Heat exchange in a draining liquid film in the initial thermal part

1980 ◽  
Vol 39 (4) ◽  
pp. 1043-1046 ◽  
Author(s):  
V. M. Sobin
1988 ◽  
Vol 54 (5) ◽  
pp. 490-492
Author(s):  
V. G. Rifert ◽  
Yu. V. Putilin ◽  
V. L. Podbereznyi

1994 ◽  
Vol 30 (2) ◽  
pp. 78-81
Author(s):  
A. M. Makarov ◽  
S. S. Sorokin

1978 ◽  
Vol 34 (4) ◽  
pp. 391-394
Author(s):  
N. S. Mochalova ◽  
L. P. Kholpanov ◽  
V. A. Malyusov ◽  
N. M. Zhavoronkov

2020 ◽  
Vol 38 (3) ◽  
pp. 622-628
Author(s):  
Vitaly V. Dubrovsky ◽  
Aleksandr A. Shraiber

The laws of heat exchange between air and a liquid film flowing down along a solid surface with spherical dimples were investigated experimentally. Three cases of heat transfer were considered: quiescent air, air – liquid counter flow, or their cross flow. In all cases, a significant growth of the heat exchange intensity, especially at air – liquid cross flow, was observed. This is caused by the substantial turbulization of flow and mixing of liquid layers in the film. As a result, it was established that surface profiling (manufacture of dimples) under the optimal conditions leads to an increase in heat exchange intensity by an unexpended factor of 2.5 – 2.8 as compared with a smooth surface, other conditions being equal. The obtained experimental data were generalized in the form of dimensionless dependences Nu vs. Re. The best heat transfer surface can be recommended for use in different heat exchangers.


Author(s):  
A. A. Genbach ◽  
K. K. Shokolakov

Nozzle-free capillary-porous dust and gas trap with foam generating and defoaming structures was developed and studied. Foam flow is generated by dusty gas, micro and ultra microscopic particles, which are especially dangerous for human body, are cleaned. Stability of liquid film in the porous structure during supply of foam-forming liquid by a spray in the form of a tubular ring, was determined. Foam generating and defoaming structures have been optimized, due to this material consumption and dimensions are reduced by 2-2.5 times, hydraulic resistance - by dozens of times (up to one hundred times), and gas-dynamic - by up to two times.


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