{"title":"Mixed Convection Adjacent to 3-D Backward-Facing Step","authors":"An Li, B. Armaly","doi":"10.1115/imece2000-1408","DOIUrl":null,"url":null,"abstract":"Results from three-dimensional numerical simulation of laminar, buoyancy assisting, mixed convection airflow adjacent to a backward-facing step in a vertical rectangular duct are presented. The Reynolds number, and duct geometry were kept constant at Re = 200, AR = 8, ER = 2, and S = 1 cm. Heat flux at the wall downstream from the step was kept uniform, but its magnitude was varied to cover a Grashof number (Gr) range between 0.0 to 4000. All the other walls in the duct were kept at adiabatic condition. The flow, upstream of the step, is treated as fully developed and isothermal. The relatively small aspect ratio of the channel is selected specifically to focus on the developments of the three-dimensional mixed convection flow in the separated and reattached flow regions downstream from the step. The presented results focus on the effects of increasing the buoyancy force, by increasing the uniform wall heat flux, on the three-dimensional flow and heat transfer characteristics. The flow and thermal fields are symmetric about the duct’s centerline. Vortex generated near the sidewall, is the major contributor to the three dimensional behavior in the flow domain, and that feature increases as the Grashof number increases. Increasing the Grashof number results in an increase in the Nusselt number, the size of the secondary recirculating flow region, the size of the sidewall vortex, and the spanwise flow from the sidewall toward the center of the channel. On the other hand, the size of the primary reattachment region decreases with increasing the Grashof number. That region lifts away and partially detaches from the downstream wall at high Grashof number flow. The maximum Nusselt number occurs near the sidewalls and not at the center of the channel. The effects of the buoyancy force on the distributions of the three-velocity components, temperature, reattachment region, friction coefficient, and Nusselt number are presented, and compared with 2-D results.","PeriodicalId":201774,"journal":{"name":"Heat Transfer: Volume 2","volume":"28 1","pages":"0"},"PeriodicalIF":0.0000,"publicationDate":"2000-11-05","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"11","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Heat Transfer: Volume 2","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.1115/imece2000-1408","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 11
Abstract
Results from three-dimensional numerical simulation of laminar, buoyancy assisting, mixed convection airflow adjacent to a backward-facing step in a vertical rectangular duct are presented. The Reynolds number, and duct geometry were kept constant at Re = 200, AR = 8, ER = 2, and S = 1 cm. Heat flux at the wall downstream from the step was kept uniform, but its magnitude was varied to cover a Grashof number (Gr) range between 0.0 to 4000. All the other walls in the duct were kept at adiabatic condition. The flow, upstream of the step, is treated as fully developed and isothermal. The relatively small aspect ratio of the channel is selected specifically to focus on the developments of the three-dimensional mixed convection flow in the separated and reattached flow regions downstream from the step. The presented results focus on the effects of increasing the buoyancy force, by increasing the uniform wall heat flux, on the three-dimensional flow and heat transfer characteristics. The flow and thermal fields are symmetric about the duct’s centerline. Vortex generated near the sidewall, is the major contributor to the three dimensional behavior in the flow domain, and that feature increases as the Grashof number increases. Increasing the Grashof number results in an increase in the Nusselt number, the size of the secondary recirculating flow region, the size of the sidewall vortex, and the spanwise flow from the sidewall toward the center of the channel. On the other hand, the size of the primary reattachment region decreases with increasing the Grashof number. That region lifts away and partially detaches from the downstream wall at high Grashof number flow. The maximum Nusselt number occurs near the sidewalls and not at the center of the channel. The effects of the buoyancy force on the distributions of the three-velocity components, temperature, reattachment region, friction coefficient, and Nusselt number are presented, and compared with 2-D results.
本文对垂直矩形风管中靠近后台阶的层流、浮力辅助、混合对流气流进行了三维数值模拟。雷诺数和导管几何形状在Re = 200, AR = 8, ER = 2, S = 1 cm时保持不变。台阶下游壁面的热流密度保持均匀,但其大小在0.0 ~ 4000之间变化。管道中的其他壁都保持绝热状态。台阶上游的流体被认为是完全发育的等温流体。专门选择相对较小的通道宽高比,以关注台阶下游分离和再附着流区的三维混合对流流动的发展。研究结果着重于通过增加均匀壁面热流密度来增加浮力对三维流动和换热特性的影响。流场和热场围绕管道中心线对称。在侧壁附近产生的涡是影响流域三维特性的主要因素,并且该特征随着Grashof数的增加而增加。增大Grashof数导致Nusselt数增大,二次再循环流区增大,侧壁涡增大,从侧壁向通道中心的展向流动增大。另一方面,随着Grashof数的增加,初级再附着区域的大小减小。在高格拉希夫数流速下,该区域从下游壁面上抬升并部分分离。最大努塞尔数出现在通道的侧壁附近,而不是在通道的中心。给出了浮力对三速度分量、温度、再附着面积、摩擦系数和努塞尔数分布的影响,并与二维结果进行了比较。