化学工程
化學工程
화학공정
CHEMICAL ENGINEERING
2010年
3期
18-21
,共4页
谭宏博%厉彦忠%脱瀚斐%周满%田宝聪
譚宏博%厲彥忠%脫瀚斐%週滿%田寶聰
담굉박%려언충%탈한비%주만%전보총
冻结特性%变壁温%内翅片管
凍結特性%變壁溫%內翅片管
동결특성%변벽온%내시편관
solidification characteristics%varied wall temperature%internally finned tube
通过测量管内低温气体、管壁温度分布及冰层图相,分析了波纹内翅片管管内传热热阻、管壁温度和冰层增长的变化特性.结果表明:内翅片管管内传热阻仅为光管的6.65%,由管壁至管内低温气体的热流量大大增加,因此,管外冰层增长速度在距入口250 mm和500 mm处分别约为光管的4.2倍和1.7倍.冰层热阻占整个耦合传热总热阻的比例更大,以至于管外冰层热阻的增加引起管壁和管内气体温度的降低.由于内翅片管管内低温气体沿轴向温升更大,使其冰层厚度沿轴向斜率远大于光管.
通過測量管內低溫氣體、管壁溫度分佈及冰層圖相,分析瞭波紋內翅片管管內傳熱熱阻、管壁溫度和冰層增長的變化特性.結果錶明:內翅片管管內傳熱阻僅為光管的6.65%,由管壁至管內低溫氣體的熱流量大大增加,因此,管外冰層增長速度在距入口250 mm和500 mm處分彆約為光管的4.2倍和1.7倍.冰層熱阻佔整箇耦閤傳熱總熱阻的比例更大,以至于管外冰層熱阻的增加引起管壁和管內氣體溫度的降低.由于內翅片管管內低溫氣體沿軸嚮溫升更大,使其冰層厚度沿軸嚮斜率遠大于光管.
통과측량관내저온기체、관벽온도분포급빙층도상,분석료파문내시편관관내전열열조、관벽온도화빙층증장적변화특성.결과표명:내시편관관내전열조부위광관적6.65%,유관벽지관내저온기체적열류량대대증가,인차,관외빙층증장속도재거입구250 mm화500 mm처분별약위광관적4.2배화1.7배.빙층열조점정개우합전열총열조적비례경대,이지우관외빙층열조적증가인기관벽화관내기체온도적강저.유우내시편관관내저온기체연축향온승경대,사기빙층후도연축향사솔원대우광관.
Time-wise variation of thermal resistance, wall temperature and ice-layer increasing of wave-like internal finned tube were analyzed through measuring internal cryogenic gas temperature, tube wall temperature, and ice profiles outside tube. The comparison with smooth tube shows that the internal convective thermal resistance of finned tube is only 6.65% of that of smooth tube and the heat transfer flux from tube wall to internal cryogenic gas is augmented greatly due to heat transfer enhancement by internal fins. Thus, ice layer outside tube grows about 4.2 and 1.7 times as much as outside smooth tube at axial position of 250 mm and 500 mm. The corresponding icelayer thermal resistance accounts for such a high proportion in that of overall conjugate heat transfer that the temperature of tube wall and internal cryogenic gas decreases due to the increase of ice layer. The axial rise of internal cryogenic gas temperature is enormous for internally finned tube so the slope of ice thickness in the axial direction is much higher than that of smooth tube.