Heat and mass transfer modeling for a better knowledge of the large-area growth of homoepitaxial SiC by CVD

2000 ◽  
Vol 640 ◽  
Author(s):  
Michel Pons ◽  
Jerome Mezière ◽  
Jean Marc Dedulle ◽  
Stephane Wan Tang Kuan ◽  
Elisabeth Blanquet ◽  
...  

ABSTRACTThe growth of thick epitaxial 4H-SiC layers with low defect density is an essential step for the fabrication of SiC based devices. Cold- and hot wall reactors using silane and propane diluted in hydrogen were used in this study. The typical growth temperature range is 1700–1900 K and total pressure range 10–100 kPa. The resulting epilayers exhibit low background doping, low defect density and good thickness uniformity. The main problem is that it is difficult with this first generation of reactors to ensure a constant temperature over large wafer. A 3D simulation approach of heat and mass transfer was used with three objectives. The first one is to have a visualization of the flow, temperature and gaseous species fields in the standard reactor. The second one is to propose solutions for the optimal control of the temperature field and the subsequent uniformity of the epilayers over large dimensions. The third one is to improve the kinetic databases in this temperature range which has been very little investigated.

Author(s):  
Tov Elperin ◽  
Andrew Fominykh ◽  
Boris Krasovitov

In this study we investigated numerically simultaneous heat and mass transfer during evaporation/condensation on the surface of a stagnant droplet in the presence of inert admixtures containing non-condensable solvable gas. The performed analysis is pertinent to slow droplet evaporation/condensation when Mach number is small (M≪1). The system of transient conjugate nonlinear energy and mass conservation equations was solved using anelastic approximation. Transport coefficients of the gaseous phase were calculated as functions of temperature and concentrations of gaseous species. Thermophysical properties of the liquid phase are assumed to be constant. Using the material balance at the droplet surface we obtained equations for Stefan velocity and the rate of change of the droplet radius taking into account the effect of solvable gas absorption at the gas-liquid interface. We derived also boundary conditions at gas-liquid interface taking into account the effect of gas absorption. The governing equations were solved using a method of lines. Numerical calculations showed essential change of the rates of heat and mass transfer in water droplet-air-water vapor system under the influence of solvable species in a gaseous phase. Consequently, the use of additives of solvable noncondensable gases to enhance the rate of heat and mass transfer in dispersed systems allows to increase the efficiency and reduce the size of gas-liquid contactors.


2009 ◽  
Vol 27 (10) ◽  
pp. 1051-1059 ◽  
Author(s):  
Y. L. Lin ◽  
S. J. Li ◽  
Y. Zhu ◽  
G. Bingol ◽  
Z. Pan ◽  
...  

2016 ◽  
Vol 171 ◽  
pp. 1-13 ◽  
Author(s):  
L. Lecoq ◽  
D. Flick ◽  
E. Derens ◽  
H.M. Hoang ◽  
O. Laguerre

2018 ◽  
Vol 556 ◽  
pp. 248-262 ◽  
Author(s):  
Amin Engarnevis ◽  
Ryan Huizing ◽  
Sheldon Green ◽  
Steven Rogak

2013 ◽  
Vol 5 (2) ◽  
pp. 57-76 ◽  
Author(s):  
J. F. Cepeda ◽  
C. L. Weller ◽  
M. Negahban ◽  
J. Subbiah ◽  
H. Thippareddi

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