Systems for producing silane
US-9011803-B2 · Apr 21, 2015 · US
US9487406B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9487406-B2 |
| Application number | US-201514622326-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 13, 2015 |
| Priority date | Dec 23, 2010 |
| Publication date | Nov 8, 2016 |
| Grant date | Nov 8, 2016 |
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Methods and systems for producing silane that use electrolysis to regenerate reactive components therein are disclosed. The methods and systems may be substantially closed-loop with respect to halogen, an alkali or alkaline earth metal and/or hydrogen.
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What is claimed is: 1. A system for producing silane in a substantially closed-loop process, the system comprising: a vessel for electrolyzing an alkali or alkaline earth metal halide salt to produce metallic alkali or alkaline earth metal and halogen gas; a halogenation reactor for producing at least one of (1) silicon tetrahalide, and (2) trihalosilane; by reacting silicon with at least one of: (1) halogen gas discharged from the vessel; and (2) hydrogen halide produced by contacting halogen gas discharged from the vessel with hydrogen; a disproportionation system for producing monohalosilane or dihalosilane from at least one of (1) silicon tetrahalide and (2) trihalosilane to produce a halogenated silicon feed gas consisting essentially of halosilanes; a hydride reactor for reacting metallic alkali or alkaline earth metal discharged from the vessel and hydrogen to produce an alkali or alkaline earth metal hydride; and a silane reactor for reacting the halogenated silicon feed gas with the alkali or alkaline earth metal hydride to produce silane and an alkali or alkaline earth metal halide salt. 2. The system as set forth in claim 1 wherein the vessel is an electrolysis cell. 3. The system as set forth in claim 1 wherein the halogenation reactor is a fluidized bed reactor in which silicon is suspended in a halogenated silicon feed gas comprising at least one halosilane selected from the group consisting of silicon tetrahalide, trihalosilane, dihalosilane and monohalosilane. 4. The system as set forth in claim 1 wherein the system comprises a polycrystalline silicon reactor for decomposing silane to produce hydrogen and polycrystalline silicon. 5. The system as set forth in claim 4 wherein the polycrystalline reactor comprises electrically heated rods for thermally decomposing silane. 6. The system as set forth in claim 4 wherein the polycrystalline reactor is a fluidized bed reactor in which silane fluidizes polycrystalline silicon particles. 7. The system as set forth in claim 4 wherein the system comprises a conveying apparatus for conveying hydrogen from the polycrystalline silicon reactor to the hydride reactor. 8. The system as set forth in claim 4 wherein the system comprises a conveying apparatus for conveying silane from the silane reactor to the polycrystalline silicon reactor.
Features relating to the reactants or products · CPC title
employing electric or magnetic energy · CPC title
employing electric or magnetic energy · CPC title
Monosilane · CPC title
Tetrachloride, trichlorosilane or silicochloroform, dichlorosilane, monochlorosilane or mixtures thereof · CPC title
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