Please wait a minute...
J4  2013, Vol. 47 Issue (9): 1637-1643    DOI: 10.3785/j.issn.1008-973X.2013.09.019
能源工程     
 基于aspen plus的垃圾衍生燃料热解模拟与实验
李延吉1,2,姜璐1,邹科威1,赵宁1,李玉龙1,李润东1,池涌2
1.沈阳航空航天大学 清洁能源辽宁省重点实验室,辽宁 沈阳 110136;
2.浙江大学 能源清洁利用国家重点实验室,浙江 杭州 310027
Simulation and experimental of refuse derived fuel pyrolysis
 based on aspen plus
LI Yan-ji1,2,JIANG Lu1,ZOU Ke-wei1,ZHAO Ning1,LI Yu-long1,
LI Run-dong1,CHI Yong2
1.Clean Energy Key Laboratory of Liaoning, Shenyang Aerospace University,Shenyang 110136,China|
2.State Key Laboratory of Clean Energy Utilization, Zhejiang University, Hangzhou 310027,China
 全文: PDF  HTML
摘要:

采用化工流程模拟软件aspen plus对垃圾衍生燃料(RDF)建立热解反应模型,得出RDF各热解产物产率及气体体积分数.在高温管式炉中进行RDF热解实验,利用气相色谱分析仪测出各气体体积分数.将模拟值与实验值进行比较,结果表明:热解终温增加,热解液和热解气产率增大,半焦产率下降H2体积分数增加, CO2体积分数下降|与添加废石灰的RDF相比,添加污泥的RDF热解液和半焦产率更低,热解气产率更高|生物质质量分数下降,CO2体积分数下降|与添加废石灰RDF相比,添加污泥的RDF的CO2体积分数下降.

Abstract:

Conducted a simulation to the pyrolysis process of refuse derived fuel (RDF) based on chemical simulation software aspen plus firstly and established the pyrolysis reaction model to obtain the pyrolysis yields of RDF products and the volume fractions of pyrolysis gases. Then the pyrolysis experiment of RDF was conducted in a high-temperature tube furnace and the volume fractions of pyrolysis gases were measured by using gas chromatographic analyzer. By comparing the simulation values with experimental values, it is concluded that: the yields of pyrolysis liquid and gas increase with the increase of final pyrolysis temperature,but the yield of semi-coke decreases, while the H2 volume fraction increases but the CO2 volume fraction decreases| Compared to the RDF added waste lime, the RDF added sludge lower productivities of pyrolysis liquid and char, whereas has higher productivity of pyrolysis gas| the CO2 volume fraction reduces with the decrease of biomass content| moreover, the volume fraction of CO2 from the RDF added sludge is lower than that from the  RDF added waste lime.

出版日期: 2013-09-01
:  TK 09  
基金资助:

国家“973”重点基础研究发展规划资助项目(2011CB201500);国家水重大专项课题资助项目(2008ZX07313-006).

通讯作者: 池涌, 男, 教授.     E-mail: chiyong@zju.edu.cn
作者简介: 李延吉(1974-),男,副教授,从事工程热物理研究.E-mail:yanji0518@163.com
服务  
把本文推荐给朋友
加入引用管理器
E-mail Alert
RSS
作者相关文章  

引用本文:

李延吉,姜璐,邹科威,赵宁,李玉龙,李润东,池涌.  基于aspen plus的垃圾衍生燃料热解模拟与实验[J]. J4, 2013, 47(9): 1637-1643.

LI Yan-ji,JIANG Lu,ZOU Ke-wei,ZHAO Ning,LI Yu-long. Simulation and experimental of refuse derived fuel pyrolysis
 based on aspen plus. J4, 2013, 47(9): 1637-1643.

链接本文:

http://www.zjujournals.com/eng/CN/10.3785/j.issn.1008-973X.2013.09.019        http://www.zjujournals.com/eng/CN/Y2013/V47/I9/1637

[1] SOTUDEH-GHAREBAAGH R, LEGROS R, CHAOUKI J, et al.Simulation of circulating fluidized bed reactor using aspen plus[J]. Fuel , 1998 ,77:327-337.
[2] HYUN-MIN S, SEUNG-JONG L, YOUNG-DON Y, et al. Simulation of DME synthesis from coal syngas by kinetics model[J]. Chemical Engineering, 2009,26(3): 641-648.
[3] 马顺勤.基于aspen plus对整体煤气化联合循环系统的模拟分析[D].北京:华北电力大学,2008:7-34.
MA Sun-qin. Based on aspen plus of integrated gasification combined cycle system simulation analysis[D].Beijing: North China Electric Power University,2008: 7-34.
[4] 张瑞雪.生物质热解油气化实验与模拟研究[D]. 武汉:华中科技大学,2008:3-18.
ZHANG Rui-xue. Gasification experiment and simulation research of biomass pyrolysis oil[D].Wuhan: Huazhong University of Science and Technology,2008:3-18.
[5] 徐越,吴一宁,危师让. 基于aspen plus平台的干煤粉加压气流床气化性能模拟[J].西安交通大学学报, 2003, 37(7): 692694, 706.
XU Yue,WU Yi-ning,WEI Shi-rang. Simulation of the performance based on aspen plus for dry feed entrained flow coal gasification of entrained-bed gasifier[J].Journal of Xian Jiaotong University,2003,37(7):692694,706.
[6] 张斌,李政,江宁,等. 基于Aspen Plus 建立喷流床煤气化炉模型[J].化工学报,2003, 54(8): 1179-1182.
ZHANG Bin, LI Zheng, JIANG Ning, et al. Modeling of entrained bed coal gasifiers with aspen plus[J]. Journal of Chemical Industry and Engineering,2003,54(8): 1179-1182.
[7] SILVANO C, MARINA P, DIEGO B. Simulation of a waste incineration process with flue-gas cleaning and heat recovery sections using Aspen Plus[J]. Waste Management, 2005,25(10): 171-175.
[8] WAYNE D, ANTHONY R, DAVID K. The effect of air preheating in a biomass CFB gasifier using aspen plus simulation[J]. Biomass & Bioenergy, 2009,33(9):1158-1167.
[9] 陈汉平,赵向富,米铁,等. 基于aspen plus平台的生物质气化模拟[J].华中科技大学学报,2007,35(9):49-52.
CHEN Han-ping, ZHAO Xiang-fu, MI Tie, et al. Simulation of biomass gasification by aspen plus[J]. Journal of Huazhong University of Science and Technology, 2007, 35(9):49-52.
[10] 汪洋,代正华,于广锁,等. 运用Gibbs自由能最小化方法模拟气流床煤气化炉[J].煤炭转化,2004,27(4): 27-33.
WANG Yang, DAI Zheng-hua, YU Guang-suo, et al. Simulation of entrained-flow bed coal gasifier by the method of gibbs free energy minimization[J]. Coal Conversion, 2004,27(4): 27-33.
[11] 张巍巍, 曾国勇, 陈雪莉, 等. 生物质气流床气化前的处理工艺[J]. 过程工程学报,2007,7(4): 747-750.
ZHANG Wei-wei, ZENG Guo-yong, CHEN Xue-li, et al. Pretreatment technology of biomass entrained flow gasification[J].The Chinese Journal of Process Engineering, 2007,7(4): 747-750.
[12] DEMIRBAS A . Mechanisms of liquefaction and pyrolysis reactions of biomass[J]. Energy Conversion & Management, 2000, 41(6): 633-646.
[13] 王艳,张书廷,张于峰,等. 城市生活垃圾低温热解产气特性的实验研究[J]. 燃料化学学报,2005,33(1):62-67.
WANG Yan, ZHANG Shu-ting, ZHANG Yu-feng, et al. Gas formation characteristics during low temperature pyrolysis of municipal household garbage[J].Journal of Fuel Chemistry and Technology, 2005,33(1):62-67.
[14] 江建方,肖波,杨家宽,等. 城市生活垃圾热解产气特性的试验研究[J]. 环境科学与技术,2006,29(7): 79-81.
JIANG Jian-fang, XIAO Bo, YANG Jia-Kuan, et al. Pyrolysis gas characteristics of municipal solid waste[J].Environmental Science and Technology, 2006,29(7): 79-81.

No related articles found!