Characterization and control of the fiber-matrix interface in ceramic ...
Characterization and control of the fiber-matrix interface in ceramic ...
Characterization and control of the fiber-matrix interface in ceramic ...
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77<br />
was not deoxygenated. O<strong>the</strong>r gases such as silane, ammonia, <strong>and</strong> diborane<br />
were not treated but were used as received (at least 99.99% purity).<br />
Methyltrichlorosilane (MTS), which is a liquid at room temperature,<br />
was carried to <strong>the</strong> reactor by a flow <strong>of</strong> hydrogen through an evaporator,<br />
<strong>and</strong> flow was metered us<strong>in</strong>g a vapor source <strong>control</strong>ler.* On bubbl<strong>in</strong>g <strong>the</strong><br />
hydrogen carrier gas through <strong>the</strong> reservoir conta<strong>in</strong><strong>in</strong>g <strong>the</strong> liquid<br />
reactant, <strong>the</strong> gas stream becomes saturated with vapor. The vapor-source<br />
<strong>control</strong>ler monitors <strong>the</strong> heat capacity <strong>of</strong> <strong>the</strong> <strong>in</strong>com<strong>in</strong>g gas <strong>and</strong> <strong>the</strong> exit<br />
gas mixture <strong>and</strong>, by subtract<strong>in</strong>g <strong>the</strong> <strong>in</strong>com<strong>in</strong>g carrier flow signal, can<br />
measure <strong>the</strong> vapor concentration <strong>in</strong> <strong>the</strong> outgo<strong>in</strong>g mixture. The <strong>control</strong>ler<br />
varies <strong>the</strong> flow <strong>of</strong> hydrogen to <strong>the</strong> reservoir to ma<strong>in</strong>ta<strong>in</strong> <strong>the</strong> given vapor<br />
concentration. The gas-vapor mixture is <strong>the</strong>n diluted to <strong>the</strong> proper ratio<br />
us<strong>in</strong>g a mass flow <strong>control</strong>ler that is placed <strong>in</strong> series with <strong>the</strong> vapor-<br />
source <strong>control</strong>ler.<br />
The system is designed to allow for complete <strong>control</strong><br />
<strong>of</strong> not only vapor flow but gas-to-vapor ratios. Although <strong>the</strong> source<br />
<strong>control</strong>ler ma<strong>in</strong>ta<strong>in</strong>s <strong>the</strong> flow <strong>of</strong> reactant <strong>in</strong>dependent <strong>of</strong> pressure or<br />
temperature, <strong>the</strong> reservoir temperature was held at 297 K us<strong>in</strong>g a constant<br />
temperature bath to m<strong>in</strong>imize cool<strong>in</strong>g effects caused by <strong>the</strong> evaporation <strong>of</strong><br />
<strong>the</strong> MTS.<br />
On completion <strong>of</strong> densification, a programmed cool-down sequence was<br />
used to m<strong>in</strong>imize <strong>the</strong>rmal shock effects. Temperature <strong>control</strong> was switched<br />
from <strong>the</strong> optical pyrometer to a <strong>the</strong>rmocouple <strong>control</strong>led programmer. **<br />
*Research, Inc . , M<strong>in</strong>neapolis, M<strong>in</strong>nesota.<br />
""Tylan, Inc., Torrance, California.