Patent US4244325A successfully refreshed from Google Patents.
US4244325A
Expired / Lapsed
US
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Disposal of oxides of nitrogen and heat recovery in a single self-contained structure
Assignee: KGI Inc
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Filing: 1979-03-01
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Granted: 1981-01-13
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Expires: 1999-03-01
Abstract
Abstract A self-contained single structure for NOX disposal and heat recovery, comprising a burner means (12), including means to supply NOX (oxides of nitrogen) gases (146) to be reduced, primary air (130) in less-than-stoichiometric flow rate, and gaseous fuel (128) at selected flow rate. The gases flow into a first reducing section (114), in which the fuel is burned in a reducing atmosphere, and the NOX gases are reduced. Fire tubes (124) carrying water or steam are positioned to receive heat from the burning gases. At the outlet of the reducing section precooled stack gases (135) are injected (137) into the flame so as to cool the hot products of combustion. The direction of flow of hot gases is turned to 90° (164) in a second section. At the end of the second section the direction of flow is turned 90° so as to be counter to the first direction in a third or oxidizing section (182) to which secondary air is added (172) and a fourth or boiler section (124) accepts the hot gases from the oxidizing section to recover the waste heat.
Inventors
- 👤 Wallace F. Hart
- 👤 David O. Watts
- 👤 Robert D. Reed
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-07 23:46
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/54; B01D53/56; F; F22; F22B; F22B33/00; F23; F23G; F23G7/00; F23G7/06; F23G7/061; F23G7/065
Claims Analysis
Total Claims: 15
Claim 1
Independent Claim
225 words
A self-contained combination NOX disposal and heat recovery system characterized by: (a) a burner means and means to supply to said burner means NOX gases to be reduced, gaseous fuel at selected flow rate sufficient to maintain combustion, and primary air in less-than-stoichiometric flow rate; (b) a reducing section in which said NOX gases, primary air and fuel are burned after flowing through said burner means in a first direction; (c) water/steam tubes positioned in said reducing section to receive heat from the flame therein; (d) means to inject cooled stack gases into the hot products of combustion as they leave said reducing section into a furnace section downstream of said reducing section; (e) outlet means from said furnace section positioned such that the gases flowing out of said furnace section flow in a second direction opposite to said first direction; (f) means to inject secondary air into said gases flowing out of said furnace section; whereby the total of primary plus secondary air is greater-than-stoichiometric value; (g) a reoxidation section positioned to receive the flame and products of combustion flowing out of said furnace section in said second direction, and to output its products of reoxidation in said second direction to a heat recovery section; and (h) means to output cooled, NOX-reduced products of combustion from said heat recovery section to a stack means.
Claim 2
Dependent Claim
225 words
A self-contained combination NOX disposal and heat recovery system characterized by: (a) a burner means and means to supply to said burner means NOX gases to be reduced, gaseous fuel at selected flow rate sufficient to maintain combustion, and primary air in less-than-stoichiometric flow rate; (b) a reducing section in which said NOX gases, primary air and fuel are burned after flowing through said burner means in a first direction; (c) water/steam tubes positioned in said reducing section to receive heat from the flame therein; (d) means to inject cooled stack gases into the hot products of combustion as they leave said reducing section into a furnace section downstream of said reducing section; (e) outlet means from said furnace section positioned such that the gases flowing out of said furnace section flow in a second direction opposite to said first direction; (f) means to inject secondary air into said gases flowing out of said furnace section; whereby the total of primary plus secondary air is greater-than-stoichiometric value; (g) a reoxidation section positioned to receive the flame and products of combustion flowing out of said furnace section in said second direction, and to output its products of reoxidation in said second direction to a heat recovery section; and (h) means to output cooled, NOX-reduced products of combustion from said heat recovery section to a stack means.
Claim 3
Dependent Claim
23 words
The system as in claim 1 including a reduction in cross-section for gas flow at point of injection of said cooled stack gases.
Claim 4
Dependent Claim
23 words
The system as in claim 1 including a reduction in cross-section for gas flow at the point of injection of said secondary air.
Claim 5
Dependent Claim
28 words
The apparatus as in claim 1 including means to conduct heated water/steam from the heat recovery section as the input to said water/steam tubes in said reducing section.
Claim 6
Dependent Claim
38 words
The system as in claim 2 including means to take cooled gaseous products of combustion at the outlet of said heat recovery section, and to inject said cooled gases under pressure at the outlet of said reducing section.
Claim 7
Dependent Claim
31 words
The system as in claim 4 including means to inject said cooled gases substantially perpendicular to said first direction from opposite sides of said gases flowing out of said reducing section.
Claim 8
Dependent Claim
31 words
The system as in claim 4 including means to inject said cooled gases substantially perpendicular to said first direction from opposite sides of said gases flowing out of said furnace section.
Claim 9
Dependent Claim
20 words
The apparatus as in claim 7 in which the outer diameter of said reducing and cooling sections are substantially equal.
Claim 10
Dependent Claim
22 words
The apparatus as in claim 7 in which the outer diameters of said reoxidation section and said boiler means are substantially equal.
Claim 11
Dependent Claim
50 words
The apparatus as in claim 7 in which said means to inject said cooled stack gases into said cooling section comprises axial tubular means extending from a wall at the downstream end of said means to reverse direction, and including radial ports through the wall of said axial tubular means.
Claim 12
Dependent Claim
230 words
A combination NOX disposal and heat recovery system, characterized by: (a) A burner means and means to supply to said burner means with; NOX gases to be reduced, primary air in less-than-stoichiometric flow rate; and a gaseous fuel at selected flow rate; (b) a reducing section in which NOX gases, primary air and fuel are burned after flowing through said burner means, in a first direction; (c) annular fire tube boiler means, surrounding said reducing section; the inner wall of said boiler means forming the outer wall of aid reducing section, whereby heat is transferred through said fire wall from said reducing section to said boiler; (d) a cooling section downstream of said reducing section; and means to inject into said cooling section a selected flow rate of cooled stack gases; (e) a reoxidation section surrounding said second cooling section with a common insulating wall therebetween; and means to reverse the direction of gas flow from said first direction in said reducing and cooling sections, to the opposite second direction in said reoxidation section; (f) means to inject secondary air into the gas flowing out of said cooling section; (g) means to conduct hot gases from said reoxidation section into the fire tubes of said annular boiler means to form said cooled stack gases; and (h) means to conduct said cooled gases to a stack and/or to said cooling section.
Claim 13
Dependent Claim
230 words
A combination NOX disposal and heat recovery system, characterized by: (a) A burner means and means to supply to said burner means with; NOX gases to be reduced, primary air in less-than-stoichiometric flow rate; and a gaseous fuel at selected flow rate; (b) a reducing section in which NOX gases, primary air and fuel are burned after flowing through said burner means, in a first direction; (c) annular fire tube boiler means, surrounding said reducing section; the inner wall of said boiler means forming the outer wall of aid reducing section, whereby heat is transferred through said fire wall from said reducing section to said boiler; (d) a cooling section downstream of said reducing section; and means to inject into said cooling section a selected flow rate of cooled stack gases; (e) a reoxidation section surrounding said second cooling section with a common insulating wall therebetween; and means to reverse the direction of gas flow from said first direction in said reducing and cooling sections, to the opposite second direction in said reoxidation section; (f) means to inject secondary air into the gas flowing out of said cooling section; (g) means to conduct hot gases from said reoxidation section into the fire tubes of said annular boiler means to form said cooled stack gases; and (h) means to conduct said cooled gases to a stack and/or to said cooling section.
Claim 14
Dependent Claim
209 words
A self-contained combination NOX disposal and heat recovery system, characterized by: (a) a burner means and means to supply to said burner means; NOX gases to be reduced, gaseous fuel at selected flow rate sufficient to maintain combustion, and primary air in less-than-stoichiometric flow rate; (b) a reducing section in which said NOX gases, primary air and fuel are burned after flowing through said burner means in a first direction; (c) water/steam tubes positioned in said reducing section to receive heat from the flame therein; (d) means to inject cooled stack gases into the hot products of combustion as they leave said reducing section; (e) a furnace section downstream of said reducing section, and outlet means from said furnace section positioned such that the gases flowing out of said section flow in a second direction opposite to said first direction; (f) means to inject secondary air into said gases flowing out of said furnace section; whereby the total of primary plus secondary air is greater-than-stoichiometric value; (g) a reoxidation section positioned to receive the flame and products of combustion flowing out of said furnace section in said second direction, and to output its products of reoxidation into heat exchange with said water/steam tubes to form said cooled stack gases.
Claim 15
Dependent Claim
209 words
A self-contained combination NOX disposal and heat recovery system, characterized by: (a) a burner means and means to supply to said burner means; NOX gases to be reduced, gaseous fuel at selected flow rate sufficient to maintain combustion, and primary air in less-than-stoichiometric flow rate; (b) a reducing section in which said NOX gases, primary air and fuel are burned after flowing through said burner means in a first direction; (c) water/steam tubes positioned in said reducing section to receive heat from the flame therein; (d) means to inject cooled stack gases into the hot products of combustion as they leave said reducing section; (e) a furnace section downstream of said reducing section, and outlet means from said furnace section positioned such that the gases flowing out of said section flow in a second direction opposite to said first direction; (f) means to inject secondary air into said gases flowing out of said furnace section; whereby the total of primary plus secondary air is greater-than-stoichiometric value; (g) a reoxidation section positioned to receive the flame and products of combustion flowing out of said furnace section in said second direction, and to output its products of reoxidation into heat exchange with said water/steam tubes to form said cooled stack gases.
References Cited (Backward Citations)
US2673141A
Cited
US3232713A
Cited
US3873671A
Cited
US3612001A
Cited
US3816595A
Cited
US3911083A
Cited
US3776199A
Cited
US4050877A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1984-01-13 | 1984-07-14 | 1985-01-13 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-01-13 | 1988-07-14 | 1989-01-13 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-01-13 | 1992-07-14 | 1993-01-13 | $7700.00 | Window Closed / Lapsed |