R410A空调器空泡系数模型适用性的实验验证

为了找到适用于R410A空调器两相制冷剂质量计算的空泡系数公式,提出了一种可以方便地测量换热器中制冷剂质量的准在线液氮称重法(QOMM),检验了该方法的测量精度,并建立实验台测量了不同空调工况下空调器换热器中的制冷剂量.基于所测制冷剂质量,验证了11种两相流体空泡系数模型对于R410A空调器的适用性.结果表明,QOMM具有较高的测量精度,R410A空调器制冷工况下空泡系数公式宜采用Hughmark模型,而热泵工况下宜采用Premoli模型.     

微生物污垢对翅片管换热器空气侧换热和压降特性的影响

为了研究翅片管换热器表面微生物污垢对其换热和压降特性的影响,对4种不同污垢程度的翅片管换热器进行了实验.比较分析了不同ReDc下,不同微生物污垢面积的换热器和清洁换热器的换热和压降特性.结果表明:在RReDc较小时,微生物污垢对换热器空气侧换热有一定的增强作用,随着RReDc.的增大,增强作用逐渐减弱;当RReDc1200后,污垢对换热只起到衰减的作用.微生物污垢对压降的影响明显大于对换热的影响.随着RReDc.的增大,污垢压降因子逐渐减小,并且污垢面积越大,减小的趋势越显著.     

析湿工况下亲水层对开缝翅片管换热器空气侧换热压降特性影响分析

对附带亲水层和没有附带亲水层的开缝翅片管换热器在析湿工况下的空气侧特性进行了实验研究,分析了亲水层对空气侧换热和压降特性的影响.实验结果表明:析湿工况下亲水层使翅片管换热器空气侧的换热特性减弱,风速和翅片间距越小时,减弱程度越强;对于相同结构参数没有亲水处理过的翅片,亲水处理过翅片的空气侧换热系数降低的最大值可达到25.4%;亲水层对降低空气侧的压降则有显著作用,降低的最大值可达到51%;附带亲水层与未附带亲水层开缝翅片管换热器析湿工况下,空气侧换热系数比和压降比关联式的平均误差分别为5.6%和8.4%,在±15%误差范围内分别能涵盖93.4%和84.2%实验数据.     

积液型两相流分配器的性能与优化

摘要： 试验研究了带有复杂入口管的积液型两相流分液器在不同干度和质量流量条件下的分液均匀性.结果表明：当干度增大时,分液器的分液均匀性下降;当质量流量增大时,分液器的分液均匀性得到改善;各工况下分液器分液的流体质量流量标准偏差（STD）的平均值为2.80%.同时,对复杂入口管进行了计算流体动力学模拟,提出了一种能够有效降低入口管形式影响的新型双筒体型分液器,并通过试验加以验证.验证试验结果表明,在各工况下,双筒体型分液器分液的STD的平均值为2.36%,比积液型分液器的分液均匀性提高了15.7%.     

Heat Transfer and Friction Characteristics of Wavy Fin with Hydrophilic Coating under Dehumidifying Conditions

An experimental study on the airside heat transfer and friction characteristics of seven hydrophilic-coated wavy finned tube heat exchangers is performed under dehumidifying conditions. The effects of fin pitch, number of tube rows and inlet air relative humidity on the airside characteristics are investigated. The airside heat transfer and friction characteristics are presented in the form of Colburn factor and friction factor, respectively. The test results indicate that the Colburn factor and friction factor increase with decreasing fin pitch. The Colburn factor of 2tube row heat exchanger is higher than that of 3 row heat exchanger, while their friction factors are nearly equal. As the inlet relative humidity increases, the Colburn factor increases and the friction factor is almost unchanged. The airside heat transfer and friction correlations are proposed for the hydrophilic-coated wavy fin with mean deviations of 6.5% and 9.1%, respectively. They can be used to design or evaluate hydrophilic-coated wavy fin-and-tube heat exchangers.