Biomass pyrolysis in fully-developed turbulent riser flow

被引:24
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
相关论文
共 64 条
[1]   The role of meso-scale structures in rapid gas-solid flows [J].
Agrawal, K ;
Loezos, PN ;
Syamlal, M ;
Sundaresan, S .
JOURNAL OF FLUID MECHANICS, 2001, 445 :151-185
[2]   Filtered models for scalar transport in gas-particle flows [J].
Agrawal, Kapil ;
Holloway, William ;
Milioli, Christian C. ;
Milioli, Fernando E. ;
Sundaresan, Sankaran .
CHEMICAL ENGINEERING SCIENCE, 2013, 95 :291-300
[3]   A FLUID MECHANICAL DESCRIPTION OF FLUIDIZED BEDS [J].
ANDERSON, TB ;
JACKSON, R .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1967, 6 (04) :527-&
[4]  
[Anonymous], 2012, BIOMASS BIOENERG
[5]  
[Anonymous], 2003, BIORENEWABLE RESOURC
[6]   Turbulent Dispersed Multiphase Flow [J].
Balachandar, S. ;
Eaton, John K. .
ANNUAL REVIEW OF FLUID MECHANICS, 2010, 42 :111-133
[7]   CFD modeling of space-time evolution of fast pyrolysis products in a bench-scale fluidized-bed reactor [J].
Boateng, A. A. ;
Mtui, P. L. .
APPLIED THERMAL ENGINEERING, 2012, 33-34 :190-198
[8]   KINETIC-MODEL FOR PYROLYSIS OF CELLULOSE [J].
BRADBURY, AGW ;
SAKAI, Y ;
SHAFIZADEH, F .
JOURNAL OF APPLIED POLYMER SCIENCE, 1979, 23 (11) :3271-3280
[9]   Effect of Domain Size on Fluid-Particle Statistics in Homogeneous, Gravity-Driven, Cluster-Induced Turbulence [J].
Capecelatro, Jesse ;
Desjardins, Olivier ;
Fox, Rodney O. .
JOURNAL OF FLUIDS ENGINEERING-TRANSACTIONS OF THE ASME, 2016, 138 (04)
[10]   On fluid-particle dynamics in fully developed cluster-induced turbulence [J].
Capecelatro, Jesse ;
Desjardins, Olivier ;
Fox, Rodney O. .
JOURNAL OF FLUID MECHANICS, 2015, 780 :578-635