铁矿石载氧体甲烷还原热重动力学分析

张怿,金保昇,王晓佳,刘先立,刘溪

电力建设 ›› 2013, Vol. 34 ›› Issue (6) : 7-10.

PDF(714 KB)
PDF(714 KB)
电力建设 ›› 2013, Vol. 34 ›› Issue (6) : 7-10.
重点理论研究

铁矿石载氧体甲烷还原热重动力学分析

  • 张怿,金保昇,王晓佳,刘先立,刘溪
作者信息 +

Research on Methane Reduction Kinetics of Iron Ore Oxygen Carrier Based on TGA

  • ZHANG Yi,JIN Baosheng,WANG Xiaojia,LIU Xianli,LIU Xi
Author information +
文章历史 +

摘要

介绍了一种能够同时实现高效率发电和低能耗分离CO2的新颖电站锅炉燃烧方式 — 化学链燃烧(chemical-looping combustion, CLS),并基于徐州利国铁矿矿石制备铁基载氧体,以CH4为还原性气体进行了热重实验(thermogravimetric analysis, TGA),并针对TGA曲线数据进行了化学动力学分析。分析结果表明,温度是影响载氧体还原程度的重要因素,温度升高导致还原速率加快、还原程度加深。还原反应过程在450~700 ℃温度段由扩散控制的Valensi方程模型控制,而在850~1 050 ℃温度段则由收缩球体模型控制,并依据模型分别计算出了相应模型的活化能和频率因子,为CLC应用于电力生产领域提供了理论指导。

Abstract

A novel combustion method used in boiler chemical-looping combustion(CLC) is introduced, which can simultaneously realize high-efficiency power generation and low-energy CO2 separation. Thermogravimetric analysis (TGA) was carried out in methane atmosphere, with iron ore from Xuzhou Liguo Iron Mine as the oxygen carrier, as well as the chemical kinetics was analyzed based on TGA curves. The results show that temperature is the key factor to the reduction of iron-based oxygen carrier, in which the reduction rate becomes faster and the reduction degree becomes deeper with the increase of temperature. In addition, the Valensi model between 450-700 ℃ and the contractive sphere model between 850-1 050 ℃ are most suitable for the reduction of the iron-based oxygen carrier, and the kinetic parameters including activation energy and pre-exponential factor are calculated according to the kinetic model respectively. The research results can provide theoretical guidance for CLC applied in electric power industry.

关键词

分离CO2 / 载氧体 / 化学链燃烧(CLC) / 热重分析(TGA) / 指前因子 / 活化能

Key words

CO2 separation / oxygen carrier / chemical-looping combustion(CLC) / thermogravimetric analysis (TGA) / pre-exponential factor / activation energy

引用本文

导出引用
张怿,金保昇,王晓佳,刘先立,刘溪. 铁矿石载氧体甲烷还原热重动力学分析[J]. 电力建设. 2013, 34(6): 7-10
ZHANG Yi,JIN Baosheng,WANG Xiaojia,LIU Xianli,LIU Xi. Research on Methane Reduction Kinetics of Iron Ore Oxygen Carrier Based on TGA[J]. Electric Power Construction. 2013, 34(6): 7-10

参考文献

 


[1]宋启磊.基于钙基载氧体化学链燃烧反应机理的研究[D]. 南京:东南大学,2009. 

[2]霍志红. 增压富氧燃烧CFB传热特性研究[D]. 保定:华北电力大学,2011. 

[3]Herzog H J. The economics of CO2 capture[C]// Proceedings of Fourth International Conference on Greenhouse Gas Control Technologies. London:Pergamon ress,1999:101-106. 

[4]肖睿,张帅,郑文广.铁基载氧体的燃煤加压化学链燃烧循环反应特性[J].东南大学学报:自然科学版,2010,40(5):985-991. 

[5]Richter H J, Knoche K F. Reversibility of combustion processes[C]//ACS Symposium Series 235. Washington DC,1983:71-85. 

[6]Song B H,Kim S D. Catalytic activity of alkali and iron salt mixtures for steam-char gasification[J]. Fuel,1993,72:797-803. 

[7]郑瑛,池保华,王保文,等.燃煤CO2减排技术 [J].中国电力,2006,39(10):91-94. 

[8]高正平,沈来宏,肖军,等. 基于Fe2O3载氧体的煤化学链燃烧试验 [J]. 工程热物理学报,2009,30(7):1249-1252. 

[9]Jin H G,Hong H,Han T.Progress of energy system with chemical-looping combustion [J].Chin Sci Bull,2008,54(6):906-919. 

[10]高正平,沈来宏,肖军,等. 煤化学链燃烧Fe2O3载氧体的反应性研究 [J]. 燃料化学学报,2009,37 (5) : 513-520. 

[11]宋涛,沈来宏,肖军,等. 铁矿石载氧体化学链燃烧高温还原表征 [J]. 燃料化学学报,2011,39(8):567-574. 

[12]孙小燕,向文国,田文栋,等. 基于Fe3O4的化学链制氢动力学特性 [J]. 燃烧科学与技术,2011,17(6):535-540. 

[13]魏永刚,王华,何方. 氧化铁作为氧载体在无烟燃烧技术中反应活化能的确定[J]. 工业加热,2007,36(2):16-18.

基金

国家自然科学基金资助项目(51076029);国际科技合作项目(2010DFA61960)。


PDF(714 KB)

Accesses

Citation

Detail

段落导航
相关文章
AI小编
你好!我是《电力建设》AI小编,有什么可以帮您的吗?

/