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

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73<br />

fur<strong>the</strong>r protection.<br />

A 6.5-cm-diam by 10-cm-long graphite spacer can be<br />

placed between <strong>the</strong> graphite holder <strong>and</strong> <strong>the</strong> water-cooled <strong>in</strong>jector to<br />

provide a uniform iso<strong>the</strong>rmal hot zone across t<strong>in</strong>e preform.<br />

9.2 Instrumentation<br />

A schematic <strong>of</strong> <strong>the</strong> <strong>in</strong>filtration system is given <strong>in</strong> Figure 9.3. The<br />

<strong>control</strong> systems have been automated to allow for unattended operation <strong>and</strong><br />

to elim<strong>in</strong>ate daily cycl<strong>in</strong>g. The furnace operakes on ei<strong>the</strong>r a time- or<br />

pressure-<strong>control</strong> circuit. A photograph <strong>of</strong> <strong>the</strong> system is given In<br />

Figure 9.4.<br />

The correctxtd optical temperature at <strong>the</strong> top surface <strong>of</strong> <strong>the</strong> speci.nien<br />

is measured <strong>and</strong> <strong>control</strong>led by a s<strong>in</strong>gle-wavelength automatic optical<br />

*<br />

pyrometer equi.pped with a time-proportion<strong>in</strong>g power <strong>control</strong>ler. The<br />

operat<strong>in</strong>g temperature must be measured directly from <strong>the</strong> top surface <strong>of</strong>:<br />

<strong>the</strong> specimen. As <strong>in</strong>filtration proceeds, t:ht? density <strong>and</strong> <strong>the</strong>rmal conducti-vity<br />

<strong>of</strong> <strong>the</strong> specimen <strong>in</strong>crease <strong>and</strong> <strong>the</strong> heat flow through <strong>the</strong><br />

<strong>in</strong>filtrat<strong>in</strong>g composi.te <strong>in</strong>creases. More heat is requi.red to ma<strong>in</strong>ta<strong>in</strong><br />

<strong>the</strong> proper temperature <strong>and</strong> <strong>the</strong>rmal gradient for deposition to cont<strong>in</strong>ue.<br />

This is demonstrzted by a steady <strong>in</strong>crease <strong>in</strong> voltage <strong>and</strong> current be<strong>in</strong>g<br />

suppl-ied to <strong>the</strong> furnace as densification proceeds, In <strong>the</strong> past, a<br />

<strong>the</strong>rmocouple placed <strong>in</strong> contact with <strong>the</strong> outs icle surface <strong>of</strong> <strong>the</strong> coati.ng<br />

chnmlici: at <strong>the</strong> level <strong>of</strong> <strong>the</strong> specimen did not al.J.ow<br />

for (.his change.<br />

Furnace power levels were held constant <strong>and</strong> <strong>the</strong> top surface temperature<br />

*<br />

IRCON, Inc., Niles, Ill<strong>in</strong>ois

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