化工进展
化工進展
화공진전
CHEMICAL INDUSTRY AND ENGINEERING PROGRESS
2013年
12期
2837-2841
,共5页
三分螺旋折流板换热器%流场%二次流%湍流动能%换热系数
三分螺鏇摺流闆換熱器%流場%二次流%湍流動能%換熱繫數
삼분라선절류판환열기%류장%이차류%단류동능%환열계수
trisection helical baffled heat exchangers%flow field%secondary flow%turbulent kinetic energy%heat transfer coefficient
通过对倾斜角35°首尾相连的三分螺旋折流板换热器的数值模拟,展示了其壳侧通道内流体在典型切面上的流场和流线分布,以及典型切面上典型直线的流动和换热参数分布,并与性能测试结果进行了对比。结果表明,数值模拟结果与实验结果是吻合的。螺旋折流板形成的近似螺旋通道,使换热器壳侧流体受离心力和向心力共同作用形成了迪恩涡二次流,且在每个螺旋周期内都存在;二次流增强了主流区域流体与靠近壁面流体的掺混,使得壳侧典型切面上中心线和折流板外缘直线的轴向速度较大;除主流中心区域外,壳侧流体在二次流的作用下具有均匀的湍流动能;二次流所在区域内,壳侧同心柱面内典型直线上换热系数相差不大,但由于二次流能使其附近区域传热面上的流体得到不断卷吸掺混,由此强化传热。
通過對傾斜角35°首尾相連的三分螺鏇摺流闆換熱器的數值模擬,展示瞭其殼側通道內流體在典型切麵上的流場和流線分佈,以及典型切麵上典型直線的流動和換熱參數分佈,併與性能測試結果進行瞭對比。結果錶明,數值模擬結果與實驗結果是吻閤的。螺鏇摺流闆形成的近似螺鏇通道,使換熱器殼側流體受離心力和嚮心力共同作用形成瞭迪恩渦二次流,且在每箇螺鏇週期內都存在;二次流增彊瞭主流區域流體與靠近壁麵流體的摻混,使得殼側典型切麵上中心線和摺流闆外緣直線的軸嚮速度較大;除主流中心區域外,殼側流體在二次流的作用下具有均勻的湍流動能;二次流所在區域內,殼側同心柱麵內典型直線上換熱繫數相差不大,但由于二次流能使其附近區域傳熱麵上的流體得到不斷捲吸摻混,由此彊化傳熱。
통과대경사각35°수미상련적삼분라선절류판환열기적수치모의,전시료기각측통도내류체재전형절면상적류장화류선분포,이급전형절면상전형직선적류동화환열삼수분포,병여성능측시결과진행료대비。결과표명,수치모의결과여실험결과시문합적。라선절류판형성적근사라선통도,사환열기각측류체수리심력화향심력공동작용형성료적은와이차류,차재매개라선주기내도존재;이차류증강료주류구역류체여고근벽면류체적참혼,사득각측전형절면상중심선화절류판외연직선적축향속도교대;제주류중심구역외,각측류체재이차류적작용하구유균균적단류동능;이차류소재구역내,각측동심주면내전형직선상환열계수상차불대,단유우이차류능사기부근구역전열면상적류체득도불단권흡참혼,유차강화전열。
Using the numerical simulation of end to end tube-and-shell heat exchangers with trisection helical baffles with 35°inclined angle, this research demonstrated the distribution of the flow field and streamline on the typical sections of fluid in the shell side channel, as well as the distribution of flow and heat transfer parameters of typical straight lines on the typical sections. The results showed that the approximate spiral channel composed by helical baffles impelled the Dean vortex secondary flow formed by the combined effect of centrifugal and centripetal force, and the Dean vortex secondary flow existed in each spiral cycle. the secondary flow enhanced the mixing of fluid in mainstream region and fluid near the wall, resulting a larger axial velocity of the centerline and the outer edge straight line on the typical sections. Other than the mainstream center region, the shell side fluid had uniform turbulent kinetic energy in the role of secondary flow. The heat transfer coefficient on the concentric cylindrical surface differed little in the secondary flow region,however, heat transfer can be enhanced due to the fact that the secondary flow was continuously entraining the fluid of the adjacent areas.