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机构地区:[1]华南理工大学机械与汽车工程学院,广州510640 [2]广州市华德工业有限公司,广州510663
出 处:《制冷学报》2014年第3期90-95,共6页Journal of Refrigeration
基 金:广东省部产学研结合项目(2012B091100330)资助~~
摘 要:本文利用CFD软件对蒸发冷凝器中波纹填料间的气流速度、压力、温度以及含湿量进行了模拟计算,分析了不同填料间距、进口气流速度、喷淋水流量对空气含湿量、进出口压差、填料表面传热系数变化的影响,并将模拟结果与实验数据进行对比,两者误差在5%以内。结果表明:随着填料间距增大,填料出口处空气含湿量先增加后减少,进出口压差从900 Pa降为50Pa;当进入填料的气流速度变大时,表面传热系数随之变大,出口空气含湿量从24 g/kg减少到23 g/kg;喷淋水流量增加,出口空气含湿量从23.1 g/kg升至24 g/kg,表面传热系数则从15.2 W/(m2·K)减为14.6 W/(m2·K)。填料间距选择为6 mm,气流速度设置为2 m/s以及喷淋水流量为0.025 kg/s时,空气和冷却水间的热质传递效果最好且机组能耗低。The CFD software was applied to conduct the numerical simulation for predicting the air velocity, pressure, and temperature, humidity ratio in the corrugated filler which was used in evaporative condenser. And then studies on influencing factors of humidity ratio, pressure difference and surface heat transfer coefficient, i. e. , filler space, air velocity and mass flux of cooling water were conducted. Simulation results were verified through experiments, and the error was less than 5%. The results showed that with the increasing filler space, humidity ratio of outlet air decreased after the first increase, and pressure difference decreased from 900 Pa to 50 Pa. Surface heat transfer coefficient increased with increasing air velocity, and humidity ratio of outlet air decreased from 24 g/kg to 23 g/kg. With the in- crease of mass flux of cooling water, humidity ratio of outlet air changed from 23.1 g/kg to 24 g/kg and surface heat transfer coefficient decreased 15.2 W/(m2 · K)to 14.6 W/( m2 · K). It contributed to heat and mass transfer and lower energy consumption when filler space was 6 mm, air velocity was 2 m/s and mass flux of cooling water was 0. 025 kg/s.
分 类 号:TK172[动力工程及工程热物理—热能工程]
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