The diameter of silicon carbide (SiC) single crystal grown by the physical
vapor transport method has increased significantly in recent years. Process
modeling has played an important role in designing and developing the larg
e diameter SIC growth systems. The numerical algorithm incorporates the cal
culations of radio-frequency, time-harmonic magnetic field by induction hea
ting, radiation and conduction heat transfer in the system, as well as the
growth kinetics. The generated power density in the graphite susceptor is o
btained by solving the magnetic vector potential equations, and radiative h
eat transfer is calculated from the integrated equations for radiation. Che
mical reactions and transport of gaseous species, Si2C, SiC2, SiC and Si, a
re also considered. A growth kinetics model is proposed for the first time,
which uses the Hertz-Knudsen equation to relate the growth rate to the sup
ersaturation of a rate-determining vapor species, the driving force for the
deposition. The theoretical predictions compare reasonably with the publis
hed experimental data. The growth rate curves are obtained as a function of
growth temperature and system pressure. The growth kinetics is greatly inf
luenced by the inert gas pressure, temperature and temperature gradient. Si
nce the vapor pressure is an ascending function of the temperature, for low
temperature growth, a larger temperature gradient is needed in order to ac
hieve the desired level of supersaturation (or growth rate). A low temperat
ure growth is usually associated with small diameter systems, which maintai
n larger temperature differences. At a high growth temperature, since the v
apor pressure is high, only a small temperature difference is required to a
chieve the same level of supersaturation. Desirable growth temperature and
growth rate profiles can be obtained across the seed surface by optimizing
the furnace components, such as the graphite susceptor, induction coil, and
insulation materials. (C) 2001 Elsevier Science B.V. All rights reserved.