Fluorine-based SiC-CVD crystal and film growth process tail gas FTrPSA all-component recycling method
A thin-film growth and full-component technology, applied in chemical instruments and methods, hydrogen fluoride, fluorine/hydrogen fluoride, etc., can solve the problems of high preparation cost, high cost, and inability to recycle and reuse, so as to realize recycling and reduce tail gas The effect of emissions
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Embodiment 1
[0040] Such as figure 1 Shown, a kind of fluorine-based SiC-CVD crystal and thin film growth process tail gas FTrPSA full component recovery and reuse method, feed gas with ethylene (C 2 h 4 ) as the main carbon (C) source, silicon tetrafluoride (SiF 4 ) is the silicon (Si) source, and adding hydrogen fluoride (HF) mainly a small amount of hydrogen chloride (HCl) and hydrogen (H 2 ) as the carrier gas, carry out chemical vapor deposition (CVD) on the substrate based on silicon carbide (SiC) to prepare the tail gas of the fluorine-based SiC-CVD thin film growth process of SiC thin film epitaxial wafers, wherein, in addition to a large amount of H 2 In addition, the main active ingredient is C 2 h 4 、SiF 4 , HF, HCl, and a small amount of methane (CH 4 ), SiH 4 , chlorosilanes, fluoroalkanes (CH m f n ), and trace amounts of carbon monoxide (CO), carbon dioxide (CO 2 ), water (H 2 O) and silicon dioxide (SiO 2 ), Si / C fine particles, normal pressure and temperature. ...
Embodiment 2
[0052] Such as figure 2 Shown, on the basis of embodiment 1, contain the ethylene of higher concentration (C 2 h 4 ) working conditions, the purified raw gas first enters the shallow cold oil absorption process, and the non-condensable gas 1 flowing out from it enters the medium-temperature pressure swing adsorption concentration process to form the intermediate gas of the non-adsorption phase, and the non-condensable gas 2 formed after condensation After entering the tail gas absorption process, the crude SiF formed after condensation 4 The liquid enters the HF rectification process, and the concentrated gas of the adsorption phase formed in the medium temperature and pressure swing adsorption concentration process enters the chlorosilane spray absorption process, and the non-condensable gas 3 flowing out from it returns to the shallow cooling oil absorption process for further recovery and effective Components, the absorption liquid flowing out from it, enters into multi-...
Embodiment 3
[0054] Such as image 3 Shown, on the basis of embodiment 1, purifying SiF in raw gas 4 / HF concentration is high and the chloride concentration including HCl / chlorosilane is less than 1%, the purified raw gas first enters the medium temperature pressure swing adsorption concentration process, and the formed concentrated gas enters the new condensation after cooling and pressurization The non-condensable gas 1 formed thus enters the shallow cold oil absorption process, and the non-condensable gas 2 formed therefrom is mixed with the intermediate gas from the medium temperature pressure swing adsorption process and enters the tail gas absorption process, and then enters the tail gas absorption process from the medium temperature pressure swing adsorption concentration process The outflowing intermediate gas in the non-adsorption phase enters the tail gas absorption process for treatment, and the concentrated gas formed from the medium temperature pressure swing adsorption conce...
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