化学工程
化學工程
화학공정
CHEMICAL ENGINEERING
2010年
1期
26-29
,共4页
杨蕾%朱冬生%曾力丁%张迎恺%高莉萍
楊蕾%硃鼕生%曾力丁%張迎愷%高莉萍
양뢰%주동생%증력정%장영개%고리평
扭曲管%椭圆管%数值模拟%强化传热
扭麯管%橢圓管%數值模擬%彊化傳熱
뉴곡관%타원관%수치모의%강화전열
twisted tube%elliptic tube%numerical simulation%heat transfer enhancement
为了研究扭曲管强化传热性能,通过建立模型数值模拟和实验研究相结合的方法对扭曲管及具有相同截面形状的普通椭圆管的传热性能进行了对比分析.研究了扭曲管和椭圆管管内流体努塞尔数Nu,压力降Δp和管内综合性能评价因子η随雷诺数Re的变化情况,在Re为800-2000时,扭曲管管内Nu是普通椭圆管的2-3倍,综合传热性能是椭圆管的1.5-2倍.得出了扭曲管可以很好地加剧管内流体湍流、强化管内传热,特别适用于管内流体在低雷诺数范围内的传热,是一种十分高效的强化传热管.
為瞭研究扭麯管彊化傳熱性能,通過建立模型數值模擬和實驗研究相結閤的方法對扭麯管及具有相同截麵形狀的普通橢圓管的傳熱性能進行瞭對比分析.研究瞭扭麯管和橢圓管管內流體努塞爾數Nu,壓力降Δp和管內綜閤性能評價因子η隨雷諾數Re的變化情況,在Re為800-2000時,扭麯管管內Nu是普通橢圓管的2-3倍,綜閤傳熱性能是橢圓管的1.5-2倍.得齣瞭扭麯管可以很好地加劇管內流體湍流、彊化管內傳熱,特彆適用于管內流體在低雷諾數範圍內的傳熱,是一種十分高效的彊化傳熱管.
위료연구뉴곡관강화전열성능,통과건립모형수치모의화실험연구상결합적방법대뉴곡관급구유상동절면형상적보통타원관적전열성능진행료대비분석.연구료뉴곡관화타원관관내류체노새이수Nu,압력강Δp화관내종합성능평개인자η수뢰낙수Re적변화정황,재Re위800-2000시,뉴곡관관내Nu시보통타원관적2-3배,종합전열성능시타원관적1.5-2배.득출료뉴곡관가이흔호지가극관내류체단류、강화관내전열,특별괄용우관내류체재저뢰낙수범위내적전열,시일충십분고효적강화전열관.
The heat transfer performance of twisted tube was researched by numerical simulation and experimental research, and compared with that of normal elliptic tube with the same size. The change trend of Nusselt number (Nu), pressure drop Δp, the comprehensive function evaluation factor(η), and Reynolds number (Re) of inner-tube liquid was researched in twisted tube and elliptic tube. When the Re is between 800 and 2 000, the inner-tube liquid Nu of twisted tube is 2-3 times more than that of elliptic tube, and the heat transfer performance of twisted tube can be enhanced by 1.5-2 times that of elliptic tube. The results show that the twisted tube can greatly enhance the onflow and the heat transfer of tube-side liquid, which performs especially well when the Re of tube-side is small. The twisted tube is a high efficiency heat transfer tube.