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Characterization and control of the fiber-matrix interface in ceramic ...

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80<br />

graphite holders through multiple wash<strong>in</strong>gs <strong>in</strong> acetone.<br />

The average <strong>fiber</strong><br />

content <strong>of</strong> <strong>the</strong> result<strong>in</strong>g <strong>fiber</strong> preforms was 41.4 f 1.3 vol %.<br />

9.3.2 Jntermediate coat<strong>in</strong>e deDositioQ<br />

The preforms next were precoated with th<strong>in</strong> layers <strong>of</strong> various<br />

materials.<br />

The deposition parameters <strong>and</strong> nom<strong>in</strong>al thicknesses <strong>of</strong> <strong>the</strong><br />

films are summarized <strong>in</strong> Table 9.1.<br />

The coat<strong>in</strong>g runs were carried out<br />

us<strong>in</strong>g <strong>the</strong> follow<strong>in</strong>g procedure. The preform was placed atop <strong>the</strong> graphite<br />

spacer, <strong>and</strong> Grafoil gaskets were used to seal <strong>the</strong> <strong>in</strong>jector to <strong>the</strong> spacer<br />

<strong>and</strong> <strong>the</strong> preform to <strong>the</strong> spacer.<br />

Hot water <strong>of</strong> 355 K average temperature<br />

was supplied to <strong>the</strong> <strong>in</strong>jector, whereas only cold water was passed through<br />

<strong>the</strong> furnace sections <strong>and</strong> electrodes.<br />

The apparatus was evacuated (with <strong>the</strong> exception <strong>of</strong> <strong>the</strong> MTS<br />

reservoir) to an ultimate pressure <strong>of</strong> < 0.5 torr us<strong>in</strong>g a rotary<br />

mechanical pump.<br />

The argon purges to <strong>the</strong> furnace base, shell, <strong>and</strong> sight<br />

port were set at appropriate levels (a total flow <strong>of</strong> 5 L/m<strong>in</strong>), <strong>and</strong> argon<br />

was allowed to flow to <strong>the</strong> preform at a rate <strong>of</strong> 500 cm3/m<strong>in</strong> through <strong>the</strong><br />

reactant gas supply l<strong>in</strong>es, subsequently flush<strong>in</strong>g <strong>the</strong>se l<strong>in</strong>es at <strong>the</strong><br />

same time. The furnace was <strong>the</strong>n heated to <strong>the</strong> specified deposition<br />

temperature <strong>and</strong> <strong>the</strong> system was allowed to degas for 30 m<strong>in</strong>.<br />

After <strong>the</strong>se prelim<strong>in</strong>ary procedures, <strong>the</strong> operation pressure <strong>of</strong> <strong>the</strong><br />

furnace was set on <strong>the</strong> <strong>control</strong>ler <strong>and</strong> reactants were directed <strong>in</strong>to <strong>the</strong><br />

reaction chamber. The system was allowed to stabilize <strong>and</strong> <strong>the</strong>n run at<br />

steady state for 2 hours.<br />

On completion, <strong>the</strong> reactant gases were<br />

replaced with argon gas flow <strong>and</strong> <strong>the</strong> furnace was cooled to room

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