暖通空调>期刊目次>2017年>第7期

双回路逆流干式蒸发器设计及实验验证

Design and experimental verification for double-loop countercurrent dry-expansion evaporators

尹应德[1][2][3] 孙晋飞[1][2][3] 朱冬生[1][2][3] 刘 峰[4] 王 洪[4]
[1]中国科学院广州能源研究所 [2]中科院可再生能源重点实验室 [3]广东省新能源和可再生能源研究开发和应用重点实验室 [4]TCL空调器(中山)有限公司

摘要:

基于非对称空间传热理念,设计了一种新型双回路逆流干式蒸发器,并将其安装在空气源热泵机组上进行实验测试。理论计算和测试结果表明:制冷工况下,干式蒸发器总表面传热系数的理论计算值为1 709.4 W/(m2·K),实测值为1 938.1 W/(m2·K),后者比前者大11.8%;制热工况下,干式蒸发器总表面传热系数的理论计算值为1 834.9 W/(m2·K),实测值为2 226.4 W/(m2·K),后者比前者大17.5%。对误差原因进行了分析,结果显示:实际测试时壳程流速增大;蒸发器内换热管的污垢热阻很小。

关键词:双回路,逆流,自支撑,干式蒸发器,总表面传热系数

Abstract:

Based on the asymmetric space heat transfer concept, designs a novel double-loop counter-currrent dry-expansion evaporator equipment, and installs it to an air-source heat pump unit and performs the experiment. Theoretical calculation and test results show that the calculated value of the overall surface coefficient of heat transfer is 1 709.4 W/m2·K, and the measured value is 1 938.1 W/m2·K for dry-expansion evaporator under cooling condition, the latter is 11.8% higher than the former; and that the corresponding values under heating condition are 1 834.9 W/m2·Kand 2 226.4 W/m2·Krespectively, the latter is 17.5% higher than the former. Analyses the error cause and concludes that the flow velocity in shell-side of the measured evaporator is increased, and the fouling resistance of heat exchanger tube in the measured evaporator is nearly zero.

Keywords:double-loop, countercurrent, self-supporting, dry-expansion evaporator, overall surface coefficient of heat transfer

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