Biomass pyrolysis in fully-developed turbulent riser flow

被引:20
|
作者
Beetham, S. [1 ]
Capecelatro, J. [1 ]
机构
[1] Univ Michigan, Dept Mech Engn, Ann Arbor, MI 48105 USA
基金
美国国家科学基金会;
关键词
Multiphase; Turbulence; Biomass pyrolysis; Euler-Lagrange; CFD; Riser; DIRECT NUMERICAL-SIMULATION; GAS-SOLID FLOW; FLUIDIZED-BED; HEAT-TRANSFER; KINETIC-MODEL; REACTOR; PARTICLES; CELLULOSE; DYNAMICS; CLUSTERS;
D O I
10.1016/j.renene.2019.03.095
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
This work presents a numerical study of biomass pyrolysis in turbulent riser flow. Eulerian Lagrangian simulations of unbounded sedimenting gas-solid flows are performed to isolate the effects of particle clustering on the production of syngas and tar. This configuration provides a framework to resolve the relevant length- and time-scales associated with thermal, chemical and multiphase processes taking place in the fully-developed region of a circulating fluidized bed riser. A four-step kinetic scheme is employed to model the devolatilization of biomass particles and secondary cracking of tar. Two-way coupling between the phases leads to clusters of sand particles that generate and sustain gas-phase turbulence and transport biomass particles. Neglecting the heterogeneity caused by clusters was found to lead to a maximum over-prediction of syngas yield of 33%. Further, it was found that two-dimensional simulations over-predict the level of clustering, resulting in an under-prediction of syngas and tar yields. (C) 2019 Elsevier Ltd. All rights reserved.
引用
收藏
页码:751 / 760
页数:10
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