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Table
6:
Comparison of measured Ky and calculated
&
weight loss rates for Sic of this study
with data published by Robinson [9]
and
Opila
[lo]
at 1400°C.
0.062
In principle, all data are of the same order of magni-
tude. The calculated values were found to be lower than
the measured data in all cases, indicating the very com-
plex character of the corrosion processes, e.g., the pres-
ence of other silicon hydroxides than %(OH),,
as
pro-
posed by Opila. As a consequence
of
the addition
of
steam, which produced the highest partial vapor pres-
sure, the highest weight loss rate was observed in Test
1
of this study. The weight
loss
rates from Test
3
and
from tests in the literature in which a similar partial
steam pressure was used seem to be more comparable.
While the calculated data were found to be similar, the
higher weight loss rate
of
Test 3 in this study may be the
consequence of a higher influence of the flow speed in
the burner rig.
CONCLUSIONS
Silicon-based nonoxide ceramic materials were stud-
ied in a corrosive atmosphere similar to that in a gas
turbine at high temperatures. Under these conditions,
the microstructural stability
of
the bulk material can be
stabilized by e.g. Si3N4-MoSi2 composites by a mecha-
nism similar to the mechanisms found during oxidation
of these materials in air.
Unlike oxidation in air, the tests in the burner rig
caused all materials to suffer surface degradation. The
weight loss measured was the consequence of the for-
mation and evaporation of silicon hydroxides, mainly
Si(OH)4.. The oxidation surface layer
of
mainly SiO,,
which
is
essential for the oxidation protection of
nonoxide materials because it induces the passive,
diffusion-controlled oxidation mechanism,
was
found to
be degraded. As a result of this, the material showed a
higher rate of oxidation. The main factor influencing the
evaporation processes seems to be the partial vapor
pressure. In spite of the different burner rig set-ups and
test conditions, the data obtained in this study were
similar
to
the results for corrosion
of
CVD Sic reported
in the literature. However, additional studies are re-
quired for a quantitative interpretation
of
the influence
of test parameters such as pressure, partial vapor pres-
sure and flow speed.
ACKNOWLEDGMENTS
We acknowledge the interesting discussions with E.
Opila,
R.
Robinson and J. Smialek, NASA Glenn Re-
search Center, Cleveland. The studies were carried out
on behalf of Siemens KWU Mulheim.
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156