chemical physics of discharges - Argonne National Laboratory
chemical physics of discharges - Argonne National Laboratory chemical physics of discharges - Argonne National Laboratory
H2 --1 DE-OXO DRYING TOWER TAKE-UP REEL CHEMICAL CLEANING TRAIX COLD TRAPS Fig. 9 Schematic of Continuous System for Plating in a Corona Discharge Fig. 10 Boron Deposit on 0.15-mil Tungsten Wire, Continuous System (600~) i
199 a red heat in this cell using dc power. Tests performed in this system have utilized both 0.5-mil and 0.15-mil tungsten substrate. Results 11) AC Pickup. The use of shielded leads and wire cages around the transformers has, with the use of 1,000 ohm current measuring resistors, virtually eliminatyd the ac pickup. j2) Dcposition on 0.5-mil Tungsten IVire. Satisfactory results have been obtained at a hydrogen flow rate through the bubbler of about 100 cc/min and additional hydrogen at a flow rate of about 350 cc/min. Hydrogen is flowing through the cleaning cell at about 140 cc/ min and the wire is cleaned by resistance heating at a dc voltage of about 70 V and a DC current of about 320 milliamperes. Some of the results obtained are indicated in Table 6. Using only one cell, at a filament speed of about 3.6 in. /min a coating about 0.25-mil thick was obtained; at a filament speed of about 14.4 in./min, a coating ab-out 0.05-mil thick was obtained. Using two cells, there was some problem in maintaining the corona in the second cell. At a filament speed of about 3,6 in. /min a coating about 0.7-mil thick was obtained in the areas where a good corona was maintained. At a filament speed of about 14.4 in./min and a current input to the second cell of about half that to the first cell, a coating about 0.07-mil thick was obtained. 13) Deposition on 0.15-mil Tungsten Wire. The 0.15-mil tungsten substrate wire was cleaned ' by the hot-wire technique at hydrogen flow rate of about 140 cc/min and at a dc power input of about 208 V and 90 mA. While the input vapors were split between the three plating cells, only one cell was utilized for plating studies. Some of the results are indicated in Table 7. The best results were obtained at a filament speed of about 5 in./min with a hydrogen flow rate through the bubbler of about 70 cc/min, and additional hydrogen at a flow rate of about 350 cc/min. To maintain a uniform corona, it was necessary to switch the power on and off relatively slowly during the run. Under these conditions a coating thickness of about 0.17 mil was obtained. There is apparently some difference in either the morphology of the 0.15-mil substrate as compared to the 0.5-mil material, or less effect by this substrate upon the morphology of the deposit. Although the morphology of the material deposited on 0.5-mil tungsten appeared similar to that indicated in Fig. 5, the morphology of the deposit on the 0.15-mil tungsten appeared more like that indicated in Fig. 4. Figure 10 indicates the morphology usually obtained 0.15-mil tungsten substrate. The total diameter of this sample is 0.4 mil. Discussion An apparatus has been presented, and tests performed, indicating the feasibility of depositing boron on a continuously moving substrate in a corona discharge. Although no tests were made for verification, the results obtained with the 0.15-mil sub- strate indicate that the substrate diameter also effects the operating conditions, probably though buildup of the positive ion sheath to such an extent that the corona cannot recover after being quenched. This effect is possibly related to the similar effect of high flowrates on larger substrates noted in the previous section. The effects might be explained by postu- lating a higher concentration of boron radicals around the smaller substrate simply through volume considerations, and around the larger substrate through an increased concentration resulting from increased availability due to higher flowrates. The charged species would tend to remain in the volume near the substrate because of the greater effects of the elec- trical field.
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H2 --1<br />
DE-OXO DRYING<br />
TOWER<br />
TAKE-UP REEL<br />
CHEMICAL<br />
CLEANING TRAIX<br />
COLD TRAPS<br />
Fig. 9 Schematic <strong>of</strong> Continuous System for Plating in a Corona Discharge<br />
Fig. 10 Boron Deposit on 0.15-mil Tungsten Wire,<br />
Continuous System (600~)<br />
i