Falling liquid film periodical fluctuation over a superhydrophilic horizontal tube at low spray density

Author(s):  
Yi Zheng ◽  
Guoxin Chen ◽  
Xiangdi Zhao ◽  
Wanfu Sun ◽  
Xuehu Ma
1992 ◽  
Vol 27 (8) ◽  
pp. 489-497 ◽  
Author(s):  
P. K. Sarma ◽  
J. Saibabu

Author(s):  
Sergey Alekseenko ◽  
Aleksey V. Bobylev ◽  
Vladimir V. Guzanov ◽  
Sergey M. Kharlamov ◽  
Alexandr Z. Kvon ◽  
...  

2020 ◽  
Vol 1677 ◽  
pp. 012091
Author(s):  
A N Pavlenko ◽  
N I Pecherkin ◽  
O A Volodin ◽  
A I Kataev ◽  
I B Mironova

2011 ◽  
Vol 19 (03) ◽  
pp. 177-183 ◽  
Author(s):  
JIN-BO CHEN ◽  
QING-GANG QIU

The technique of horizontal-tube falling film has been used in the cooling and heating industries such as refrigeration systems, heating systems and ocean thermal energy conversion systems. The comprehensive performance of evaporator is directly affected by the film distribution characteristics outside tubes. In this paper, numerical investigation was performed to predict the film characteristics outside the tubes in horizontal-tube falling film evaporator. The effects of liquid flow rate, tube diameter and the circular degree of tube on the film thickness were presented. The numerical simulation results were compared with that of the empirical equations for calculating the falling film thickness, and agreements between them were reasonable. Numerical simulation results show that, at the fixed fluid flow density, the liquid film is thicker on the upper and lower tube and the thinnest liquid film appears at angle of about 120°. The results also indicate that, when the fluid flow density decreases to a certain value, the local dryout spot on the surface of the tube would occur. In addition, the film thickness decreases with the increases of the tube diameter at the fixed fluid flow density.


1978 ◽  
Vol 45 (1) ◽  
pp. 19-24 ◽  
Author(s):  
V. Narayanamurthy ◽  
P. K. Sarma

The dynamics of accelerating, laminar non-Newtonian falling liquid film is analytically solved taking into account the interfacial shear offered by the quiescent gas adjacent to the liquid film under adiabatic conditions of both the phases. The results indicate that the thickness of the liquid film for the assumed power law model of the shear deformation versus the shear stress is influenced by the index n, the modified form of (Fr/Re). The mathematical formulation of the present analysis enables to treat the problem as a general type from which the special case for Newtonian liquid films can be derived by equating the index in the power law to unity.


Sign in / Sign up

Export Citation Format

Share Document