Method for preparing organochlorosilanes
US-2022242887-A1 · Aug 4, 2022 · US
US9422316B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9422316-B2 |
| Application number | US-201314436095-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 2, 2013 |
| Priority date | Oct 16, 2012 |
| Publication date | Aug 23, 2016 |
| Grant date | Aug 23, 2016 |
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A method comprises separate and consecutive steps (i) and (ii). Step (i) includes contacting a copper catalyst with hydrogen gas and a halogenated silane monomer at a temperature of 500° C. to 1400° C. to form a silicon-containing copper catalyst comprising at least 0.1% (w/w) of silicon. Step (ii) includes contacting the silicon-containing copper catalyst with an organohalide at a temperature of 100° C. to 600° C. to form a reaction product. The organohalide has formula H a C b X c , where X is a halogen atom, subscript a is an integer of 0 or more, subscript b is an integer of 1 or more, and subscript c is an integer of 2 or more. The method produces a reaction product. The reaction product includes a halogenated silahydrocarbylene.
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The invention claimed is: 1. A method comprises separate and consecutive steps (i) and (ii), where Step (i) comprises contacting a copper catalyst with hydrogen gas and a halogenated silane monomer at a temperature of 500° C. to 1400° C. to form a silicon-containing copper catalyst comprising at least 0.1% (w/w) of silicon; and Step (ii) comprises contacting the silicon-containing copper catalyst with an organohalide at a temperature of 100° C. to 600° C. to form a reaction product comprising a halogenated silahydrocarbylene, where the organohalide has formula H a C b X c , where X is a halogen atom, subscript a is an integer of 0 or more, subscript b is an integer of 1 or more, and subscript c is an integer of 2 or more. 2. The method of claim 1 , where the copper catalyst further comprises at least one element selected from calcium, cesium, gold, magnesium, nickel, sulfur, tin, and zinc. 3. The method of claim 1 , where the halogenated silane monomer comprises a monomer selected from a silicon tetrahalide, a trihalosilane, and a combination thereof. 4. The method of claim 1 , further comprising a third step (iii) in which the separate and consecutive first step (i) and second step (ii) are repeated one or more times. 5. The method of claim 1 , further comprising purging the silicon-containing copper catalyst formed in step (i) with at least one of hydrogen gas and an inert gas before contacting the silicon-containing copper catalyst with the organohalide in step (ii). 6. The method of claim 5 , where the silicon-containing copper catalyst is first purged with hydrogen gas and then subsequently purged with an inert gas. 7. The method of claim 1 , where the copper catalyst further comprises a metal oxide or carbon-based support. 8. The method of claim 1 , where the copper catalyst comprises copper, gold, and magnesium. 9. The method of claim 1 , where a mole ratio of hydrogen gas to halogenated silane monomer is from 15:1 to 1:1. 10. The method of claim 1 , where the organohalide is selected from: 1) an alkyl halide where subscript b is 1 to 10, and 2) a cycloalkyl halide where subscript b is 4 to 10. 11. The method of claim 10 , where the organohalide is an alkyl halide, subscript b is 1, subscript c is 2, 3, or 4, and each X is Cl. 12. The method of claim 1 , where the halogenated silahydrocarbylene has formula X d H e R 1 f Si—R—SiX d H e R 1 f , where each X is independently a halogen atom; each subscript d is independently 0, 1, 2, or 3, with the proviso that at least one instance of d>0; each subscript e is independently 0, 1, or 2; each subscript f is independently 0, 1, or 2; with the proviso that a quantity (d+e+f)=3, each R 1 is independently a monovalent hydrocarbon group, and R is a divalent hydrocarbon group. 13. The method of claim 1 further comprising the step of recovering the halogenated silahydrocarbylene. 14. The method of claim 1 , where the temperature at which the reactants in step (i) contact the copper catalyst is 500° C. to 950° C. 15. The method of claim 1 , where the method further comprises step (iv): forming a resin from the halogenated silahydrocarbylene.
by reactions involving both Si-C and Si-halogen linkages, the Si-C and Si-halogen linkages can be to the same or to different Si atoms, e.g. redistribution reactions · CPC title
Preparation thereof from silicon and halogenated hydrocarbons {direct synthesis} · CPC title
in which all the silicon atoms are connected by linkages other than oxygen atoms · CPC title
by reactions involving the formation of Si-C linkages (hydrosilylation reactions C07F7/14; direct synthesis C07F7/16) · CPC title
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