Low-Order Modeling of Internal Heat Transfer in Biomass Particle Pyrolysis

被引:24
|
作者
Wiggins, Gavin M. [1 ]
Ciesielski, Peter N. [2 ]
Daw, C. Stuart [1 ]
机构
[1] Oak Ridge Natl Lab, 2360 Cherahala Blvd, Knoxville, TN 37932 USA
[2] Natl Renewable Energy Lab, 15013 Denver West Pkwy, Golden, CO 80401 USA
关键词
FLUIDIZED-BED REACTOR; EXPERIMENTAL VALIDATION; MATHEMATICAL-MODEL; MASS-TRANSFER; WOOD; KINETICS; TRANSPORT; DEVOLATILIZATION; DECOMPOSITION; GASIFICATION;
D O I
10.1021/acs.energyfuels.6b00554
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
We present a computationally efficient, one-dimensional simulation methodology for biomass particle heating under conditions typical of fast pyrolysis. Our methodology is based on identifying the rate limiting geometric and structural factors for conductive heat transport in biomass particle models with realistic morphology to develop low-order approximations that behave appropriately. Comparisons of transient temperature trends predicted by our one-dimensional method with three-dimensional simulations of woody biomass particles reveal good agreement, if the appropriate equivalent spherical diameter and bulk thermal properties are used. We conclude that, for particle sizes and heating regimes typical of fast pyrolysis, it is possible to simulate biomass particle heating with reasonable accuracy and minimal computational overhead, even when variable size, aspherical shape, anisotropic conductivity, and complex, species-specific internal pore geometry are incorporated.
引用
收藏
页码:4960 / 4969
页数:10
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