建筑热能通风空调
建築熱能通風空調
건축열능통풍공조
BUILDING ENERGY & ENVIRONMENT
2015年
3期
52-55
,共4页
宋祥龙%黄翔%李鑫%张璐瑶%邱佳
宋祥龍%黃翔%李鑫%張璐瑤%邱佳
송상룡%황상%리흠%장로요%구가
立管式间接蒸发冷却器%卧式管式间接蒸发冷却器%换热效率%二次/一次风量比%淋水密度%阻力
立管式間接蒸髮冷卻器%臥式管式間接蒸髮冷卻器%換熱效率%二次/一次風量比%淋水密度%阻力
립관식간접증발냉각기%와식관식간접증발냉각기%환열효솔%이차/일차풍량비%림수밀도%조력
vertical tube-type indirect evaporative cooler%heat exchange efficiency%working/product air flow ratio%optimalspraying consistency
利用现有的卧式管式间接蒸发冷却器搭建了模拟立管式间接蒸发冷却器实验台,并进行相关测试,在标准实验工况下,该模拟立管式间接蒸发冷却器最大温降9.2℃,最高换热效率62.4%,最佳一次空气流量为2000~2500m 3/h,最佳二次/一次风量比为0.7,最佳淋水密度1197kg/(m·h)。与卧式管式间接蒸发冷却器性能进行对比,该模拟立管式间接蒸发冷却器换热效率略低,二次空气侧阻力较大。总结出实际的立管式间接蒸发冷却器应设计为大管径、圆形换热管,布水方式采用管内直接布水。
利用現有的臥式管式間接蒸髮冷卻器搭建瞭模擬立管式間接蒸髮冷卻器實驗檯,併進行相關測試,在標準實驗工況下,該模擬立管式間接蒸髮冷卻器最大溫降9.2℃,最高換熱效率62.4%,最佳一次空氣流量為2000~2500m 3/h,最佳二次/一次風量比為0.7,最佳淋水密度1197kg/(m·h)。與臥式管式間接蒸髮冷卻器性能進行對比,該模擬立管式間接蒸髮冷卻器換熱效率略低,二次空氣側阻力較大。總結齣實際的立管式間接蒸髮冷卻器應設計為大管徑、圓形換熱管,佈水方式採用管內直接佈水。
이용현유적와식관식간접증발냉각기탑건료모의립관식간접증발냉각기실험태,병진행상관측시,재표준실험공황하,해모의립관식간접증발냉각기최대온강9.2℃,최고환열효솔62.4%,최가일차공기류량위2000~2500m 3/h,최가이차/일차풍량비위0.7,최가림수밀도1197kg/(m·h)。여와식관식간접증발냉각기성능진행대비,해모의립관식간접증발냉각기환열효솔략저,이차공기측조력교대。총결출실제적립관식간접증발냉각기응설계위대관경、원형환열관,포수방식채용관내직접포수。
Using the horizontal tubular indirect evaporative cooler to set up vertical tube-type indirect evaporative cooler test bench, it is concluded that the vertical tube-type cooler can reduce the temperature about 9.2℃ with 62.4%efficiency.The best product airflow is 2000~2500m3/h,andthebestworking/productairratiois0.7,andthebestwater pouring density is 1197kg/(m·h). B y comparing with horizontal tubular cooler, the vertical tubular cooler has a lower efficiency and a higher air resistance, and the real vertical tubular indirect evaporative cooler should have a rounded, heavy caliber heatexchanger tube,spray water in the tube directly.