Computational fluid dynamics and discrete element simulation of the formation of inorganic syngas contaminants during lignocellulosic biomass gasification

被引:4
作者
Oyedeji, Oluwafemi [1 ]
Abdoulmoumine, Nourredine [2 ,3 ]
机构
[1] Oak Ridge Natl Lab, Div Environm Sci, POB 2008, Oak Ridge, TN 37831 USA
[2] Univ Tennessee, Biosyst Engn & Soil Sci Dept, Knoxville, TN 37996 USA
[3] Univ Tennessee, Ctr Renewable Carbon, Knoxville, TN 37996 USA
关键词
BENCH-SCALE GASIFICATION; OPERATIONAL CONDITIONS; COAL-GASIFICATION; PRODUCT GAS; CEDAR WOOD; FLOW; STEAM; TEMPERATURE; PARTICLES; PYROLYSIS;
D O I
10.1039/d0se00705f
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
We report in this study the development of a computational fluid dynamics and discrete element method (CFD-DEM) model to predict the yield of deleterious nitrogen and sulfur contaminants (NH3, HCN, H2S, COS, and SO2) during biomass gasification. Additionally, the yields of major producer gas species (CO, CO2, CH4, and H-2) were predicted. The formation of nitrogen contaminants was assumed to follow a heterogeneous reaction producing HCN, which was later hydrolyzed to form NH3. Similarly, the formation of sulfur contaminants was assumed to follow a heterogeneous reaction producing H2S, which was later oxidized to form COS and SO2. The effects of two important gasification process variables (temperature and equivalence ratio) were evaluated. The results of the CFD-DEM simulation were validated against experimental data in the literature. The CFD-DEM model yield predictions for the main syngas species (CO, CO2, H-2, and CH4) compares well with the experimental results. Also, the predicted yields of NH(3)and H2S generally fit within a 95% confidence interval of the experimental data. However, the predicted yields of HCN were about 20-50% lower than the experimental data. The main outcome of this work is a computational tool that can be used to gain in-depth knowledge to better understand how to optimize process variables for mitigating the formation of nitrogen and sulfur contaminants during gasification.
引用
收藏
页码:4219 / 4231
页数:13
相关论文
共 43 条
[1]   Large eddy simulations of coal gasification in an entrained flow gasifier [J].
Abani, Neerav ;
Ghoniem, Ahmed F. .
FUEL, 2013, 104 :664-680
[2]   A review on biomass gasification syngas cleanup [J].
Abdoulmoumine, Nourredine ;
Adhikari, Sushil ;
Kulkarni, Avanti ;
Chattanathan, Shyamsundar .
APPLIED ENERGY, 2015, 155 :294-307
[3]   Effects of Temperature and Equivalence Ratio on Pine Syngas Primary Gases and Contaminants in a Bench-Scale Fluidized Bed Gasifier [J].
Abdoulmoumine, Nourredine ;
Kulkarni, Avanti ;
Adhikari, Sushil .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2014, 53 (14) :5767-5777
[4]  
Adhikari S, 2017, WOODHEAD PUBL SER EN, P541, DOI 10.1016/B978-0-08-101031-0.00016-8
[5]   Bench-scale gasification of cedar wood - Part I: Effect of operational conditions on product gas characteristics [J].
Aljbour, Salah H. ;
Kawamoto, Katsuya .
CHEMOSPHERE, 2013, 90 (04) :1495-1500
[6]   Bench-scale gasification of cedar wood - Part II: Effect of Operational conditions on contaminant release [J].
Aljbour, Salah H. ;
Kawamoto, Katsuya .
CHEMOSPHERE, 2013, 90 (04) :1501-1507
[7]  
[Anonymous], 2010, Crit Care, V14
[8]  
[Anonymous], OP SOURC CFD TOOLB
[9]  
Basu P, 2010, BIOMASS GASIFICATION AND PYROLYSIS: PRACTICAL DESIGN AND THEORY, P1
[10]   Simulation of particles and gas flow behavior in the riser section of a circulating fluidized bed using the kinetic theory approach for the particulate phase [J].
Benyahia, S ;
Arastoopour, H ;
Knowlton, TM ;
Massah, H .
POWDER TECHNOLOGY, 2000, 112 (1-2) :24-33