MATHEMATICAL-MODELING OF A FLUIDIZED-BED STRAW GASIFIER - PART II - MODEL SENSITIVITY

Citation
A. Ergudenler et al., MATHEMATICAL-MODELING OF A FLUIDIZED-BED STRAW GASIFIER - PART II - MODEL SENSITIVITY, Energy sources, 19(10), 1997, pp. 1085-1098
Citations number
12
Journal title
ISSN journal
00908312
Volume
19
Issue
10
Year of publication
1997
Pages
1085 - 1098
Database
ISI
SICI code
0090-8312(1997)19:10<1085:MOAFSG>2.0.ZU;2-R
Abstract
The sensitivity of the kinetic-free homogeneous equilibrium model, dev eloped for fluidized bed gasification of cereal straw, was tested unde r a wine range of parameters, including equivalence ratio, bed height, fluidization velocity solid circulation coefficient, nitrogen-oxygen ratio, and fuel distribution function. The results showed that the bed temperature was sensitive to changes in all of these parameters. The composition and the higher heating value of the produced gas were only affected by the equivalence ratio and the nitrogen-oxygen ratio. The normalized gas production was mainly affected by the equivalence ratio , fluidization velocity, and nitrogen-oxygen ratio.