US4044102A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method for treating exhaust gases
Assignee: Kurashiki Spinning Co Ltd
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Filing: 1975-12-19
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Granted: 1977-08-23
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Expires: 1995-12-19
Abstract
Abstract Apparatus for treating exhaust gases comprising a catalyst bed through which the exhaust gas is passed whereby nitrogen oxides and dust present therein are removed from the gas, said catalyst bed being designed such that the catalyst therein is discharged from the bed continuously or intermittantly while being fed in an amount that can compensate for the discharged amount, a heating device for heating the catalyst discharged from the bed to a temperature in a range from about 700° to 1200° C. for reactivation of the catalyst and separation of the dust accumulated on the bed surface and retained in the interstices between the catalyst particles therein, and a device for discharging sulfur dioxides produced during the course of heating the catalyst. This apparatus is very effective in simultaneously removing the nitrogen oxides and the dust from exhaust gases such as boiler exhaust gases.
Inventors
- 👤 Ryoji Muraki
- 👤 Masao Endo
- 👤 Nobuaki Aoki
- 👤 Masahiro Takeshita
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-25 06:27
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/74; B01D53/86; B01D53/8621; B01D53/8625; B01D53/8631
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
172 words
In a continuous method of removing nitrogen oxides and dust from flue gases formed by the combustion of fuel which comprises passing the flue gas, in admixture with ammonia, through a fixed particulate catalyst bed capable of reducing nitrogen oxides in the presence of ammonia, wherein said nitrogen oxides are reduced and said dust is retained by the catalyst bed thereby increasing the gas passage pressure, the improvement which comprises: a. continuously or intermittently discharging a portion of the particulate catalyst and accumulated dust from said bed at a rate between about 10 to 100 mm per hour per 500 to 10,000 mm of catalyst bed height, which rate is sufficient to prevent plugging of the catalyst bed, while feeding catalyst into the catalyst bed in an amount that compensates for the amount of catalyst removed, b. heating of the catalyst discharged from said bed to reactivate said catalyst and remove a gas therefrom, c. separating the reactivated catalyst from the dust, and d. returning the regenerated catalyst to the catalyst bed.
Claim 2
Dependent Claim
172 words
In a continuous method of removing nitrogen oxides and dust from flue gases formed by the combustion of fuel which comprises passing the flue gas, in admixture with ammonia, through a fixed particulate catalyst bed capable of reducing nitrogen oxides in the presence of ammonia, wherein said nitrogen oxides are reduced and said dust is retained by the catalyst bed thereby increasing the gas passage pressure, the improvement which comprises: a. continuously or intermittently discharging a portion of the particulate catalyst and accumulated dust from said bed at a rate between about 10 to 100 mm per hour per 500 to 10,000 mm of catalyst bed height, which rate is sufficient to prevent plugging of the catalyst bed, while feeding catalyst into the catalyst bed in an amount that compensates for the amount of catalyst removed, b. heating of the catalyst discharged from said bed to reactivate said catalyst and remove a gas therefrom, c. separating the reactivated catalyst from the dust, and d. returning the regenerated catalyst to the catalyst bed.
Claim 3
Dependent Claim
25 words
A method, as in claim 1, wherein the catalyst discharged from the catalyst bed is heated in the range of about 700° to 1200° C.
Claim 4
Dependent Claim
19 words
A method, as in claim 2, wherein the catalyst is heated in the range of 700° to 1000° C.
Claim 5
Dependent Claim
14 words
A method, as in claim 1, wherein the flue gas further comprises sulfur oxides.
Claim 6
Dependent Claim
151 words
In a continuous method of removing nitrogen oxides and dust from flue gases formed by the combustion of fuel which comprises passing the flue gas, in admixture with ammonia, through a fixed particulate catalyst bedcapable of reducing nitrogen oxides in the presence of ammonia, wherein said nitrogen oxides are reduced and said dust is retained by the catalyst bed thereby increasing the gas passage pressure, the improvement which comprises: a. continuously or intermittently discharging a portion of the particulate catalyst and accumulated dust from said bed at a rate between about 10 to 100 mm per hour per 500 to 10,000 mm of catalyst bed height, which rate is sufficient to prevent plugging of the catalyst bed, while feeding catalyst into the catalyst bed in an amount that compensates for the amount of catalyst removed, b. separating the catalyst from the dust, and c. returning the catalyst to the catalyst bed.
Claim 7
Dependent Claim
151 words
In a continuous method of removing nitrogen oxides and dust from flue gases formed by the combustion of fuel which comprises passing the flue gas, in admixture with ammonia, through a fixed particulate catalyst bedcapable of reducing nitrogen oxides in the presence of ammonia, wherein said nitrogen oxides are reduced and said dust is retained by the catalyst bed thereby increasing the gas passage pressure, the improvement which comprises: a. continuously or intermittently discharging a portion of the particulate catalyst and accumulated dust from said bed at a rate between about 10 to 100 mm per hour per 500 to 10,000 mm of catalyst bed height, which rate is sufficient to prevent plugging of the catalyst bed, while feeding catalyst into the catalyst bed in an amount that compensates for the amount of catalyst removed, b. separating the catalyst from the dust, and c. returning the catalyst to the catalyst bed.
Claim 8
Dependent Claim
14 words
A method, as in claim 5, wherein the flue gas further comprises sulfur oxides.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-08-22 | 1981-02-21 | 1981-08-23 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-08-22 | 1985-02-21 | 1985-08-23 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-08-22 | 1989-02-21 | 1989-08-23 | $7700.00 | Window Closed / Lapsed |