Comparing calcined and un-treated olivine as bed materials for tar reduction in fluidized bed gasification

2014 ◽  
Vol 124 ◽  
pp. 275-285 ◽  
Author(s):  
Chr. Christodoulou ◽  
D. Grimekis ◽  
K.D. Panopoulos ◽  
E.P. Pachatouridou ◽  
E.F. Iliopoulou ◽  
...  
2010 ◽  
Vol 132 (3) ◽  
Author(s):  
Vijay Jain ◽  
Prabir Basu ◽  
Dominic Groulx

A study on the heating of inert bed solids in a bubbling fluidized bed by means of an over-bed start-up oil burner is presented in this paper. Experiments carried out in a 160 mm diameter bed shows that the bed heats up nonlinearly with time. The rate of heating and the peak temperature reached by the bed solids depend on the bed depth, the mean particle size, and the superficial velocity through the bed. It was further noted that premixing a certain amount of biomass with the inert bed solids accelerates the rate of heating, as well as increase the peak temperature attained. The internal heat generation in the biomass is found to start at temperatures as low as 200°C. Thus, premixing some biomass with inert bed materials could reduce the combustion start-up time of a fluidized bed boiler, reducing at the same time the start-up cost by saving on consumption of expensive fuel oil in the burner. Experimental data in the present laboratory-scale unit shows good agreement with those obtained earlier in an industrial fluidized bed tested with waste-coal.


2016 ◽  
Vol 30 (6) ◽  
pp. 4848-4857 ◽  
Author(s):  
Teresa Berdugo Vilches ◽  
Jelena Marinkovic ◽  
Martin Seemann ◽  
Henrik Thunman

2015 ◽  
Vol 69 ◽  
pp. 1741-1749 ◽  
Author(s):  
T. Etori ◽  
N. Gokon ◽  
A. Takeuchi ◽  
T. Miki ◽  
M. Yokota ◽  
...  

2010 ◽  
Vol 49 (22) ◽  
pp. 11294-11301 ◽  
Author(s):  
Manuel Campoy ◽  
Alberto Gómez-Barea ◽  
Diego Fuentes-Cano ◽  
Pedro Ollero
Keyword(s):  

1999 ◽  
Vol 13 (4) ◽  
pp. 773-777 ◽  
Author(s):  
Hans-Jürgen Franke ◽  
Tadaaki Shimizu ◽  
Akira Nishio ◽  
Hiroyuki Nishikawa ◽  
Makoto Inagaki ◽  
...  

2011 ◽  
Vol 354-355 ◽  
pp. 338-343
Author(s):  
Qian Jun Li ◽  
Dong Ping Zhang

Experimental investigations on hydrodynamic characteristics of cylindrical pressurized spout-fluidizing bed were carried out. Two kinds of millet were used as bed materials. The operational pressure is 0.1MPa~0.4MPa (absolutely pressure). Five distinct flow patterns, i.e, fixed bed(FB), jet in fluidized bed with bubbles(JFB), jet in fluidized bed with slugging(JFS), spout with aeration(SA) and spout-fluidizing bed(SF) were identified. Effects of the static bed height and operational pressure on the flow pattern map were particularly studied. Typical flow pattern images obtained by a high- resolution digital CCD camera were presented for classifying these flow patterns. Typical flow pattern maps were plotted for describing the transitions between flow patterns with operating conditions


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