FTrPSA recovery and reutilization method of chlorine-based SiC-CVD epitaxial process tail gas generated by reaction of ethylene and silane
A technology of silane and ethylene, which is applied in SiC-CVD epitaxy process exhaust gas treatment, semiconductor materials and semiconductor process environmental protection fields, can solve the problems of high production cost of silane/chlorosilane and ethylene, achieve stable recycling and reuse process, and reduce exhaust emissions , Improve the effect of recycling efficiency
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Embodiment 1
[0065] Such as figure 1 As shown, the chlorine-based SiC-CVD epitaxial process tail gas FTrPSA recovery and recycling method of ethylene and silane reaction includes the following steps:
[0066] Step 1, raw material gas pretreatment, successively remove dust, particles, oil mist, part of high chlorinated silane, high chlorinated alkanes and high hydrocarbon impurities; raw material gas, with ethylene (C 2 h 4 ) as the main carbon (C) source, with silane (SiH 4 ) is the silicon (Si) source and hydrogen chloride (HCl) is added for chemical vapor deposition (CVD) to prepare the exhaust gas in the chlorine-based epitaxial growth process based on silicon carbide (SiC), and its main composition is hydrogen (H 2 ), HCl, C 2 h 4 , Silane (SiH 4 ) / chlorosilane (SiHmCln), a small amount of methane (CH 4 ), chloroalkanes (CHmCln), chloroalkenes (VCM), and trace amounts of carbon monoxide (CO), carbon dioxide (CO 2 ), ethane and light hydrocarbon components above carbon two and hi...
Embodiment 2
[0079] Such as figure 2 As shown, on the basis of Example 1, under the condition that the concentration of HCl and chlorosilane / chloroalkene contained in the purified raw gas is relatively high, for example, the concentration of chlorine is greater than 3-6%, and the shallow cooling chlorosilane absorption process is added twice. Medium-temperature chlorosilane absorption process, that is, the non-condensable gas 1 from the shallow-cold chlorosilane absorption process is compressed, condensed, and gas-liquid separated, and the formed non-condensable gas 1' is pressurized to 0.6-0.8 MPa, and cooled and heated After being exchanged to 60-120°C, it enters from the bottom of the absorption tower of the additional secondary medium-temperature chlorosilane absorption process, and uses a mixed liquid containing chlorosilane / HCl as the absorbent to spray down from the top of the secondary medium-temperature chlorosilane absorption tower. The condensed gas 1' performs reverse mass tra...
Embodiment 3
[0081] Such as image 3 As shown, on the basis of Examples 1 and 2, the non-condensable gas 2 / 2' formed after compression, condensation and gas-liquid separation from the shallow cold chlorosilane absorption process or the second medium temperature chlorosilane absorption process is blown The pressurization method enters the shallow cold pressure swing adsorption concentration process composed of the two-stage PSA system, that is, the non-condensable gas 2 is pressurized to 0.2-0.3MPa, enters from the bottom of the first PSA adsorption tower (1-stage PSA), and enters from the bottom of the first PSA adsorption tower (1-stage PSA). The non-adsorbed gas flowing out from the top of the first-stage PSA tower is hydrogen-rich gas, which enters the next process, that is, adsorption purification; into the bottom of the second PSA adsorption tower (2-stage PSA), and the enriched non-adsorbed phase hydrogen-rich mixed intermediate gas flows out from the top of the 2-stage PSA tower, an...
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