Simulation of municipal solid waste gasification for syngas production in fixed bed reactors

被引:34
作者
Chen, Chong [1 ]
Jin, Yu-qi [1 ]
Yan, Jian-hua [1 ]
Chi, Yong [1 ]
机构
[1] Zhejiang Univ, State Key Lab Clean Energy Utilizat, Hangzhou 310027, Peoples R China
来源
JOURNAL OF ZHEJIANG UNIVERSITY-SCIENCE A | 2010年 / 11卷 / 08期
关键词
Municipal solid waste (MSW); Gasification; Syngas; Aspen plus; Fixed bed; ASPEN-PLUS; DOWNDRAFT GASIFIER; BIOMASS GASIFICATION; PARTIAL OXIDATION; GAS; TECHNOLOGY; CONVERSION; DESIGN; MODEL; PLANT;
D O I
10.1631/jzus.A0900792
中图分类号
T [工业技术];
学科分类号
08 ;
摘要
This study proposes a model of syngas production from municipal solid waste (MSW) gasification with air in fixed bed reactors. The model (using Aspen plus simulator) is used to predict the results of MSW gasification and to provide some process fundamentals concerning syngas production from MSW gasification. The effects of gasification temperature, air equivalence ratio and moisture concentration on the composition of syngas, lower heating value (LHV) of syngas, heat conversion efficiency, and carbon conversion are discussed. The results indicate that higher temperature improves gasification, and higher air equivalence ratio increases the carbon conversion while decreasing syngas LHV. Heat conversion efficiency increases and reaches the maximum and then decreases with the increase of air equivalence ratio. Higher moisture concentration increases the carbon conversion and increases the heat conversion efficiency at lower ratios. Higher temperature and a lower equivalence ratio are favorable for obtaining a higher LHV of syngas at the same moisture concentration.
引用
收藏
页码:619 / 628
页数:10
相关论文
共 29 条
[1]   Continuous in-line gasification/vitrification process for thermal waste treatment: process technology and current status of projects [J].
Calaminus, B ;
Stahlberg, R .
WASTE MANAGEMENT, 1998, 18 (6-8) :547-556
[2]  
[陈汉平 Chen Hanping], 2007, [华中科技大学学报. 自然科学版, Journal of Huazhong University of Science and Technology. Nature Science], V35, P49
[3]   Simulation of a waste incineration process with flue-gas cleaning and heat recovery sections using Aspen Plus [J].
Cimini, S ;
Prisciandaro, M ;
Barba, D .
WASTE MANAGEMENT, 2005, 25 (02) :171-175
[4]   Biomass and fossil fuel conversion by pressurised fluidised bed gasification using hot gas ceramic filters as gas cleaning [J].
de Jong, W ;
Ünal, Ö ;
Andries, J ;
Hein, KRG ;
Spliethoff, H .
BIOMASS & BIOENERGY, 2003, 25 (01) :59-83
[5]   Drying characteristics of wood cylinders for conditions pertinent to fixed-bed countercurrent gasification [J].
Di Blasi, C ;
Branca, C ;
Sparano, S ;
La Mantia, B .
BIOMASS & BIOENERGY, 2003, 25 (01) :45-58
[6]   Gasification of hazelnut shells in a downdraft gasifier [J].
Dogru, M ;
Howarth, CR ;
Akay, G ;
Keskinler, B ;
Malik, AA .
ENERGY, 2002, 27 (05) :415-427
[7]   Measurements of mass flux and stoichiometry of conversion gas from three different wood fuels as function of volume flux of primary air in packed-bed combustion [J].
Friberg, R ;
Blasiak, W .
BIOMASS & BIOENERGY, 2002, 23 (03) :189-208
[8]   Numerical investigation of the partial oxidation in a two-stage downdraft gasifier [J].
Gerun, Luc ;
Paraschiv, Maria ;
Vijeu, Razvan ;
Bellettre, Jerome ;
Tazerout, Mohand ;
Gobel, Benny ;
Henriksen, Ulrik .
FUEL, 2008, 87 (07) :1383-1393
[9]   The development of a computer model for a fixed bed gasifier and its use for optimization and control [J].
Gobel, Benny ;
Henriksen, Ulrik ;
Jensen, Torben Kvist ;
Qvale, Bjorn ;
Houbak, Niels .
BIORESOURCE TECHNOLOGY, 2007, 98 (10) :2043-2052
[10]   Simulation of the flue gas cleaning system of an RDF incineration power plant [J].
Jannelli, E. ;
Minutillo, M. .
WASTE MANAGEMENT, 2007, 27 (05) :684-690