中空纤维膜换热器传热传质特性的实验和理论研究

王赞社 1; 冯诗愚 1; 李云 1; 顾兆林 2

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中空纤维膜换热器传热传质特性的实验和理论研究

更新时间：2025-07-09

- 中空纤维膜换热器传热传质特性的实验和理论研究
- Experimental and Theoretical Study on Heat and Mass Transfer of Hollow Fiber Membrane Heat Exchanger
- 西安交通大学学报 2009年43卷第5期页码：40-45
- 作者机构：
  
  西安交通大学能源与动力工程学院,西安,710049
- 作者简介：
- 基金信息：
  
  : 2008-07-22. 作者简介: 王赞社(1971-),男,博士生;冯诗愚(联系人),男,博士,讲师. 基金项目: 陕西省科技研究发展计划资助项目(2005K05-G17)
- DOI：
  中图分类号： TB61;TQ028.8
- 网络首发：2009-05-10，
  
  纸质出版：2009
- 稿件说明：
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王赞社 1, 冯诗愚 1, 李云 1, 等. 中空纤维膜换热器传热传质特性的实验和理论研究[J]. 西安交通大学学报, 2009,43(5):40-45.

Experimental and Theoretical Study on Heat and Mass Transfer of Hollow Fiber Membrane Heat Exchanger[J]. 2009, 43(5): 40-45.
王赞社 1, 冯诗愚 1, 李云 1, 等. 中空纤维膜换热器传热传质特性的实验和理论研究[J]. 西安交通大学学报, 2009,43(5):40-45. DOI：

Experimental and Theoretical Study on Heat and Mass Transfer of Hollow Fiber Membrane Heat Exchanger[J]. 2009, 43(5): 40-45. DOI：

摘要

将直接接触式膜蒸馏的概念和操作过程引入到换热器的设计中

提出了一种既有传热又有传质的新型中空纤维膜换热器.以水为工作介质

对采用聚偏氟乙烯膜(PVDF)的中空纤维膜换热器进行了初步的传热、传质实验研究

考察了逆流布置下溶液的进口温度和流量对换热器的传热、传质效果的影响

并构建了同样尺寸的铜列管式换热器进行对比研究.实验和理论结果表明

虽然膜材料本身的热传导系数较低

但膜换热器冷热流体之间接触面积比传统换热器大

特别是水蒸气从热侧向冷侧进行质量传递的同时还进行潜热传递

因此膜换热器的换热量可维持在较高水平

流体的进出口温差也有大幅度提高.初步研究结果显示

在实验的工况范围内

在低流速、小流量下

膜换热器的传热性能优于金属换热器

但随着管内流速的增加

膜换热器的沿程阻力将远大于金属换热器

因此膜换热器适合于在低流速的情况下使用.

Abstract

An experiment on heat and mass transfer of a hollow fiber membrane heat exchanger proposed in our study was conducted with water as a working medium and Poly(vinylidene fluoride)(PDVF)as a membrane material. The influence of inlet temperature and flow rate of the solution on heat and mass transfer of the heat exchanger was explored under the counter flow condition. Moreover

a brass shell-and-tube heat exchanger with the same size as the membrane one was fabricated to compare its heat transfer

pressure drop and other character istics with those of the membrane heat exchanger. The experimental and theoretical studies indicate that although the thermal conductivity of the membrane materials is lower

the heat transfer capability of the membrane heat exchanger is higher due to its larger contact surface between the hot fluid and cold fluid

especially

the latent heat of the vapor caused by the mass transfer from the hot side to the cold side. The experimental result shows that the performance of the membrane heat exchanger is better than that of the metal one at the low flow rate under the experimental operation conditions. However

when the flow velocity in the tubes increases

the frictional resistance in the membrane heat exchanger is far larger than that in the metal heat exchanger. It seems that the present heat exchanger could be applied under low flow rate conditions.

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references

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