共查询到17条相似文献,搜索用时 171 毫秒
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通过数值模拟,研究了85%甘油在旋流片支撑光滑管管束间纵向流动的传热与流阻特性,并与无支撑光滑管束的纵向流动进行了对比,揭示了高粘度流体置换类强化传热方法的有效传热温差缓变特性机理。研究结果表明,层流时,小扭率与大角度旋流片支撑的光滑管管束的传热综合性能更佳,旋流片支撑光滑管管束在有旋流片段可以通过提高有效传热系数与增加有效传热温差的双重途径提高传热速率,而在旋流片下游段则可以利用有效传热温差的缓变特性继续维持较大的传热速率,从而能避免过多的流体置换次数,极大幅度的降低了流体的输送功耗。 相似文献
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提出了由旋流片支撑缩放管管束的管壳式换热器壳程结构,对壳程工质为空气时,4种类型旋流片和空心环分别支撑缩放管管束的传热与流阻性能进行了实验研究,并进行了相互比较。实验结果表明:工质为空气时,270-20.3、180-20.3两种旋流片分别与缩放管管束配合,均具有优良的复合强化传热性能。尤其是270-20.3旋流片与缩放管管束配合,当Reynolds数为2000~20000时,其强化传热综合评价因子比空心环与缩放管管束配合时平均高出18%。 相似文献
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通过数值模拟,以水为工质,研究了湍流时旋流片支撑缩放管管束管间的传热综合性能,并与无支撑光滑管管束、无支撑缩放管管束及旋流片支撑光滑管管束的传热性能进行了对比,分析了不同结构参数对其传热综合性能的影响;揭示了旋流片支撑缩放管管间流体速度场与温度场之间的协同性。结果表明:旋流片支撑急扩慢缩型缩放管管束相对急缩慢扩型具有更好的传热综合性能,且都比旋流片支撑光滑管管束的传热综合性能好,但二者都没有对应的无支撑缩放管管束综合性能好;具有小角度跟大扭率结构的旋流片更有利于旋流片支撑管束传热综合性能的提高;相对旋流片支撑光滑管管束与无支撑缩放管管束,旋流片支撑缩放管管束强化传热的原因在于传热场协同的增强作用更为明显。考虑管间支撑物支撑管束与抗振的必要性,旋流片支撑缩放管管束是一种高效的壳程强化传热措施,文中条件下通过优化,最大传热综合性能能达到1.057。 相似文献
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为了获得较好的传热性能,提出一种在缩放管内间隔插入旋流片的复合强化传热方法。采用水为流动介质,在湍流状态下,通过数值模拟,详细研究了缩放管内插入旋流片的速度场与热流场的分布特性及其相互间的协同。对缩放管插入不同结构旋流片的热阻性能与缩放管和光滑管进行了比较,模拟结果表明,在相同条件下,传热系数和阻力系数最大分别提高25%,120%,120%,370%。缩放管与旋流片的复合使用能有效地改善速度场和温度场的协同程度,是提高换热性能的一个有效手段。 相似文献
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介绍了粗糙管换热器中沿传热管轴向间隔分置旋流片的两区协同强化传热方法。旋流片使流体产生螺旋流,螺旋流在离开旋流片之后依靠自身的运动惯性保持一定距离的自旋流,对管道近壁区与中心区产生互动的协同传热强化。此外,该方法也可用于管间,除了对管间管束的机械支撑外,旋流片也可使管间流体产生自旋运动,实现壳程流体的两区协同传热强化。对现有工业系统的换热器技术升级、实现节能降耗意义重大。 相似文献
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管内周期性自旋流强化传热的结构优化 总被引:8,自引:2,他引:6
在圆管内间隔插入多个旋流片的流道中,流体流动呈现周期性自旋流.用数值模拟方法对空气湍流情况的传热和流阻性能受相邻旋流片间距Lp、旋流角β和旋转角α3个因素的影响进行了分析,并得出旋流片的优化结构,而且实验验证了数值模拟预测的正确性.结果表明:α越大,传热性能越好,阻力越大;Lp越小,传热性能越好,阻力越大;β越大,传热性能越好,而阻力损失因受到摩擦阻力和形体阻力的综合影响而呈现非单调变化.旋流片的最佳结构参数为:旋流角β为20.3°,旋转角α为180°,相邻旋流片间距Lp为33d.与α相比,β对传热和流阻性能的影响更显著. 相似文献
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The distributions of thermal resistance in viscous sublayer,buffer region and turbulent core region,local flow resistance and local heat transfer characteristics at different locations downstream of the twisted-tape element were numerically studied in a converging-diverging tube inserted with spaced twisted-tape element by analyzing the attenuation of self-sustaining swirl flow.The results showed that the local performance was poor as thermal resistance was too concentrated in its distribution for a particular region.The more uniform the distribution of thermal resistance,the better the local performance.The local performance reached its best when the fluid just left the spaced twisted-tape,in which the flow resistance dropped substantially but the enhancement of heat transfer was still significant.The self-sustaining flow was maintained at a long distance.The best performance was at the length of 36.85 times the diameter,increasing by 6.8% compared with a converging-diverging tube. 相似文献
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含间隔分置旋流片的缩放管复合强化传热 总被引:3,自引:0,他引:3
Pressure drop and compound heat transfer characteristics of a converging-diverging tube with evenly spaced twisted-tapes (CD-T tube) have been investigated experimentally. Swirl was generated by evenly spaced twisted-tape elements which vary in twist ratio and rotation angle. Space ratio also has an important effect on the characteristics. For comparison, experiments in a smooth circular tube and a converging-diverging (CD) tube with-out twisted-tapes were carried out. The results show that the twisted-tape with twist ratio y=4.72 and rotation angle θ=180° has the best performance among the four types of twisted-tapes presented in this paper. At Reynolds number ranging from 3400 to 20000, when space ratio s=48.6, the heat transfer efficiency index, which increases as the Reynolds number increases, is 0.85-1.21 and 1.07-1.15 compared to that of a smooth circular tube and a CD tube without twisted-tape inserts, respectively. 相似文献
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The paper presents a 3D numerical simulation of turbulent heat transfer and flow characteristics in converging-diverging tubes(CDs) and converging-diverging tubes equipped with twin counter-swirling twisted tapes(CDTs).The effects of Reynolds number(Re 10000-20000),pitch length(P 11.25,22.5 mm),rib height(e 0.5,0.8,1.1 mm),pitch ratio(δ1:8,5:4,8︰1),gap distance between twin twisted tapes(b 0.5,4.5,8.5 mm) and tape number(n 2,3,4,5,6) on Nusselt number(Nu),friction factor(f) and thermal enhancement factor(η) are investigated under uniform heat flux conditions,using water as working fluid.In order to illustrate the heat transfer and fluid flow mechanisms,flow structures in CDs and CDTs are presented.The obtained results reveal that all geometric parameters have important effects on the thermal performance of CD and CDT,and both CD and CDT show better thermal performance than plain tube at the constant pumping power.It is also found that the increases in the Nusselt number and friction factor for CDT are,respectively,up to 6.3%-35.7% and 1.75-5.3 times of the corresponding bare CD.All CDTs have good thermal performance with η greater than 1 which indicates that the compound heat transfer technique of CDT is commendable for the maximum enhanced heat transfer rate. 相似文献
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自转螺旋扭带管内湍流特性研究 总被引:6,自引:0,他引:6
应用激光测速仪LDV(Laser Doppler Velocimeter)对自转塑料螺旋扭带管的湍流特性进行了实验研究。结果表明:与普通光管内流体的流动相比,自转塑料螺旋扭带管内流体的湍流特性发生了根本性的变化:流体在自转塑料螺旋扭带的带动下,呈螺旋流动,而且在近管壁环形区域内流体的轴向分速度明显比管中心区域的高,提高幅度为25%左右,轴向湍流度比无自转扭带的大,提高幅度为68%左右;切向分速度随半径的增大而增大,而且切向湍流度很大,比轴向湍流度大10倍左右。流体的这些湍流特性的测得为自转塑料螺旋扭带管内对流传热强化机理的深入理论研究提供了实验支持。 相似文献