0114 Flow and Heat Transfer Control of Fin-Tube Type Heat Exchanger : Effects of Vortex Generator

2009 ◽  
Vol 2009 (0) ◽  
pp. 31-32
Author(s):  
Toshihiko Shakouchi ◽  
Keiji Hori ◽  
Ichiro Suzaki ◽  
Koichi Tsujimoto ◽  
Toshitake Ando
2020 ◽  
Vol 2020 (0) ◽  
pp. S05114
Author(s):  
Toshihiko SHAKOUCHI ◽  
Shoma OTA ◽  
Kazuma YAMAMURA ◽  
Koichi TSUJIMOTO ◽  
Toshitake ANDO ◽  
...  

Author(s):  
Haolin Ma ◽  
Alparslan Oztekin

Computational fluid dynamics and heat transfer simulations are conducted for a novel shell-tube type heat exchanger. The heat exchanger consists of tube with a narrow slot oriented in the streamwise direction. Numerical simulations are conducted for the Reynolds number of 1500. The 3D turbulent flow in the tube bank region is modeled by k-ε Reynolds stress averaging method by employing ANSYS FLUENT. 3-D transient flow and heat transfer simulations are conducted to determine the flow structure and temperature profiles in the wake of cylinders in the first row and other rows. The effects of the slot size and the orientation and the arrangement of the cylinder in different configuration will be examined. The slotted tube heat exchanger improved heat transfer by more than 27% compare to the traditional shell-tube heat exchanger without slots. Enhancement in heat transfer is even higher at higher values of Reynolds number.


2014 ◽  
Vol 2014 (0) ◽  
pp. _E123-1_-_E123-2_
Author(s):  
Yuya Arakawa ◽  
Taketo Uchino ◽  
Taro Nakanishi ◽  
Ryutaro Shinohara

2019 ◽  
Vol 28 (1) ◽  
pp. 47-57 ◽  
Author(s):  
Sachin Gupta ◽  
Aditya Roy ◽  
Arvind Gupta

The heat transfer performance of fin-tube heat exchangers can be enhanced with the help of longitudinal vortex generators. In this work, we investigate the effect of employing a rectangular winglet having a punched hole on heat transfer and flow resistance characteristics in a fin-tube heat exchanger with the help of numerical simulations. Studies were performed on two configurations, namely, common flow down and common flow up at upstream and downstream locations. Performance characteristics such as Colburn’s factor ( j), friction factor ( f), and performance evaluation criterion were considered for evaluating the thermohydraulic performance. Investigations were performed considering Reynolds number in the range of 1500–9000, keeping the angle of attack as 45°. The shear stress transport k-ω turbulence model was used for performing numerical simulations. A significant augmentation of up to 71% in the thermohydraulic performance of fin-tube heat exchanger was observed with the common flow down configuration located upstream over the common flow up configuration located upstream, which displayed the least improvement.


2020 ◽  
Vol 12 (3) ◽  
pp. 168781402091148 ◽  
Author(s):  
Amnart Boonloi ◽  
Withada Jedsadaratanachai

Flow prediction, heat transfer pattern, and thermo-hydraulic efficiency in a heat exchanger tube fitted with vortex generator are chosen for the present research. The 30° inclined ring is opted to develop the performance of the heat exchanger tube. The effects of inclined ring configuration and placement in the heat exchanger tube on the patterns of flow and heat transfer are investigated. The Reynolds number (at the entry zone of the periodic model) in the range of around 100–2000 (laminar flow region) is discussed. The heat transfer ability, pressure loss, and efficiency of the heat exchanger tube fitted with 30° inclined ring are analyzed with the numerical method (finite volume method). The SIMPLE algorithm of the commercial code is picked for the present study. The simulated results in the heat exchanger tube fitted with 30° inclined ring are offered in patterns of streamlines, temperature contour, and Nusselt number contour. From the preliminary result, it is found that the creation model of the heat exchanger tube fitted with 30° inclined ring has sufficient reliance to measure flow and heat transfer profiles. The installment of the 30° inclined ring in the heat exchanger tube leads to greater heat transfer ability and thermo-hydraulic performance because of the creation of the vortex flow and thermal boundary layer disturbance on the heat exchanger tube surface. The heat transfer ability in the heat exchanger tube fitted with 30° inclined ring is found to be around 1.00–10.56 times above the plain circular tube. In addition, the installation of the 30° inclined ring in the heat exchanger tube gives the maximum thermal enhancement factor around 3.18.


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