节点文献

薄膜蒸发器内流体流动特性的数值模拟

Numerical Simulation on Fluid Flow in a Thin Film Evaporator

  • 推荐 CAJ下载
  • PDF下载
  • 不支持迅雷等下载工具,请取消加速工具后下载。

【作者】 贺小华唐平李佳陆小华

【Author】 HE Xiao-hua1, TANG Ping1, LI Jia1, LU Xiao-hua2 (1. College of Mechanical and Power Engineering, Nanjing University of Technology, Nanjing, Jiangsu 210009, China; 2. College of Chemical Engineering, Nanjing University of Technology, Nanjing, Jiangsu 210009, China)

【机构】 南京工业大学机械与动力工程学院南京工业大学化学工程学院 江苏南京210009江苏南京210009江苏南京210009

【摘要】 建立了薄膜蒸发器的计算模型,采用大型计算流体力学(CFD)分析软件CFX4.4模拟了薄膜蒸发器内水及粘性料液的流动过程,得到了各种速度分布.结果表明,刮板转速、进料量对流体流动状态影响显著.提高刮板转速,可明显促进液膜和圈形波内流体的物质交换.在任一转速下,各料液均存在同一最佳进料量,此时其圈形波截面内平均速度达到最大值.对纯物质水,最佳进料量对应的流动边界层厚度与膜厚之比最小.粘性料液和水的轴向速度分布存在差异,且在液膜厚度内未形成明显的流动边界层.

【Abstract】 The calculation model of thin film evaporator (TFE) was developed, the flow of water and viscous fluid was simulated using CFX 4.4 software and the velocity distribution was obtained. The results show that the rotor speed and feeding rate have great effects on the fluid flow of TFE. The material exchange between the fillet and film can be promoted by increasing the rotor speed. There is one common optimum feeding rate under different rotor speeds for different fluids. At this feeding rate, the mean velocity in the fillet section reaches the maximum value. For water, the ratio of flow boundary layer thickness to film thickness is the minimum under the optimum feeding rate. Difference exists for the axial velocity distribution between viscous fluid and water, and no obvious flow boundary layer forms for viscous fluid.

  • 【文献出处】 过程工程学报 ,The Chinese Journal of Process Engineering , 编辑部邮箱 ,2005年04期
  • 【分类号】TQ051.62
  • 【被引频次】26
  • 【下载频次】439
节点文献中: 

本文链接的文献网络图示:

本文的引文网络