Transient heat transfer performance of stainless steel structured surfaces combined with air-water spray evaporative cooling at high temperature scenarios

2017 ◽  
Vol 115 ◽  
pp. 418-434 ◽  
Author(s):  
Muhammad Aamir ◽  
Liao Qiang ◽  
Wang Hong ◽  
Zhu Xun ◽  
Jiaqiu Wang ◽  
...  
2022 ◽  
Vol 171 ◽  
pp. 107243
Author(s):  
Javier Gil-Font ◽  
Nuria Navarrete ◽  
Estefanía Cervantes ◽  
Rosa Mondragón ◽  
Salvador F. Torró ◽  
...  

2014 ◽  
Vol 1081 ◽  
pp. 270-274
Author(s):  
Zui Xian Yu ◽  
Xue Sheng Wang ◽  
Qin Zhu Chen

A new preparation technique of carbon steel/stainless steel clad tube was introduced, and the contact surface was well combined. Meanwhile, with the using of tube heat exchanger, the experiment on the heat transfer performance of the clad tube was done. Comparing the 10/316 clad tube and the 316 stainless steel tube, the effects on the heat transfer performance of 316 stainless steel tube attached to carbon steel was evaluated. It is showed that overall heat transfer coefficient of 10/316 clad tubes is higher than that of stainless steel tube. The average heat transfer coefficient of 10/316 clad tubes is about 18.7%~34.4% higher than that of stainless steel tube. Experimental investigation indicates that, by brazing and cold drawing, the 10/316 clad tube was well combined and the thermal conductivity was better than that of stainless steel tube.


2015 ◽  
Vol 27 (1) ◽  
pp. 16001
Author(s):  
郭海兵 Guo Haibing ◽  
马纪敏 Ma Jimin ◽  
王少华 Wang Shaohua ◽  
宋娟 Song Juan ◽  
祁建敏 Qi Jianmin

Author(s):  
Tomohiro Hirano ◽  
Mitsuo Yoshimura ◽  
Koji Shimoyama ◽  
Atsuki Komiya

Abstract Toward a practical application of the additive manufacturing (AM), this study proposes a shape optimization approach for the cross-sectional shape of the inner pipe of a counter-flow double pipe heat exchanger. The cross-sectional shape of the inner pipe is expressed by an algebraic expression with a small number of parameters, and their heat transfer performance is evaluated by a commercial Computational Fluid Dynamics (CFD) solver. The optimization is conducted by the Non-Dominated Sorting Genetic Algorithm II (NSGA-II) assisted by the Kriging surrogate model, and the NSGA-II finds the optimal cross-sectional shape with many protrusions around the perimeter of the inner channel to improve the heat transfer performance. In this study, heat transfer performance is evaluated from the temperature drop at the outlet of the high-temperature fluid. Through the comparison of two cross-sectional shapes with the same heat transfer surface area — average temperature at the outlet of the optimal high-temperature channel is 324.58 K while average temperature at the outlet of a circular high-temperature channel with the same area as the optimal channel is 331.93 K, it is revealed that the number of protrusions plays important roles which contribute not only to increase heat transfer area but also to improve heat transfer performance.


Author(s):  
C. Y. Zhao ◽  
D. Zhou ◽  
Z. G. Wu

In this paper the solid/liquid phase change heat transfer in porous materials (metal foams and expanded graphite) at low and high temperatures is experimentally investigated, in an attempt to examine the feasibility of using metal foams to enhance the heat transfer capability of phase change materials for use with both the low and high temperature thermal energy storage systems. In this research, the organic commercial paraffin wax and inorganic hydrate calcium chloride hydrate salts were employed as the low-temperature materials, while the sodium nitrate is used as the high-temperature PCM in the experiment. The heat transfer characteristics of these PCMs embedded with open-cell metal foams were studied experimentally. The composites of paraffin and expanded graphite with different graphite mass ratios, namely, 3%, 6% and 9%, were also made and the heat transfer performances of these composites were tested and compared with metal foams. Overall metal foams can provide better heat transfer performance than expanded graphite due to their continuous inter-connected structures. But the porous materials can suppress the natural convection effect in liquid zone, particularly for the PCMs with low viscosities, thereby leading to the different heat transfer performance at different regimes (solid, solid/liquid and liquid regions). This implies that the porous materials don’t necessarily mean they can always enhance heat transfer in every regime.


2016 ◽  
Vol 110 ◽  
pp. 327-337 ◽  
Author(s):  
Xian-long Meng ◽  
Xin-lin Xia ◽  
Shun-de Zhang ◽  
Nazmi Sellami ◽  
Tapas Mallick

2019 ◽  
Vol 158 ◽  
pp. 541-546 ◽  
Author(s):  
Xiangyang Shen ◽  
Jianfeng Lu ◽  
Jing Ding ◽  
Weilong Wang

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