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流化床中污泥干燥特性
引用本文:邵志伟,黄亚继,严玉朋,杨高强,伏启让. 流化床中污泥干燥特性[J]. 环境工程学报, 2014, 8(9): 3965-3970
作者姓名:邵志伟  黄亚继  严玉朋  杨高强  伏启让
作者单位:东南大学能源热转换及其过程测控教育部重点实验室, 南京 210096;东南大学能源热转换及其过程测控教育部重点实验室, 南京 210096;东南大学能源热转换及其过程测控教育部重点实验室, 南京 210096;东南大学能源热转换及其过程测控教育部重点实验室, 南京 210096;东南大学能源热转换及其过程测控教育部重点实验室, 南京 210096
基金项目:国家重点基础研究发展计划(973)资助项目(2011CB201505);江苏省环保厅课题(2012027)
摘    要:
以湿污泥为原料在气固流动流化床干燥器内进行了污泥干燥特性的实验研究,考察流化风速、送风温度、联合干燥热量配比的变化对干燥强度、干燥热效率及平均传热系数的影响。实验结果表明,流化床污泥干燥最佳流化风速为1.48 m/s左右;随着流化风温的升高,干燥强度和干燥热效率逐渐增大,但增幅减小;单独的加热管干燥和流化风干燥的干燥热效率均较低,分别为33%和45%左右。在相同总输入热量下,随着内置加热管输入热量的比重越来越大,干燥热效率、干燥强度和平均传热系数均先增大后减小。

关 键 词:流化床  污泥  干燥特性  干燥热效率

Drying characteristics of sludge in a fluidized bed
Shao Zhiwei,Huang Yaji,Yan Yupeng,Yang Gaoqiang and Fu Qirang. Drying characteristics of sludge in a fluidized bed[J]. Techniques and Equipment for Environmental Pollution Control, 2014, 8(9): 3965-3970
Authors:Shao Zhiwei  Huang Yaji  Yan Yupeng  Yang Gaoqiang  Fu Qirang
Affiliation:Key Laboratory of Energy Thermal Conversion and Control of Ministry of Education, Southeast University, Nanjing 210096, China;Key Laboratory of Energy Thermal Conversion and Control of Ministry of Education, Southeast University, Nanjing 210096, China;Key Laboratory of Energy Thermal Conversion and Control of Ministry of Education, Southeast University, Nanjing 210096, China;Key Laboratory of Energy Thermal Conversion and Control of Ministry of Education, Southeast University, Nanjing 210096, China;Key Laboratory of Energy Thermal Conversion and Control of Ministry of Education, Southeast University, Nanjing 210096, China
Abstract:
An experimental investigation on the drying characteristics of wet sludge was carried in a bubbling fluidized bed. The effects of fluidized wind speed, air supply temperature and combined drying heat ratio on drying strength, drying thermal efficiency and average heat transfer coefficient were investigated. The results show that the best fluidized wind speed by fluidized bed drying is about 1.48 m/s. With the air supply temperature increasing, drying strength and drying thermal efficiency both increase, but the growth extent decreases. The thermal efficiency of separate heating tube drying and fluidized wind drying are relatively lower, respectively about 33% and 45%. Drying thermal efficiency, drying strength and average heat transfer coefficient all increase and then decrease with the increasing proportion of built-in heating pipes heat input for the same total heat input.
Keywords:fluidized bed  sludge  drying characteristics  drying thermal efficiency
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