US4042667A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method of cleaning waste gas containing a fluorine component
Assignee: Asahi Fiber Glass Co Ltd
•
Filing: 1975-04-17
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Granted: 1977-08-16
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Expires: 1995-04-17
Abstract
Abstract In a method of cleaning a fluorine-containing waste gas evolved frm a furnace, by contacting said gas with a fluorine-reactive powder and filtering the fluorine-reactive powder by a filter, an improvement comprising cooling the waste gas to 150 DEG -400 DEG C; feeding a fluorine-reactive powder into the cooled waste gas; passing the cooled waste gas through a filter on which the fluorine-reactive powder is deposited so as to react with the fluorine component of the waste gas; and removing the deposited powder layer from the filter.
Inventors
- 👤 Shosuke Ishiwata
- 👤 Kaoru Ozaki
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-26 07:33
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/68
Claims Analysis
Total Claims: 31
Claim 1
Independent Claim
89 words
In a method of cleaning a fluorine-containing waste gas evolved from a furnace, by contacting said gas with a fluorine-reactive powder and filtering the fluorine-reactive powder by a filter, an improvement which comprises cooling the waste gas to 150°-400° C with a water spray; feeding a fluorine-reactive powder into the cooled waste gas; passing the cooled waste gas through a filter on which the fluorine-reactive powder is deposited so as to react with the fluorine component of the waste gas; and removing the deposited powder layer from the filter.
Claim 2
Dependent Claim
89 words
In a method of cleaning a fluorine-containing waste gas evolved from a furnace, by contacting said gas with a fluorine-reactive powder and filtering the fluorine-reactive powder by a filter, an improvement which comprises cooling the waste gas to 150°-400° C with a water spray; feeding a fluorine-reactive powder into the cooled waste gas; passing the cooled waste gas through a filter on which the fluorine-reactive powder is deposited so as to react with the fluorine component of the waste gas; and removing the deposited powder layer from the filter.
Claim 3
Dependent Claim
33 words
The method of claim 1, wherein the fluorine-reactive powder is a fluorine-reactive calcium compound applied in a molar ratio of 1.5-10 relative to the amount of the fluorine component in the waste gas.
Claim 4
Dependent Claim
23 words
The method of claim 1, wherein the cooled waste gas is passed through a filter on which the fluorine-reactive powder is already deposited.
Claim 5
Dependent Claim
49 words
The method of claim 1, wherein a plurality of filters is used and wherein fluorine-reactive powder is pre-deposited onto the filters with air and wherein the waste gas is continually passed through all except one filter during the time the reacted powder layer is removed from the one filter.
Claim 6
Dependent Claim
27 words
The method of claim 1, wherein the deposited powder layer is removed such that a residual layer having an average thickness of more than 5 mm remains.
Claim 7
Dependent Claim
18 words
The method of claim 1, wherein the deposited powder layer on the filter is removed by applying back-pressure.
Claim 8
Dependent Claim
38 words
The method of claim 1, wherein a part of the deposited powder layer having a thickness of less than 5 mm is removed while a residual deposited powder layer having a thickness of more than 5 mm remains.
Claim 9
Dependent Claim
16 words
The method of claim 1, wherein the filter is a bag filter made of glass fiber.
Claim 10
Dependent Claim
16 words
The method of claim 1, wherein waste gas evolved from a glass melting furnace is treated.
Claim 11
Dependent Claim
34 words
The method of claim 9, wherein waste gas evolved from a glass melting furnace is treated and the powder material removed from the filter is recycled as a raw material for the glass production.
Claim 12
Dependent Claim
16 words
The method of claim 1, wherein the filter is preheated to 150° C before the filtration.
Claim 13
Dependent Claim
16 words
The method of claim 1, wherein fluorine-reactive powder is deposited on the filter before the filtration.
Claim 14
Dependent Claim
98 words
In a method of cleaning a fluorine-containing waste gas evolved from a furnace, by contacting it with a fluorine-reactive powder and filtering the fluorine-reactive powder by a filter, an improvement which comprises cooling the waste gas to 150°-400° C by a water spray; feeding into the cooled waste gas an active calcium compound powder at a molar ratio of 1.5 - 10 relative to the fluorine component; passing the waste gas through a filter on which the fluorine-reactive powder is deposited so as to react with the fluorine component; and removing the deposited powder layer from the filter.
Claim 15
Dependent Claim
98 words
In a method of cleaning a fluorine-containing waste gas evolved from a furnace, by contacting it with a fluorine-reactive powder and filtering the fluorine-reactive powder by a filter, an improvement which comprises cooling the waste gas to 150°-400° C by a water spray; feeding into the cooled waste gas an active calcium compound powder at a molar ratio of 1.5 - 10 relative to the fluorine component; passing the waste gas through a filter on which the fluorine-reactive powder is deposited so as to react with the fluorine component; and removing the deposited powder layer from the filter.
Claim 16
Dependent Claim
128 words
In a method of cleaning a fluorine-containing waste gas evolved from a furnace by contacting it with a fluorine-reactive powder and filtering the fluorine-reactive powder by a filter, an improvement which comprises cooling the waste gas to 150° - 400° C by a water spray; feeding into the cooled waste gas an active calcium hydroxide powder, at a molar ratio of 1.5 - 10 relative to the fluorine component; passing the waste gas through a glass fiber bag filter on which the fluorine-reactive powder is deposited so as to react with the fluorine component; and removing from the filter part of the deposited powder layer having a thickness of less than 5 mm while a residual deposited powder layer having a thickness of more than 5 mm remains.
Claim 17
Dependent Claim
128 words
In a method of cleaning a fluorine-containing waste gas evolved from a furnace by contacting it with a fluorine-reactive powder and filtering the fluorine-reactive powder by a filter, an improvement which comprises cooling the waste gas to 150° - 400° C by a water spray; feeding into the cooled waste gas an active calcium hydroxide powder, at a molar ratio of 1.5 - 10 relative to the fluorine component; passing the waste gas through a glass fiber bag filter on which the fluorine-reactive powder is deposited so as to react with the fluorine component; and removing from the filter part of the deposited powder layer having a thickness of less than 5 mm while a residual deposited powder layer having a thickness of more than 5 mm remains.
Claim 18
Dependent Claim
32 words
The method of claim 1, wherein a part of the separated powder obtained from the deposited powder layer is recycled by feeding it into the waste gas path after the cooling step.
Claim 19
Dependent Claim
20 words
The method of claim 1, wherein a part of the separated powder is fed along with the fresh fluorine-reactive powder.
Claim 20
Dependent Claim
23 words
The method of claim 1, wherein some of the cooled waste gas is by-passed and the fluorine-reactive powder is fed in the by-pass.
Claim 21
Dependent Claim
26 words
The method of claim 19, wherein a part of a separated powder obtained from the deposited powder layer is recycled by feeding it through the by-pass.
Claim 22
Dependent Claim
23 words
The method of claim 17, wherein the ratio of the separated powder recycled to the fluorine-reactive powder is 0.1 - 10:1 by weight.
Claim 23
Dependent Claim
134 words
In a method of cleaning a fluorine-containing waste gas evolved from a furance and containing components having a melting point above about 500°-600° C by contacting said gas with fluorine-reactive powder and filtering the fluorine-reactive powder by a filter, the improvement which comprises precooling said waste gas to 500°-600° C in a duct before entering the cooler to solidify the components of said waste gas having a melting point above said precooling temperatures, then further cooling the waste gas to 150°-400° C in a cooler with a waste spray; feeding a fluorine-reactive powder into the cooled waste gas; passing the cooled waste gas through a filter on which the fluorine-reactive powder is deposited so as to react with the fluorine component of the waste gas; and removing the deposited powder layer from the filter.
Claim 24
Dependent Claim
134 words
In a method of cleaning a fluorine-containing waste gas evolved from a furance and containing components having a melting point above about 500°-600° C by contacting said gas with fluorine-reactive powder and filtering the fluorine-reactive powder by a filter, the improvement which comprises precooling said waste gas to 500°-600° C in a duct before entering the cooler to solidify the components of said waste gas having a melting point above said precooling temperatures, then further cooling the waste gas to 150°-400° C in a cooler with a waste spray; feeding a fluorine-reactive powder into the cooled waste gas; passing the cooled waste gas through a filter on which the fluorine-reactive powder is deposited so as to react with the fluorine component of the waste gas; and removing the deposited powder layer from the filter.
Claim 25
Dependent Claim
134 words
In a method of cleaning a fluorine-containing waste gas evolved from a furnance, by contacting said gas with a fluorine-reactive powder and filtering the fluorine-reactive powder by a filter, an improvement which comprises cooling the waste gas to 150°-400° C with a water spray; by-passing some of the cooled waste gas; feeding a fluorine-reactive powder into the cooled by-passed waste gas; introducing said cooled by-passed waste gas containing the fluorine-reactive powder into the cooled waste gas stream; passing the cooled waste gas through a filter on which the fluorine-reactive powder is deposited so as to react with the fluorine component of the waste gas; removing the deposited powder layer from the filter; and recycling a part of said removed powder by feeding it to the cooled waste gas along with the fresh, fluorine-reactive powder.
Claim 26
Dependent Claim
134 words
In a method of cleaning a fluorine-containing waste gas evolved from a furnance, by contacting said gas with a fluorine-reactive powder and filtering the fluorine-reactive powder by a filter, an improvement which comprises cooling the waste gas to 150°-400° C with a water spray; by-passing some of the cooled waste gas; feeding a fluorine-reactive powder into the cooled by-passed waste gas; introducing said cooled by-passed waste gas containing the fluorine-reactive powder into the cooled waste gas stream; passing the cooled waste gas through a filter on which the fluorine-reactive powder is deposited so as to react with the fluorine component of the waste gas; removing the deposited powder layer from the filter; and recycling a part of said removed powder by feeding it to the cooled waste gas along with the fresh, fluorine-reactive powder.
Claim 27
Dependent Claim
32 words
The method of claim 20, wherein a part of the separated powder obtained from the deposited powder layer is recycled by feeding it into the waste gas path after the cooling step.
Claim 28
Dependent Claim
20 words
The method of claim 20, wherein a part of the separated powder is fed along with the fresh fluorine-reactive powder.
Claim 29
Dependent Claim
23 words
The method of claim 20, wherein some of the cooled waste gas is by-passed and the fluorine-reactive powder is fed in the by-pass.
Claim 30
Dependent Claim
26 words
The method of claim 24, wherein a part of a separated powder obtained from the deposited powder layer is recycled by feeding it through the by-pass.
Claim 31
Dependent Claim
23 words
The method of claim 25, wherein the ratio of the separated powder recycled to the fluorine-reactive powder is 0.1 - 10:1 by weight.
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) | 1980-08-15 | 1981-02-14 | 1981-08-16 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-08-15 | 1985-02-14 | 1985-08-16 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-08-15 | 1989-02-14 | 1989-08-16 | $7700.00 | Window Closed / Lapsed |