Laser Recording in Chalcogenide Glass Films: Driving Forces and Kinetics of the Mass Transfer

2020 ◽  
Vol 217 (23) ◽  
pp. 2000523
Author(s):  
Yuri S. Kaganovskii ◽  
Hadar Genish ◽  
Michael Rosenbluh
1982 ◽  
Vol 47 (3) ◽  
pp. 766-775 ◽  
Author(s):  
Václav Kolář ◽  
Jan Červenka

The paper presents results obtained by processing a series of published experimental data on heat and mass transfer during evaporation of pure liquids from the free board of a liquid film into the turbulent gas phone. The data has been processed on the basis of the earlier theory of mechanism of heat and mass transfer. In spite of the fact that this process exhibits a strong Stefan's flow, the results indicate that with a proper definition of the driving forces the agreement between theory and experiment is very good.


2021 ◽  
Vol 608 ◽  
pp. 412745
Author(s):  
Mohamed N. Abd-el Salam ◽  
E.R. Shaaban ◽  
F. Benabdallah ◽  
Abdelwahab M.A. Hussein ◽  
Mansour Mohamed

2008 ◽  
Vol 273-276 ◽  
pp. 679-684
Author(s):  
Roberto Parreiras Tavares ◽  
André Afonso Nascimento ◽  
Henrique Loures Vale Pujatti

The RH process is a secondary refining process that can simultaneously attain significant levels of removal of interstitial elements, such as carbon, nitrogen and hydrogen, from liquid steel. In the RH process, the decarburization rate plays a very important role in determining the productivity of the equipment. The kinetics of this reaction is controlled by mass transfer in the liquid phase. In the present work, a physical model of a RH degasser has been built and used in the study of the kinetics of decarburization. The effects of the gas flow rate and of the configurations of the nozzles used in the injection of the gas have been analyzed. The decarburization reaction of liquid steel was simulated using a reaction involving CO2 and caustic solutions. The concentration of CO2 in the solution was evaluated using pH measurements. Based on the experimental results, it was possible to estimate the reaction rate constant. A volumetric mass transfer coefficient was then calculated based on these rate constants and on the circulation rate of the liquid. The logarithm of the mass transfer coefficient showed a linear relationship with the logarithm of the gas flow rate. The slope of the line was found to vary according to the relevance of the reaction at the free surface in the vacuum chamber. A linear relationship between the volumetric mass transfer coefficient and the nozzle Reynolds number was also observed. The slopes of the lines changed according to the relative importance of the two reaction sites, gas-liquid interface in the upleg snorkel and in the vacuum. At higher Reynolds number, the reaction in the vacuum chamber tends to be more significant.


2012 ◽  
Vol 207-208 ◽  
pp. 539-551 ◽  
Author(s):  
Nicola Gemo ◽  
Pierdomenico Biasi ◽  
Paolo Canu ◽  
Tapio O. Salmi

2014 ◽  
Vol 50 (3) ◽  
pp. 448-464 ◽  
Author(s):  
E. P. Fel’dman ◽  
T. A. Vasilenko ◽  
N. A. Kalugina
Keyword(s):  

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