SQ ;
Bakker, RR ;
Williams, RB ;
Belle-Oudry, D ;
Hill, LM .
ENERGY & FUELS, 1999, 13 (04) :860-870
[9]  
Diaz M., 2012, ENERGY FUELS UNPUB
[10]   Development of a modeling approach to predict ash formation during co-firing of coal and biomass [J].
Doshi, V. ;
Vuthaluru, H. B. ;
Korbee, R. ;
Kiel, J. H. A. .
FUEL PROCESSING TECHNOLOGY, 2009, 90 (09) :1148-1156