期刊文献+

烧结余热利用中烧结混合料干燥过程实验研究 被引量:7

Experimental Study on Drying Process of Mixture Being Sintered Utilizing Waste Heat
在线阅读 下载PDF
导出
摘要 利用自行设计的实验装置,开展了kg级烧结混合料干燥实验,研究了干燥介质流量和温度对干燥过程的影响.结果表明:干燥过程是由较短的升速段、较长的恒速段及一定的降速段组成,其中恒速段表现为分段性;升速段、恒速段、降速段对应的水的质量分数(指干基水的质量分数,下同)分别为6.5%~7.5%,2%~6.5%和2%以下;升速段约发生在干燥前10 min内,且当水的质量分数为7.0%~7.5%时,干燥速率最大;不同工况下临界水的质量分数不同,其介于1.6%~2.8%之间;干燥介质流量和温度是影响干燥过程的主要因素,在一定范围内,流量越大,温度越高,干燥速率越大,但它们不成线性关系;干燥介质流量与温度均存在适宜范围. An experimental setup was developed to test the drying process of a mixture(in kg) being sintered,with the effects of drying air flowrate and temperature on the drying process investigated.The results revealed that the whole drying process can be divided into three stages according to the drying rate,i.e.,the short rate-rising,long constant rate and fixed rate-dropping,among which the long constant rate stage can further be divided into 2~3 substages.The water contents corresponding the three stages are 6.5%~7.5%,2%~6.5% and below 2%,respectively.The rate-rising stage occurs in about the first 10 min of the drying process and the rate comes up to its maximum value when the water content is 7.0%~7.5%.The critical water content changes in the range from 1.6%~2.8% under different experimental conditions,and the drying air flowrate and temperature are both verified the main influencing factors on drying process.To a certain extent,the higher the air flowrate and temperature,the higher drying rate,but the relationship between air flowrate or temperature and drying rate is nonlinear.Both drying air flowrate and temperature should be set in appropriate range.
出处 《东北大学学报(自然科学版)》 EI CAS CSCD 北大核心 2010年第4期546-549,共4页 Journal of Northeastern University(Natural Science)
基金 国家高技术研究发展计划项目(2009AA05Z215 2008AA042901)
关键词 烧结 混合料 干燥 水的质量分数 余热 sintering mixture drying water content in percentage waste heat
  • 相关文献

参考文献3

二级参考文献8

共引文献180

同被引文献76

  • 1耿春景,李汛,朱强.高炉冲渣水发电项目的可行性研究[J].节能技术,2005,23(3):228-231. 被引量:21
  • 2赵增华,赵杉林,张振华,李萍,李君华.相对湿度和温度对铁锈硫化物氧化倾向性影响[J].石油化工高等学校学报,2006,19(4):8-10. 被引量:8
  • 3蔡九菊,王建军,陈春霞,陆钟武.钢铁企业余热资源的回收与利用[J].钢铁,2007,42(6):1-7. 被引量:153
  • 4Jang J Y, Chiu Y W. 3-D transient conjugated heat transfer and fluid flow analysis for the cooling[J ]. Applied Thermal Engineering, 2009,29(14/15) :2895- 2903.
  • 5Amara S B, Laguerre O, Flick D. Experimental study of convective heat transfer during cooling with low air velocity in a stack of objects[J]. International Journal of Thermal Sciences, 2004,43:1213 - 1221.
  • 6Caputo A C, Carsarelli G, Pelagagge P M. Analysis of heat recovery in gas-solid moving beds using a simulation approach [J]. Applied Thermal Engineering, 1996,16(1):89-99.
  • 7Ferreria L M, Castro J A M, Rodrigues A E. An analytical and experimental study of heat transfer in fixed bed [ J ]. International Journal of Heat and Mass Transfer, 2002, 45 : 951 - 961.
  • 8Laguerre O, Amara S B, Flick D. Heat transfer between wall and packed bed crossed by low velocity airflow [ J ]. Applied Thermal Engineering, 2006, 26 ( 16 ) : 1951 - 1960.
  • 9Maruoka N, Mizuoehi T, Purwanto H, et al. Feasibility study for recovering waste heat in the steelmaking industry using a chemical recuperator[J ]. ISIJ International, 2004, 44(2) :257 - 262.
  • 10Pelagagge P M, Caputo A C, Cardarelli G. Comparing heat recovery schemes in solid bed cooling[J ]. Applied Thermal Engineering, 1997,17( 11 ) : 1045 - 1054.

引证文献7

二级引证文献47

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