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风洞板翅式热交换器气体流动特性试验

赵波 陈振华 李为民 陈吉明 朱博 温乾

赵波,陈振华,李为民,等. 风洞板翅式热交换器气体流动特性试验[J]. 实验流体力学,2022,36(1):69-76 doi: 10.11729/syltlx20210081
引用本文: 赵波,陈振华,李为民,等. 风洞板翅式热交换器气体流动特性试验[J]. 实验流体力学,2022,36(1):69-76 doi: 10.11729/syltlx20210081
ZHAO B,CHEN Z H,LI W M,et al. Flow characteristics experiment of plate-fin heat exchanger in wind tunnel[J]. Journal of Experiments in Fluid Mechanics, 2022,36(1):69-76. doi: 10.11729/syltlx20210081
Citation: ZHAO B,CHEN Z H,LI W M,et al. Flow characteristics experiment of plate-fin heat exchanger in wind tunnel[J]. Journal of Experiments in Fluid Mechanics, 2022,36(1):69-76. doi: 10.11729/syltlx20210081

风洞板翅式热交换器气体流动特性试验

doi: 10.11729/syltlx20210081
详细信息
    作者简介:

    赵波:(1983—),男,四川绵阳人,硕士研究生,副研究员。研究方向:风洞气动设计及设备传热分析。通信地址:四川省绵阳市涪城区二环路南段6号(621000)。E-mail:zbugo@163.com

    通讯作者:

    E-mail:chenjimy@sina.com

  • 中图分类号: TK172

Flow characteristics experiment of plate-fin heat exchanger in wind tunnel

  • 摘要: 针对风洞板翅式热交换器,开展了其在风洞运行工况下气体流动特性的研究。对比了板翅式热交换器和椭圆翅片管热交换器的扰流和压损特性,利用试验研究了不同来流风速、不同上游扰流片角度等条件下热交换器下游湍流发展变化规律,开展了封条、模块拼接缝等特征结构对气流扰动的影响研究。研究结果表明:该型板翅式热交换器相比椭圆翅片管热交换器,其对气流扰动更小,相同换热工况下压力损失也大幅减小;板翅式热交换器具有较好的整流作用,其后的气流扰动主要由自身结构决定,与来流条件关系不大,其中厚度较大的结构对气流的扰动会传播更远,需要设计合理的整流方案以减小扰动。
  • 图  1  试验件及测试截面布置

    Figure  1.  Test specimen and test cross sections arrangement

    图  2  截面测点布置

    Figure  2.  Cross section measuring point arrangement

    图  3  扰流片阵列三视图

    Figure  3.  Three-view drawing of spoiler array

    图  4  二维热线风速仪探头

    Figure  4.  Two-dimensional hot wire anemometer probe

    图  5  板翅式热交换器试验件基本结构

    Figure  5.  Basic structure of plate-fin heat exchanger test specimen

    图  6  试验件关键结构示意图

    Figure  6.  Schematic diagram of the key structures of the test specimens

    图  7  4排椭圆翅片管结构参数

    Figure  7.  Structure parameters of 4-row finned oval tubes

    图  8  不同结构型式热交换器下游流向湍流强度分布

    Figure  8.  Distribution of flow direction turbulence at downstream cross sections of different type heat exchangers

    图  9  不同结构型式热交换器下游流向速度分布

    Figure  9.  Distribution of flow direction velocity at downstream cross sec- tions of different type heat exchangers

    图  10  不同结构型式热交换器下游横向湍流强度分布

    Figure  10.  Distribution of lateral turbulence at downstream cross sec-tions of different type heat exchangers

    图  11  不同结构型式热交换器下游横向速度分布

    Figure  11.  Distribution of lateral velocity at downstream cross sections of different type heat exchangers

    图  12  5个截面的湍流强度平均值

    Figure  12.  Average values of turbulence at the five downstream cross sections of different type heat exchangers

    图  13  不同风速下热交换器下游流向湍流强度分布

    Figure  13.  Distribution of flow direction turbulence at downstream cross sections of heat exchanger under different velocity conditions

    图  14  不同风速下热交换器下游截面横向湍流强度分布

    Figure  14.  Distribution of lateral direction turbulence at downstream cross sections of heat exchanger under different velocity conditions

    图  15  不同扰流片角度热交换器入口流向湍流强度分布

    Figure  15.  Distribution of flow direction turbulence at inlet cross section of heat exchanger under different spoiler angle conditions

    图  16  不同扰流片角度热交换器入口流向速度分布

    Figure  16.  Distribution of flow direction velocity at inlet cross section of heat exchanger under different spoiler angle conditions

    图  17  不同扰流片角度热交换器下游流向湍流强度分布

    Figure  17.  Distribution of flow direction turbulence at downstream cross sections of heat exchanger under different spoiler angle conditions

    图  18  不同扰流片角度热交换器下游流向速度分布

    Figure  18.  Distribution of flow direction velocity at downstream cross sections of heat exchanger under different spoiler angle conditions

    图  19  封条整流对下游流向湍流强度的影响

    Figure  19.  Effect of seal on downstream flow direction turbulence

    图  20  拼接缝结构对下游流向湍流强度的影响

    Figure  20.  Effect of joint on downstream flow direction turbulence

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  • 收稿日期:  2021-08-02
  • 修回日期:  2021-11-18
  • 录用日期:  2021-11-18
  • 刊出日期:  2022-03-17

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