Electrohydrodynamic enhancement of in-tube convective condensation heat transfer

2006 ◽  
Vol 49 (9-10) ◽  
pp. 1647-1657 ◽  
Author(s):  
H. Sadek ◽  
A.J. Robinson ◽  
J.S. Cotton ◽  
C.Y. Ching ◽  
M. Shoukri
Author(s):  
Li Jia ◽  
Dongmei Wu

This paper combined modified film model and Nusselt’s condensation theory and studies convective condensation heat transfer on a horizontal tube across which moist mixed gas flows horizontally at a certain speed. A theoretical model allowing for gas boundary layer separation was set up and how the liquid film flows and the heat transfers on the tube were presented. The effects of flowing direction on condensation heat transfer are discussed. Results predict that the condensate is so thin that the liquid phase heat resistance can be ignored.


2020 ◽  
pp. 255-255
Author(s):  
Shuai Wang

The condensation heat transfer characteristics and corrosion resistance of copper, Ni-P-Cu, polytetrafluoroethylene, Ni-P and Ni coated tube surfaces were investigated. The results indicate that condensation heat transfer coefficient of Ni-P-Cu, PTFE, Ni-P and Ni coated tubes grows by 36.8%?29.3%, 19.6% and 7.5% than that of copper tubes, respectively. The phase structure of Ni, Ni-P, Ni-P-Cu and PTFE coated tube surfaces is mixed crystal structure(nanocrystals-based), mixed crystal structure (amorphous-based), amorphous structure and crystal structure, respectively. Compared with Ni coating and Ni-P coated tube surfaces, the condensation droplets outside Ni-P-Cu and PTFE coated tubes are smaller in size, more densely distributed, and fall off more quickly, which can significantly promote dropwise condensation. Ni-P-Cu coated tube surfaces achieve optimal condensation heat transfer. The corrosion speed of copper, Ni, Ni-P, Ni-P-Cu and PTFE coated tubes are 86.5, 42.6, 18.2, 10.7 and 6.1 mg?dm-2?d-1, respectively. PTFE coating tubes have the optimal corrosion resistance. Ni-P-Cu and PTFE coated tube surfaces have the best condensation heat transfer characteristics and corrosion resistance, and can be well used in the recovery of waste heat from low-temperature flue gas. The multiple linear regression of the experimental data was carried out to obtain the experimental correlation formula for Nusselt number of convective condensation composite heat transfer for different coated tubes. The relative error between the predicted value and the experimental value is within ?15%.


2002 ◽  
Vol 41 (3) ◽  
pp. 295-301 ◽  
Author(s):  
P.K Sarma ◽  
C.V.N Sastry ◽  
V.D Rao ◽  
Sadik Kakac ◽  
Hongton Liu

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