US4036938A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Production of high purity hydrogen fluoride from silicon tetrafluoride
Assignee: Individual
•
Filing: 1976-10-07
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Granted: 1977-07-19
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Expires: 1996-10-07
Abstract
Abstract Method and apparatus for the production of high purity hydrogen fluoride by the flame hydrolysis of silicon tetrafluoride and the deliberate cooling of the silicon dioxide and hydrogen fluoride reaction products without appreciable dilution to promote agglomeration of the silicon dioxide and permit separation of the hydrogen fluoride with substantially no contamination.
Inventors
- 👤 Richard S. Reed
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 00:18
CPC Classifications
C; C01; C01B; C01B7/00; C01B7/19; C01B7/191; C01B7/193; C01B33/00; C01B33/113; C01B33/12; C01B33/18; C01B33/181; C01B33/183; C01B33/184
Claims Analysis
Total Claims: 18
Claim 1
Independent Claim
131 words
The method of producing commercial grade hydrogen fluoride comprising the steps of (a) forming a mixture of silicon tetrafluoride and water vapor; (b) flame hydrolysing the silicon tetrafluoride at a temperature in the range from about 2100° F. to above about 3000° F. with a ratio of available water to stochiometric water for flame hydrolysis in the range from above about 1:1 to about 14:1 to convert at least 95% of the silicon tetrafluoride to hydrogen fluoride and silicon dioxide particles with diameters in excess of about 100 millimicrons; (c) cooling the reaction products of the flame hydrolysis by more than 500° F. with negligible dilution; (d) agglomerating the silicon dioxide particles and removing them from the reaction products; and (e) recovering hydrogen fluoride with a purity in excess of 95%.
Claim 2
Independent Claim
131 words
The method of producing commercial grade hydrogen fluoride comprising the steps of (a) forming a mixture of silicon tetrafluoride and water vapor; (b) flame hydrolysing the silicon tetrafluoride at a temperature in the range from about 2100° F. to above about 3000° F. with a ratio of available water to stochiometric water for flame hydrolysis in the range from above about 1:1 to about 14:1 to convert at least 95% of the silicon tetrafluoride to hydrogen fluoride and silicon dioxide particles with diameters in excess of about 100 millimicrons; (c) cooling the reaction products of the flame hydrolysis by more than 500° F. with negligible dilution; (d) agglomerating the silicon dioxide particles and removing them from the reaction products; and (e) recovering hydrogen fluoride with a purity in excess of 95%.
Claim 3
Dependent Claim
22 words
The method of claim 1 wherein the reaction products are cooled to within the range from about 400° to about 1500° F.
Claim 4
Dependent Claim
15 words
The method of claim 1 wherein the reaction products are cooled to below 1100° F.
Claim 5
Dependent Claim
21 words
The method of claim 1 wherein the flame hydrolysis temperature is in the range from about 2200° to about 2900° F.
Claim 6
Dependent Claim
21 words
The method of claim 1 wherein the flame hydrolysis temperature is in the range from about 2200° to about 2600° F.
Claim 7
Dependent Claim
30 words
The method of claim 1 wherein the ratio of the available water to the stochiometric water for the flame hydrolysis is in the ratio from about 2:1 to about 7:1.
Claim 8
Dependent Claim
19 words
The method of claim 1 wherein the ratio of the available water to the stochiometric water is about 3.
Claim 9
Dependent Claim
22 words
The method of claim 1 wherein the mixture of silicon tetrafluorine and water vapor is formed from distilled or dehydrated fluosilicic acid.
Claim 10
Dependent Claim
13 words
The method of claim 1 wherein the hydrogen fluoride is recovered by concentration.
Claim 11
Independent Claim
138 words
The method of producing commercial grade hydrogen fluoride comprising the steps of (a) forming a mixture of silicon tetrafluoride and water vapor; (b) flame hydrolysing the silicon tetrafluoride at a temperature in the range from about 1800° F. to about 3000° F. with a ratio of available water to stochiometric water for flame hydrolysis in the range from about 2:1 to about 14:1 to convert at least 95% of the silicon tetrafluoride to hydrogen fluoride and silicon dioxide particles with diameters in excess of about 100 millimicrons; (c) cooling the reaction products of the flame hydrolysis to a temperature within the range from about 400° F. to about 1500° F. with negligible dilution (d) agglomerating the silicon dioxide particles and removing them from the reaction products; and (e) recovering hydrogen fluoride with a purity in excess of 95%.
Claim 12
Independent Claim
138 words
The method of producing commercial grade hydrogen fluoride comprising the steps of (a) forming a mixture of silicon tetrafluoride and water vapor; (b) flame hydrolysing the silicon tetrafluoride at a temperature in the range from about 1800° F. to about 3000° F. with a ratio of available water to stochiometric water for flame hydrolysis in the range from about 2:1 to about 14:1 to convert at least 95% of the silicon tetrafluoride to hydrogen fluoride and silicon dioxide particles with diameters in excess of about 100 millimicrons; (c) cooling the reaction products of the flame hydrolysis to a temperature within the range from about 400° F. to about 1500° F. with negligible dilution (d) agglomerating the silicon dioxide particles and removing them from the reaction products; and (e) recovering hydrogen fluoride with a purity in excess of 95%.
Claim 13
Independent Claim
148 words
The method of producing commercial grade hydrogen fluoride comprising the steps of (a) forming a mixture of silicon tetrafluoride and water vapor; (b) flame hydrolysing the silicon tetrafluoride at a temperature in the range from about 2000° F. to about 3000° F. with a ratio of available water to stochiometric water for flame hydrolysis in the range from about 2:1 to about 14:1 to convert at least 95% of the silicon tetrafluoride to hydrogen fluoride and silicon dioxide particles with diameters in excess of about 100 millimicrons; (c) cooling the reaction products of the flame hydrolysis to a temperature within the range from about 400° F. to about 1500° F. with negligible dilution, and without allowing the conversion rate to fall below 95%; (d) agglomerating the silicon dioxide particles and removing them from the reaction products; and (e) recovering hydrogen fluoride with a purity in excess of 95%.
Claim 14
Independent Claim
148 words
The method of producing commercial grade hydrogen fluoride comprising the steps of (a) forming a mixture of silicon tetrafluoride and water vapor; (b) flame hydrolysing the silicon tetrafluoride at a temperature in the range from about 2000° F. to about 3000° F. with a ratio of available water to stochiometric water for flame hydrolysis in the range from about 2:1 to about 14:1 to convert at least 95% of the silicon tetrafluoride to hydrogen fluoride and silicon dioxide particles with diameters in excess of about 100 millimicrons; (c) cooling the reaction products of the flame hydrolysis to a temperature within the range from about 400° F. to about 1500° F. with negligible dilution, and without allowing the conversion rate to fall below 95%; (d) agglomerating the silicon dioxide particles and removing them from the reaction products; and (e) recovering hydrogen fluoride with a purity in excess of 95%.
Claim 15
Independent Claim
127 words
The method of producing commercial grade hydrogen fluoride comprising the steps of (a) forming a mixture of silicon tetrafluoride and water vapor; (b) flame hydrolysing the silicon tetrafluoride at a temperature in the range from about 2000° F. and above, with a ratio of available water to stochiometric water for flame hydrolysis in the range from about 2:1 and above, to convert at least 95% of the silicon tetrafluoride to hydrogen fluoride and silicon dioxide particles with approximate diameters in excess of about 100 millimicrons; (c) cooling the reaction products of the flame hydrolysis to below 1500° F. with negligible dilution; (d) agglomerating the silicon dioxide particles and removing them from the reaction products; and (e) recovering the hydrogen fluoride with a purity in excess of 95%.
Claim 16
Independent Claim
127 words
The method of producing commercial grade hydrogen fluoride comprising the steps of (a) forming a mixture of silicon tetrafluoride and water vapor; (b) flame hydrolysing the silicon tetrafluoride at a temperature in the range from about 2000° F. and above, with a ratio of available water to stochiometric water for flame hydrolysis in the range from about 2:1 and above, to convert at least 95% of the silicon tetrafluoride to hydrogen fluoride and silicon dioxide particles with approximate diameters in excess of about 100 millimicrons; (c) cooling the reaction products of the flame hydrolysis to below 1500° F. with negligible dilution; (d) agglomerating the silicon dioxide particles and removing them from the reaction products; and (e) recovering the hydrogen fluoride with a purity in excess of 95%.
Claim 17
Independent Claim
127 words
The method of producing commercial grade hydrogen fluoride comprising the steps of (a) forming a mixture of silicon tetrafluoride and water vapor; (b) flame hydrolysing the silicon tetrafluoride at a temperature in the range from about 1800° F. to about 3000° F. with a ratio of available water to stochiometric water in the range from about 2:1 to about 14:1 to convert at least 99% of the silicon tetrafluoride to hydrogen fluoride and silicon dioxide particles with approximate diameters in excess of about 200 millimicrons; (c) cooling the reaction products of the flame hydrolysis by more than 500° F. with negligible dilution; (d) agglomerating the silicon dioxide particles and removing them from the reaction products; and (e) recovering hydrogen fluoride with a purity in excess of 99%.
Claim 18
Independent Claim
127 words
The method of producing commercial grade hydrogen fluoride comprising the steps of (a) forming a mixture of silicon tetrafluoride and water vapor; (b) flame hydrolysing the silicon tetrafluoride at a temperature in the range from about 1800° F. to about 3000° F. with a ratio of available water to stochiometric water in the range from about 2:1 to about 14:1 to convert at least 99% of the silicon tetrafluoride to hydrogen fluoride and silicon dioxide particles with approximate diameters in excess of about 200 millimicrons; (c) cooling the reaction products of the flame hydrolysis by more than 500° F. with negligible dilution; (d) agglomerating the silicon dioxide particles and removing them from the reaction products; and (e) recovering hydrogen fluoride with a purity in excess of 99%.
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) | 1980-07-18 | 1981-01-17 | 1981-07-19 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-07-18 | 1985-01-17 | 1985-07-19 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-07-18 | 1989-01-17 | 1989-07-19 | $7700.00 | Window Closed / Lapsed |