Patent US4067954A successfully refreshed from Google Patents.
US4067954A
Expired / Lapsed
US
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Process for the production of finely divided silicon dioxide having a large specific surface
Assignee: Evonik Operations GmbH
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Filing: 1976-01-26
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Granted: 1978-01-10
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Expires: 1996-01-26
Abstract
Abstract Process for the production of finely divided silicon dioxide having a surface of more than about 380 m 2 /g BET which comprises converting a volatile silicon halide in an inert gas vehicle with a gas forming water upon combustion and oxygen gas or air in a flame, the quantity of oxygen being sufficient for the practically complete combustion of the combustible gas, and the quantities of oxygen or air and combustible gas being sufficient to produce a quantity of water which will at least suffice for the hydrolysis of the volatile silicon halide, said volatile silicon halide consisting essentially of trichlorosilane and said inert gas vehicle consisting for instance of nitrogen, carbon dioxide, noble gases or others the amount of trichlorosilane vapor being about 410-565 g trichlorosilane vapor per Nm 3 /h total gas, the molar ratio of trichlorosilane vapor to nitrogen being about 0.5:1 - 5:1, the molar ratio of hydrogen in the combustible gas to oxygen being about 0.5:1 - 1.3:1, and separating the resulting silicon dioxide from other reaction products. Finely divided silicon dioxide prepared according to this process is also provided. The finely divided silicon dioxide is useful as a thickening agent in liquid systems.
Inventors
- 👤 Axel Volling
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-07 15:01
CPC Classifications
C; C01; C01B; C01B33/00; C01B33/113; C01B33/12; C01B33/18; C01B33/181; C01B33/183; B; B82; B82Y; B82Y30/00; C01P; C01P2004/00; C01P2004/60; C01P2004/64; C01P2006/00; C01P2006/12; C01P2006/22
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
198 words
In a process for the production of finely divided silicon dioxide having a surface area of more than about 380 m 2 /g BET which comprises converting a volatile halogen-containing inorganic silicon compound in an inert gas vehicle with a hydrogen-containing gas capable of forming water upon combustion and oxygen gas or air in a flame, whereby the quantity of oxygen is sufficient for the complete combustion of the water-forming gas, and whereby the quantities of oxygen or air and water-forming gas are sufficient to produce a quantity of water which will at least suffice for the hydrolysis of the silicon compound, said inert gas vehicle selected from the group consisting of nitrogen, carbon dioxide or noble gases, the improvement wherein said inorganic silicon compound is trichlorosilane vapor in an amount of about 410-565 g trichlorosilane vapor per Nm 3 /hr total gas the molar ratio of trichlorosilane vapor to inert gas vehicle being about 0.5:1-5:1, the molar ratio of hydrogen in the combustible gas to the oxygen being about 0.5 : 1 - 1.3 : 1, and separating the resulting silicone dioxide from other reaction products, said silicone dioxide having an enhanced thickening effect in organic media.
Claim 2
Dependent Claim
198 words
In a process for the production of finely divided silicon dioxide having a surface area of more than about 380 m 2 /g BET which comprises converting a volatile halogen-containing inorganic silicon compound in an inert gas vehicle with a hydrogen-containing gas capable of forming water upon combustion and oxygen gas or air in a flame, whereby the quantity of oxygen is sufficient for the complete combustion of the water-forming gas, and whereby the quantities of oxygen or air and water-forming gas are sufficient to produce a quantity of water which will at least suffice for the hydrolysis of the silicon compound, said inert gas vehicle selected from the group consisting of nitrogen, carbon dioxide or noble gases, the improvement wherein said inorganic silicon compound is trichlorosilane vapor in an amount of about 410-565 g trichlorosilane vapor per Nm 3 /hr total gas the molar ratio of trichlorosilane vapor to inert gas vehicle being about 0.5:1-5:1, the molar ratio of hydrogen in the combustible gas to the oxygen being about 0.5 : 1 - 1.3 : 1, and separating the resulting silicone dioxide from other reaction products, said silicone dioxide having an enhanced thickening effect in organic media.
Claim 3
Dependent Claim
53 words
Process according to claim 1 in which the silicon dioxide has a specific surface of about 380-650 m 2 /g BET, an average primary particle size of about 5-7 millimicrons, a bulk weight of about 20-120 g/l, a bulking volume of about 1,000-2,000 ml/100g, and a silanol group density of about 80-85 A/SiOH.
Claim 4
Dependent Claim
32 words
Process according to claim 2 wherein said silicon dioxide is capable of yielding a pH of about 3.4 to about 4.4 in about 5% by weight aqueous suspension of said silicon dioxide.
Claim 5
Dependent Claim
19 words
Process according to claim 3 in which the BET surface is about 480 to about 600 m 2 /g.
Claim 6
Dependent Claim
21 words
Process according to claim 2 wherein said silicon dioxide has a particle size distribution of about 2.5 to about 9.5 millimicrons.
Claim 7
Dependent Claim
16 words
Process according to claim 1 in which the BET surface is about 400-650 m 2 /g.
Claim 8
Dependent Claim
14 words
Process according to claim 1 in which the hydrogen-containing gas is hydrogen or methane.
Claim 9
Dependent Claim
33 words
Process according to claim 1 in which the molar ratio of hydrogen in the combustible gas to oxygen gas or oxygen in the air is about 0.8 : 1 - 1.0 : 1.
Claim 10
Dependent Claim
22 words
Process according to claim 1 in which the amount of trichlorosilane vapor is about 450-500 g trichlorosilane vapor per Nm 3 /hr.
Claim 11
Dependent Claim
16 words
Process according to claim 1 in which the BET surface is about 480-600 m 2 /g.
Claim 12
Dependent Claim
19 words
Process according to claim 1 in which the silicon dioxide is separated from combustion gases in a centrifugal separator.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-01-09 | 1981-07-11 | 1982-01-10 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-01-09 | 1985-07-11 | 1986-01-10 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-01-09 | 1989-07-11 | 1990-01-10 | $7700.00 | Window Closed / Lapsed |