华南理工大学学报(自然科学版) ›› 2021, Vol. 49 ›› Issue (10): 114-122.doi: 10.12141/j.issn.1000-565X.200709

所属专题: 2021年能源、动力与电气工程

• 能源、动力与电气工程 • 上一篇    下一篇

分液型板式冷凝器强化冷凝换热的实验研究

姚远1,2,3 陈颖2† 陈健勇2 梁志颖2   

  1. 1. 中国科学院广州能源研究所,广东 广州 510640; 2. 广东工业大学 材料与能源学院,广东 广州 510006; 3. 中国科学院可再生能源重点实验室,广东 广州 510640
  • 收稿日期:2020-11-17 修回日期:2020-12-28 出版日期:2021-10-25 发布日期:2021-09-30
  • 通信作者: 陈颖 ( 1969-) ,女,教授,博士生导师,主要从事空调及热能动力研究。 E-mail:chenying@gdut.edu.cn
  • 作者简介:姚远 ( 1976-) ,男,在职博士生,高级工程师,主要从事热泵及换热器强化换热研究。E-mail:yaoyauan@ms.giec.ac.cn
  • 基金资助:
    中国科学院科技服务网络计划区域重点项目 ( KFJ-STS-QYZX-114 ) ; 山东省重大科技创新工程项目 ( 2019JZZY010910)

Experimental Study on Enhanced Heat Transfer Characteristics of Plate Condenser with Liquid-Vapor Separation

YAO Yuan1,2,3 CHEN Ying2 CHEN Jianyong2 LIANG Zhiying2   

  1. 1. Guangzhou Institute of Energy Conversion,Chinese Academy of Science,Guangzhou 510640,Guangdong,China; 2. School of Materials and Energy,Guangdong University of Technology,Guangzhou 510006,Guangdong,China; 3. Key Laboratory of Renewable Energy,Chinese Academy of Sciences,Guangzhou 510640,Guangdong,China
  • Received:2020-11-17 Revised:2020-12-28 Online:2021-10-25 Published:2021-09-30
  • Contact: 陈颖 ( 1969-) ,女,教授,博士生导师,主要从事空调及热能动力研究。 E-mail:chenying@gdut.edu.cn
  • About author:姚远 ( 1976-) ,男,在职博士生,高级工程师,主要从事热泵及换热器强化换热研究。E-mail:yaoyauan@ms.giec.ac.cn
  • Supported by:
    Supported by the Regional Key Projects of Science and Technology Service of Chinese Academy of Sciences ( KFJ-STS-QYZX-114) and the Key Projects of Scientific and Technological Innovation in Shandong Province ( 2019JZZY010910)

摘要: 创新设计了可以实现中间排液功能的分液型板式冷凝器。该冷凝器中间位置设 置分液口,可以加快排液速度,减小附着在板片上的冷凝液膜的厚度,降低蒸气与板片 之间液膜的导热热阻,从而增大板式冷凝器的相变传热系数。将分液型板式冷凝器与常 规板式冷凝器进行了性能对比实验。通过 10 个不同测试工况的实验结果发现,在同等 初始条件下,与常规板式冷凝器相比,分液型板式冷凝器工质侧冷凝换热系数提高了 8. 3% ~ 51. 6% ,总换热系数提高了 7. 6% ~ 38. 3% ,总压降减小了 2. 6% ~ 11. 4% 。该 实验结果验证了分液型板式冷凝器可以实现强化换热和减小压降的目的,但也由于分液 造成第二冷凝区工质流量的减少,而使分液型板式冷凝器总换热量与常规板式冷凝器总 换热量大致相等,并无明显增加。

关键词: 板式冷凝器, 气液分离, 强化传热, 压降, 换热系数

Abstract: A new type of plate condenser which can discharge condensate in the middle was designed. The drain port was set in the middle of the condenser,which can speed up the drainage,reduce the thickness of the condensate film attached to the plate,reduce the thermal resistance of the liquid film between the vapor and the plate,and increase the phase change heat transfer coefficient of the plate condenser. The performance of the liquid-vapor separation plate condenser ( LVSPC) was compared with that of the conventional plate condenser ( CPC) . The experimental results of 10 different test conditions show that,under the same initial conditions,compared with the CPC, the condensation heat transfer coefficient of the LVSPC is increased by 8. 3% ~51. 6%,the total heat transfer coefficient is increased by 7. 6% ~ 38. 3% ,and the total pressure drop is reduced by 2. 6% ~ 11. 4% . The experimental results proved that the LVSPC can achieve the purpose of enhancing heat transfer and reducing pressure drop. However,due to the decrease of working fluid flow in the second condensing area,the total heat transfer of the LVSPC is approximately equal to that of CPC,and there is no obvious increase.

Key words: plate condenser, liquid-vapor separation, enhanced heat transfer, pressure drop, heat transfer coefficient

中图分类号: