欢迎登录材料期刊网

材料期刊网

高级检索

非均匀布风对流化床埋管换热特性有一定的影响,埋管的对流换热系数不仅是埋管所处换热区流化速度的函数,而且与相邻的流动区流化速度有一定关系。本文通过试验研究了埋管换热系数同换热区以及流动区流化速度之间的关系:换热系数变化的趋势及数值的大小与鼓泡床有明显不同,较大的流动区流化速度(6.0umf~24.0umf)直接影响换热区埋管的换热系数,换热系数同流化速度之间较为平缓的关系便于利用埋管进行非均匀布风流化床中浓相床区温度的调整与控制

The heat transfer of immersed tubes in fluidized beds is influenced by theuneven distribution of fluidized air, and the coefficient of that is not onlya function of fluidized air velocity in heat transfer zone, but also iscorrelative with the air velocity in fluidized zone nearby. In this paper,the relationship between the heat transfer coefficient and the airvelocities of heat transfer zone and fluidized zone is investigatedexperimentally. The trend and data of heat transfer coefficients are differentobviously with those of bubbling bed. They are influenced directly by thegrater air velocity in fluidized zone (6.0umf~24.0umf). The flatrelation curve between the heat transfer coefficients and fluidized airvelocities is favorable to adjust the dense bed temperature using the immersedtubes in fluidized bed with uneven distribution of air

参考文献

[1] J F D Harrison.流态化[M].北京:科学出版社,1981
[2] S,Kamisada M;Kosugi S.Characteristics of theInternally Circulating Fluidized Bed Boiler[A].,1991:56-65.
[3] T Higo T;Kosugi S et al.Formation of InternallyCirculating Flow and Control of Overall Heat-Transfer Coefficient in aFluidized-Bed Boiler[J].Heat Transfer-Japanese Research,1994,23(04):349-363.
[4] 张乃斌.垃圾焚化厂系统工程规划与设计[M].台湾:新雅出版社,1997
[5] 吴东垠;赵军旗 .垃圾焚烧锅炉实例[J].锅炉技术,1998,29(02):27-32.
[6] Wendong;Hao Jinhua;Wei Xiaolin et al.A Study on HeatTransfer for Immersed Tube in Internally Circulating Fluidized Bed[J].Journal of Thermal Science,1999,8(03):190-195.
[7] 田文栋,魏小林,盛宏至.内旋流流化床燃烧系统设计研究[J].热能动力工程,1999(05):363-366.
[8] 田文栋 .内旋流型流化床特种燃料锅炉实验研究[D].中国科学院力学研究所,1997.
上一张 下一张
上一张 下一张
计量
  • 下载量()
  • 访问量()
文章评分
  • 您的评分:
  • 1
    0%
  • 2
    0%
  • 3
    0%
  • 4
    0%
  • 5
    0%