化工学报
化工學報
화공학보
JOURNAL OF CHEMICAL INDUSY AND ENGINEERING (CHINA)
2010年
3期
587-593
,共7页
扰流柱%螺旋翅片%强化换热%套管式换热器%场协同理论
擾流柱%螺鏇翅片%彊化換熱%套管式換熱器%場協同理論
우류주%라선시편%강화환열%투관식환열기%장협동이론
pin fin%helical fin%heat transfer enhancement%double-pipe heat exchanger%field coordination theory
对于内管外壁安装有螺旋片的套管换热器的壳侧,在螺旋片所形成的螺旋通道中心,沿螺旋方向周期性地布置扰流柱以进一步提高其换热性能,对这种扰流柱协同螺旋片强化的换热器的换热特性进行了实验研究,应用场协同理论分析了其强化机理.结果表明,在Re=4000~14000范围内,扰流柱协同螺旋片强化的换热器的传热系数为相同螺距下只安装螺旋片的换热器的1.53~2.53倍,为光滑内管换热器的3.08~4.87倍.在相同质量流量、相同压降及相同泵功条件下,扰流柱协同螺旋片强化的换热器的综合换热性能明显好于相同螺距下只安装螺旋片的换热器及光滑内管换热器;在相同压降及相同泵功条件下,保持螺距不变,安装扰流柱比螺距减小一半的综合换热性能更好;单位螺距内安装奇数个扰流柱比安装偶数个扰流柱略好.扰流柱的安装增大了径向速度,使温度场与速度场的协同效果更好,从而提高了换热效果.
對于內管外壁安裝有螺鏇片的套管換熱器的殼側,在螺鏇片所形成的螺鏇通道中心,沿螺鏇方嚮週期性地佈置擾流柱以進一步提高其換熱性能,對這種擾流柱協同螺鏇片彊化的換熱器的換熱特性進行瞭實驗研究,應用場協同理論分析瞭其彊化機理.結果錶明,在Re=4000~14000範圍內,擾流柱協同螺鏇片彊化的換熱器的傳熱繫數為相同螺距下隻安裝螺鏇片的換熱器的1.53~2.53倍,為光滑內管換熱器的3.08~4.87倍.在相同質量流量、相同壓降及相同泵功條件下,擾流柱協同螺鏇片彊化的換熱器的綜閤換熱性能明顯好于相同螺距下隻安裝螺鏇片的換熱器及光滑內管換熱器;在相同壓降及相同泵功條件下,保持螺距不變,安裝擾流柱比螺距減小一半的綜閤換熱性能更好;單位螺距內安裝奇數箇擾流柱比安裝偶數箇擾流柱略好.擾流柱的安裝增大瞭徑嚮速度,使溫度場與速度場的協同效果更好,從而提高瞭換熱效果.
대우내관외벽안장유라선편적투관환열기적각측,재라선편소형성적라선통도중심,연라선방향주기성지포치우류주이진일보제고기환열성능,대저충우류주협동라선편강화적환열기적환열특성진행료실험연구,응용장협동이론분석료기강화궤리.결과표명,재Re=4000~14000범위내,우류주협동라선편강화적환열기적전열계수위상동라거하지안장라선편적환열기적1.53~2.53배,위광활내관환열기적3.08~4.87배.재상동질량류량、상동압강급상동빙공조건하,우류주협동라선편강화적환열기적종합환열성능명현호우상동라거하지안장라선편적환열기급광활내관환열기;재상동압강급상동빙공조건하,보지라거불변,안장우류주비라거감소일반적종합환열성능경호;단위라거내안장기수개우류주비안장우수개우류주략호.우류주적안장증대료경향속도,사온도장여속도장적협동효과경호,종이제고료환열효과.
To enhance the heat transfer on shell side of a double-pipe heat exchanger with helical fins on the outer wall of the inner tube, some pin fins were installed along the centerline of the helical channel formed by helical fins.The heat transfer enhanced by these fins was investigated experimentally and the enhancement mechanism was analyzed by applying the field coordination theory.The heat transfer coefficient in the exchanger with helical fins and pin fins was 1.53-2.53 times as much as that with helical fins only at the same pitch and was 3.08-4.87 times that without the fins for Reynolds number ranging from 4000 to 14000.The performance of the exchanger with pin fins and helical fins was much better at the same mass flow rate, pressure drop and pumping power.Reducing the pitch of pin fins by half, the heat transfer was much better.At the same pressure drop and pumping power, the heat transfer in the exchanger with odd-numbered pin fins within one pitch was a little better than that with even-numbered pin fins.The pin fins increased the radical velocity.Accordingly, the resultant effect of temperature field and velocity field improved the heat transfer.