期刊文献+

H_2O和CO_2对焦炭溶损反应动力学的研究 被引量:17

Study on Solution Loss Reaction Kinetics of Coke with H_2O and CO_2
原文传递
导出
摘要 采用自制高温气固相反应连续测定装置,研究了900~1100℃下,CO2,H2O及其混合气体与焦炭的溶损反应.结果表明,焦炭与H2O反应的溶损率远高于其与CO2反应后的溶损率,前者是后者的2~5倍.相比与CO2的反应,焦炭与H2O的反应在颗粒外围更为剧烈,且不易在中心部位生成大的串孔及裂纹.900℃时,与CO2、H2O反应开始的焦炭的主要气化方式分别为微孔生成、小孔扩张;1100℃时,分别为小孔扩张、微孔生成.随着混合气体中H2O含量的增加,焦炭的溶损率不断增加.当[H2O]/[CO2]=5/5和7/3时,焦炭与混合气体的共气化过程中均产生了明显的交互作用.用缩核反应模型描述了焦炭与H2O和CO2气化反应的结果,得反应活化能分别为154.47和214.77kJ/mol. The effects of CO2, H20 and their mixture on coke degradation were studied from 900℃ to 1100℃ by self-command continuous measurement device for high temperature gas-solid reaction. The results show that the solution loss rate of coke reacting with H2O is 2-5 times of that of the coke with CO2. Compared with the coke reacting with CO2, the chemical reaction of coke with H2O is much more intense in the periphery of coke, and it is not easy to generate big holes and cracks in its center part. The main gasification ways of coke beginning to react with CO2 and H2O are micro-hole formation and pore expansion respectively when the temperature is 900 ℃; that of coke beginning to react with CO2 and H2O are pore expansion and micro-hole formation respectively when the temperature is 1100℃. The solution loss rate of coke increases with increasing of H2O in gaseous mixture. The synergistic effect of coke and H20-CO2 gaseous mixture is apparent when the ratio of H2O to CO2 in the mixture is 5/5 or 7/3 during the gasification process. The shrinking core model was used to describe the gasification results of coke reacting with H2O and CO2. Their activation energy is 154.47 and 214.77 k J/tool respectively.
出处 《过程工程学报》 CAS CSCD 北大核心 2012年第5期789-795,共7页 The Chinese Journal of Process Engineering
关键词 焦炭 H2O CO2 溶损率 微观结构 交互作用 coke H20 CO2 solution loss rate micro-structure synergistic effect
  • 相关文献

参考文献12

  • 1Ohno Y, Hotta H. Test of Oxygen Blast Furnace Process withExperimental Blast Furnace Process (Development of Oxygen BlastFurnace Process I) [J].Trans. ISIJ, 1987,(27): 219-226.
  • 2Babich A, Yaroshevsik S, Formoso A,et al. CO Injection ofNon-coking Coal and Natural Gas in Blast Furnace [J]. ISIJ Int., 1999,39(3): 229-238.
  • 3陈淼.纯氧高炉喷吹天然气高炉的工艺计算和实验研究[D].马鞍山:安徽工业大学,2006.
  • 4邓守强.高炉炼铁技术[M].北京:冶金工业出版社,1990.55-57.
  • 5韩毅华,王静松,李燕珍,佘雪峰,孔令坛,薛庆国.炉顶煤气循环—氧气鼓风高炉综合数学模型[J].北京科技大学学报,2011,33(10):1280-1286. 被引量:31
  • 6Iwanaga Y. Degradation Behavior of Coke at High Temperatures inBlast Furnace [J].Ironmaking Steelmaking, 1989, 16(2): 101-109.
  • 7李家新,卢开成,汪涧江,王平.H_2O-CO_2混合气体对焦炭劣化反应的影响[J].安徽工业大学学报(自然科学版),2008,25(3):233-236. 被引量:12
  • 8Pusz S, Krzesinska M, Smedowski L, et al. Changes in a CokeStructure Due to Reaction with Carbon Dioxide [J].InternationalJournal of Coal Geology,2010, (81): 287-292.
  • 9崔平,杨敏,康士刚,汪洋.二氧化碳浸蚀后的焦炭微观结构研究[J].燃料与化工,2006,37(4):5-7. 被引量:10
  • 10金慧军,傅永宁.焦炭-CO_2反应过程中孔隙结构的变化[J].煤化工,1991(1):11-17. 被引量:11

二级参考文献31

共引文献94

同被引文献168

引证文献17

二级引证文献80

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部