1993
DOI: 10.1111/j.1151-2916.1993.tb03688.x
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Model for the Formation of Silicon Carbide from the Pyrolysis of Dichlorodimethylsilane in Hydrogen: II, Silicon Carbide Formation from Silicon and Methane

Abstract: A model is developed for the deposition of silicon carbide from the pyrolysis of dichlorodimethylsiane in hydrogen, in a tubular reactor at temperatures from 700° to 1100°C and 1.013 × 105 Pa (1 atm) pressure. Concentration of dichlorodimethylsilane varied from 2 to 8 vol%. Gas chromatography was used to determine the volatile products of reaction, and gravimetric analysis was used to determine the total silicon and silicon carbide deposition on the tube. The model developed based on the experimental data that… Show more

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Cited by 18 publications
(11 citation statements)
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“…A fraction of hydrogen is flowing through a saturator (2) for the uptake of MTS. This flow and that of pure hydrogen are mixed in a mixing chamber (3). After flowing through the reactor (4), the product stream passes a cold trap (7), held at a temperature of ±20 C, an absorption column (8) filled with a 1:1 mixture of isopropanol and glycol, another absorption column filled with a solution of NaOH (9), and a drying column filled with CaCl 2 (10).…”
Section: Methodsmentioning
confidence: 99%
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“…A fraction of hydrogen is flowing through a saturator (2) for the uptake of MTS. This flow and that of pure hydrogen are mixed in a mixing chamber (3). After flowing through the reactor (4), the product stream passes a cold trap (7), held at a temperature of ±20 C, an absorption column (8) filled with a 1:1 mixture of isopropanol and glycol, another absorption column filled with a solution of NaOH (9), and a drying column filled with CaCl 2 (10).…”
Section: Methodsmentioning
confidence: 99%
“…[1,2] Deposition rate, gas phase composition as well as composition and structure of the deposit were determined in a single study. [3] Deposition rates have been studied using a thermobalance [8,9,12,13,34,35] or a flow reactor. [1±5,7,19,29,36] In both cases hot-wall [1±5,7±9,12,13,19,29,34,36] or cold-wall reactors [21] were used.…”
Section: Introductionmentioning
confidence: 99%
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“…Fig.7(e) shows that there is a little of HCl in the gas phase during the pyrolysis of MTS below 950 . During ℃ the consecutive reaction process, the increase of the concentration of HCl with the temperature trends to be more rapid above 950 because of the reactions of ℃ SiHCl 3 , SiCl 4 and CH 4 produced in the gas phase during the dissociation of MTS, as the following reactions (7) and (8): SiHCl 3 →SiCl 2 ••+HCl (7) SiCl 2 ••+CH 4 →ClSiCH 3 ••+HCl (8) It is obvious that the concentration of HCl at n(H 2 )/n(MTS)=8 is higher than that at n(H 2 )/n(MTS)=4, which can be explained by reaction (6). When the amount of H 2 is increased, reaction (6) is promoted, which results in large amount of HCl in the gas phase.…”
Section: Gas Phase Compositionmentioning
confidence: 99%