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US4592289A
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Reducing pollutant emissions from a spreader-stoker-fired furnace by stoichiometric control
Assignee: United States, US ENVIRONMENTAL PROTECTION AGENCY THE, Administrator of
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Filing: 1983-10-18
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Granted: 1986-06-03
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Expires: 2003-10-18
Abstract
Abstract Methods and apparatus for reducing pollutant emissions, and in particular, for reducing NO x and particulate emissions, from spreader-stoker-fired furnaces. A combustible material is introduced into the spreader-stoker-fired furnace and combusted while the stoichiometric ratio of oxygen to combustible material in different regions of the furnace is carefully controlled. Control of the stoichiometric ratio is accomplished by controlling the amount of air injected into different regions of the furnace and by controlling the amount of smaller particles of combustible material or fines introduced into the furnace.
Inventors
- 👤 David W. Pershing
- 👤 George B. Martin
- 👤 James M. Munro
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 10:08
CPC Classifications
F; F23; F23L; F23L7/00; F23L7/007; F23B; F23B1/00; F23B1/16; F23B1/22; F23K; F23K3/00; F23K3/16; F23K3/18; F23L1/00; F23L1/02; Y; Y02; Y02E; Y02E20/00; Y02E20/34
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
160 words
A method for reducing pollutant emissions in a spreader-stoker-fired furnace, the method comprising the steps of: obtaining particles of a combustible material; introducing the particles of combustible material into a spreader-stoker-fired furnace by a spreading means, the spreader-stoker-fired furnace having a bed region at the bottom thereof, an under-spreader region between the bed region and the spreading means, and an over-spreader region above the spreading means; combusting the particles of combustible material within the spreader-stoker-fired furnace in the presence of oxygen; and controlling the amount of oxygen flowing into the spreader-stoker-fired furnace such that the stoichiometric ratio of oxygen to combustible material is within the range of from about 0.6 to about 0.8 in the bed region of the spreader-stoker-fired furnace, is within the range of from about 0.9 to about 1.1 in the under-spreader region of the spreader-fired furnace, and is within the range of from about 0.75 to about 0.95 in the over-spreader region of the spreader-stoker-fired furnace.
Claim 2
Independent Claim
160 words
A method for reducing pollutant emissions in a spreader-stoker-fired furnace, the method comprising the steps of: obtaining particles of a combustible material; introducing the particles of combustible material into a spreader-stoker-fired furnace by a spreading means, the spreader-stoker-fired furnace having a bed region at the bottom thereof, an under-spreader region between the bed region and the spreading means, and an over-spreader region above the spreading means; combusting the particles of combustible material within the spreader-stoker-fired furnace in the presence of oxygen; and controlling the amount of oxygen flowing into the spreader-stoker-fired furnace such that the stoichiometric ratio of oxygen to combustible material is within the range of from about 0.6 to about 0.8 in the bed region of the spreader-stoker-fired furnace, is within the range of from about 0.9 to about 1.1 in the under-spreader region of the spreader-fired furnace, and is within the range of from about 0.75 to about 0.95 in the over-spreader region of the spreader-stoker-fired furnace.
Claim 3
Dependent Claim
48 words
A method for reducing pollutant emissions in a spreader-stoker-fired furnace as defined in claim 1 wherein the stoichiometric ratio of oxygen to combustible material is about 0.7 in the bed region, about 1 in the under-spreader region, and about 0.85 in the over-spreader region of the spreader-stoker-fired furnace.
Claim 4
Independent Claim
167 words
A method for reducing pollutant emissions in a spreader-stoker-fired furnace, the method comprising the steps of: obtaining particles of a combustible material having a significant propensity for clinker formation; introducing the particles of combustible material into a spreader-stoker-fired furnace by a spreading means, the spreader-stoker-fired furnace having a bed region at the bottom thereof, an under-spreader region between the bed region and the spreading means, and an over-spreader region above the spreading means; combusting the particles of combustible material within the spreader-stoker-fired furnace in the presence of oxygen; and controlling the amount of oxygen flowing into the spreader-stoker-fired furnace such that the stoichiometric ratio of oxygen to combustible material is within the range of from about 1.0 to about 1.2 in the bed region of the spreader-stoker-fired furnace, is within the range of from about 1.0 to about 1.2 in the under-spreader region of the spreader-stoker-fired furnace, and is within the range of from about 0.75 to about 0.95 in the over-spreader region of the spreader-stoker-fired furnace.
Claim 5
Independent Claim
167 words
A method for reducing pollutant emissions in a spreader-stoker-fired furnace, the method comprising the steps of: obtaining particles of a combustible material having a significant propensity for clinker formation; introducing the particles of combustible material into a spreader-stoker-fired furnace by a spreading means, the spreader-stoker-fired furnace having a bed region at the bottom thereof, an under-spreader region between the bed region and the spreading means, and an over-spreader region above the spreading means; combusting the particles of combustible material within the spreader-stoker-fired furnace in the presence of oxygen; and controlling the amount of oxygen flowing into the spreader-stoker-fired furnace such that the stoichiometric ratio of oxygen to combustible material is within the range of from about 1.0 to about 1.2 in the bed region of the spreader-stoker-fired furnace, is within the range of from about 1.0 to about 1.2 in the under-spreader region of the spreader-stoker-fired furnace, and is within the range of from about 0.75 to about 0.95 in the over-spreader region of the spreader-stoker-fired furnace.
Claim 6
Independent Claim
132 words
An apparatus for producing heat from a combustible material with reduced pollutant emissions, comprising: a spreader-stoker-fired furnace having spreading means for introducing particles of a combustible material into the spreader-stoker-fired furnace, the spreader-stoker-fired furnace having a bed region at the bottom thereof, an under-spreader region between the bed region and the spreading means, and an over-spreader region above the spreading means; and means for controlling the stoichiometric ratio of oxygen to combustible material in the spreader-stoker-fired furnace such that the stoichiometric ratio is within the range of from about 0.6 to about 0.8 in the bed region, is within the range of from about 0.9 to about 1.1 in the under-spreader region, and is within the range of from about 0.75 to about 0.95 in the over-spreader region of the spreader-stoker-fired furnace.
Claim 7
Independent Claim
132 words
An apparatus for producing heat from a combustible material with reduced pollutant emissions, comprising: a spreader-stoker-fired furnace having spreading means for introducing particles of a combustible material into the spreader-stoker-fired furnace, the spreader-stoker-fired furnace having a bed region at the bottom thereof, an under-spreader region between the bed region and the spreading means, and an over-spreader region above the spreading means; and means for controlling the stoichiometric ratio of oxygen to combustible material in the spreader-stoker-fired furnace such that the stoichiometric ratio is within the range of from about 0.6 to about 0.8 in the bed region, is within the range of from about 0.9 to about 1.1 in the under-spreader region, and is within the range of from about 0.75 to about 0.95 in the over-spreader region of the spreader-stoker-fired furnace.
Claim 8
Dependent Claim
56 words
An apparatus as defined in claim 4 wherein said controlling means comprises means for controlling the stoichiometric ratio of oxygen to combustible material in the spreader-stoker-fired furnace such that the stoichiometric ratio is about 0.7 in the bed region, about 1 in the under-spreader region, and about 0.85 in the over-spreader region of the spreader-stoker-fired furnace.
Claim 9
Independent Claim
139 words
An apparatus for producing heat from a combustible material with reduced pollutant emissions, comprising: a spreader-stoker-fired furnace having spreading means for introducing particles of a combustible material having a significant propensity for clinker formation into the spreader-stoker-fired furnace, the spreader-stoker-fired furnace having a bed region at the bottom thereof, an under-spreader region between the bed region and the spreading means, and an over-spreader region above the spreading means; and means for controlling the stoichiometric ratio of oxygen to combustible material in the spreader-stoker-fired furnace such that the stoichiometric ratio is within the range of from about 1.0 to about 1.2 in the bed region, is within the range of from about 1.0 to about 1.2 in the under-spreader region, and is within the range of from about 0.75 to about 0.95 in the over-spreader region of the spreader-stoker-fired furnace.
Claim 10
Independent Claim
139 words
An apparatus for producing heat from a combustible material with reduced pollutant emissions, comprising: a spreader-stoker-fired furnace having spreading means for introducing particles of a combustible material having a significant propensity for clinker formation into the spreader-stoker-fired furnace, the spreader-stoker-fired furnace having a bed region at the bottom thereof, an under-spreader region between the bed region and the spreading means, and an over-spreader region above the spreading means; and means for controlling the stoichiometric ratio of oxygen to combustible material in the spreader-stoker-fired furnace such that the stoichiometric ratio is within the range of from about 1.0 to about 1.2 in the bed region, is within the range of from about 1.0 to about 1.2 in the under-spreader region, and is within the range of from about 0.75 to about 0.95 in the over-spreader region of the spreader-stoker-fired furnace.
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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) | 1989-06-02 | 1989-12-02 | 1990-06-03 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1993-06-02 | 1993-12-02 | 1994-06-03 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1997-06-02 | 1997-12-02 | 1998-06-03 | $7700.00 | Window Closed / Lapsed |