摘要
目前对篦冷机熟料多孔介质的研究多采用渗流传热理论,通过达西定律与传热方程联立求解,但模型求解过程复杂,不便于工程应用。本文将圆形截面直管换热理论引入到篦冷机熟料多孔介质单元体的研究中,建立了水泥熟料颗粒大孔隙多孔介质单元体直管等效换热模型。通过直管换热理论的方法和思想求解水泥熟料多孔介质的换热过程,以达到降低求解难度的目的。在保证计算精度的前提下,求解出熟料颗粒与流体温度随时间变化的表达式,利用自主设计实验设备进行实验,实验数据与模型计算结果基本吻合,从而验证了直管等效换热模型的可行性。
For the study on porous cement clinker, researchers solve the equations of Darcy's law and local no-thermal equilibrium heat transfer based on the theory of heat transfer of fluid flow in porous media. However, the solving process is complex and not convenient for engineering application. A kind of straight pipe equivalent heat transfer model was established by introducing the theory of straight pipe heat exchange to unit body of porous cement clinker. In order to decrease the difficulty of the solving process, the methods and ideas based on the theory of straight pipe heat transfer were used to solve the heat transfer process of porous cement clinker. On the premise of ensuring calculation precision, the changes of temperatures of both clinker and gas with time were obtained. A self-designed experimental equipment was porosities. The calculation results basically agreed with straight pipe equivalent heat transfer model. used to verify the temperature expressions at different the experimental data, which verified the feasibility of
出处
《化工学报》
EI
CAS
CSCD
北大核心
2014年第9期3434-3440,共7页
CIESC Journal
基金
国家自然科学基金项目(51076135)
河北省自然科学基金项目(E2014203160)~~
关键词
篦冷机
多孔介质
孔隙率
颗粒物料
传热
grate cooler
clinker media
porosity
granular material
heat transfer