BIOMASS ASH FLUIDISED-BED AGGLOMERATION: HYDRODYNAMIC INVESTIGATIONS

被引:0
|
作者
Balland, M. [1 ]
Froment, K. [1 ]
Ratel, G. [1 ]
Valin, S. [1 ]
Roussely, J. [1 ]
Michel, R. [2 ]
Poirier, J. [2 ]
Kara, Y. [3 ]
Galnares, A. [3 ]
机构
[1] CEA, DRT, LITEN, DTBH,SBRT,LTCB, 17 Rue Martyrs, F-38054 Grenoble 9, France
[2] Univ Orleans, CNRS, UPR3079, CEMHTI, F-45071 Orleans, France
[3] CRIGEN, ENGIE, 361 Ave President Wilson,BP33, F-93211 La Plaine St Denis, France
来源
PAPERS OF THE 24TH EUROPEAN BIOMASS CONFERENCE: SETTING THE COURSE FOR A BIOBASED ECONOMY | 2016年
关键词
gasification; fluidized-bed; ashes; biomass; modelling; SURFACE-TENSION; PREDICTION;
D O I
暂无
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Agglomeration and defluidisation (A/D) processes in fluidised-bed reactors (FBR) are a real difficulty encountered when gasifying feedstock with high ash content. According to the elemental ash composition, a liquid phase may form at the operating temperature and glue the bed particles together, thus starting disturbing the hydrodynamic of the bed, as well as the conversion efficiency. Finally, it leads to the complete defluidisation of the reactor. This work aims to investigate the influence of agglomeration on the hydrodynamic behaviour of a FBR. The identification of the main parameters involved in A/D and the study of their influence on these processes are carried out inside both a laboratory fluidised-bed operating at high temperature (700-1000 degrees C) and a cold-flow fluidised-bed at ambient temperature. The effect of the in-bed liquid fraction, the liquid properties and the operating parameters are investigated in relation to the agglomeration process and the hydrodynamic behaviour. Based on these results, a simplified modelling approach is given in order to predict the operating time before the complete defluidisation of the reactor.
引用
收藏
页码:524 / 532
页数:9
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