US5103773A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Fluid bed furnace
Assignee: Valmet Power AB
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Filing: 1991-04-26
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Granted: 1992-04-14
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Expires: 2011-04-26
Abstract
Abstract At a fluidbed furnace comprising a combustion shaft, a particle separator, a particle return passage and designed according to conventional design criteria for obtaining a good combustion at moderate temperature, a destruction of laughing gas (N 2 O), and complete combustion of possible unburnt particles in the combustion gases is brought about in a reactor passage at the entrance of which a combustion means is located. The reactor passage is moderately cooled, so the increase of temperature in the combustion gases is maintained substantially constant unto the first convection heating surface.
Inventors
- 👤 Sven B. Andersson
- 👤 Bo G. Leckner
- 👤 Lars-Erik Amand
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 01:50
CPC Classifications
F; F27; F27B; F27B15/00; F23; F23C; F23C10/00; F23C10/02; F23C10/04; F23C10/08; F23C10/10; F23J; F23J15/00; F23J15/08; F27D; F27D17/00; F27D17/10; F27D17/18; F23C2206/00; F23C2206/10; F23C2206/101; F23J2215/00; F23J2215/10; F23J2215/101
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
238 words
A fluid bed furnace comprising: (a) a vertical combustion shaft comprising a gas outlet at a top end; (b) means for supplying solid fuel to the vertical combustion shaft and means for supplying primary combustion air to the vertical combustion shaft; (c) particle separator means for separating particles from gas exiting the vertical combustion shaft, said particle separator means being connected to the gas outlet of the vertical combustion shaft and comprising particle output means for outputting particles separated from the gas output means for outputting gas from which particles have been removed; (d) convection heating surfaces located in a flue downstream from the particle separator means; (e) combustion means located downstream from the gas outlet of the vertical combustion shaft for raising the temperature of gases exiting therefrom to an elevated temperature above that in the combustion shaft, said elevated temperature being in the range of 900° to 1100° C.; (f) means for mixing gases located downstream of the combustion means; and (g) a reactor passage extending between the gas output means of the particle separator means and the flue containing the convection heating surfaces, said reactor passage comprising insulation means for maintaining the temperature of gases substantially constant at said elevated temperature until the gases reach a first convection heating surface in the flue, wherein said combustion means is located at an entrance of the reactor passage near the gas output means of the particle separator.
Claim 2
Dependent Claim
238 words
A fluid bed furnace comprising: (a) a vertical combustion shaft comprising a gas outlet at a top end; (b) means for supplying solid fuel to the vertical combustion shaft and means for supplying primary combustion air to the vertical combustion shaft; (c) particle separator means for separating particles from gas exiting the vertical combustion shaft, said particle separator means being connected to the gas outlet of the vertical combustion shaft and comprising particle output means for outputting particles separated from the gas output means for outputting gas from which particles have been removed; (d) convection heating surfaces located in a flue downstream from the particle separator means; (e) combustion means located downstream from the gas outlet of the vertical combustion shaft for raising the temperature of gases exiting therefrom to an elevated temperature above that in the combustion shaft, said elevated temperature being in the range of 900° to 1100° C.; (f) means for mixing gases located downstream of the combustion means; and (g) a reactor passage extending between the gas output means of the particle separator means and the flue containing the convection heating surfaces, said reactor passage comprising insulation means for maintaining the temperature of gases substantially constant at said elevated temperature until the gases reach a first convection heating surface in the flue, wherein said combustion means is located at an entrance of the reactor passage near the gas output means of the particle separator.
Claim 3
Dependent Claim
20 words
The fluid bed furnace according to claim 1, wherein the means for mixing gases is located in the reactor passage.
Claim 4
Dependent Claim
33 words
The fluid bed furnace according to claim 1, wherein the reactor passage has a length such that gases will need up to 5 seconds to pass through the reactor passage during normal operation.
Claim 5
Dependent Claim
241 words
A fluid bed furnace comprising: (a) a vertical combustion shaft comprising a gas outlet at a top end; (b) means for supplying solid fuel to the vertical combustion shaft and means for supplying primary combustion air to the vertical combustion shaft; (c) particle separator means for separating particles from gas exiting the vertical combustion shaft, said particle separator means being connected to the gas outlet of the vertical combustion shaft and comprising particle output means for outputting particles separated from the gas and gas output means for outputting gas from which particles have been removed; (d) convection heating surfaces located in a flue downstream from the particle separator means; (e) combustion means located downstream from the gas outlet of the vertical combustion shaft for raising the temperature of gases exiting therefrom to an elevated temperature above that in the combustion shaft, said elevated temperature being in the range of 900° to 1100° C.; (f) means for mixing gases located downstream of the combustion means; and (g) a reactor passage extending between the gas output means of the particle separator means and the flue containing the convection heating surfaces, said reactor passage comprising insulation means for maintaining the temperature of gases substantially constant at said elevated temperature until the gases reach a first convection heating surface in the flue, wherein said combustion means is located at an entrance of the particle separator means near the gas outlet of the vertical combustion shaft.
Claim 6
Dependent Claim
241 words
A fluid bed furnace comprising: (a) a vertical combustion shaft comprising a gas outlet at a top end; (b) means for supplying solid fuel to the vertical combustion shaft and means for supplying primary combustion air to the vertical combustion shaft; (c) particle separator means for separating particles from gas exiting the vertical combustion shaft, said particle separator means being connected to the gas outlet of the vertical combustion shaft and comprising particle output means for outputting particles separated from the gas and gas output means for outputting gas from which particles have been removed; (d) convection heating surfaces located in a flue downstream from the particle separator means; (e) combustion means located downstream from the gas outlet of the vertical combustion shaft for raising the temperature of gases exiting therefrom to an elevated temperature above that in the combustion shaft, said elevated temperature being in the range of 900° to 1100° C.; (f) means for mixing gases located downstream of the combustion means; and (g) a reactor passage extending between the gas output means of the particle separator means and the flue containing the convection heating surfaces, said reactor passage comprising insulation means for maintaining the temperature of gases substantially constant at said elevated temperature until the gases reach a first convection heating surface in the flue, wherein said combustion means is located at an entrance of the particle separator means near the gas outlet of the vertical combustion shaft.
Claim 7
Dependent Claim
20 words
The fluid bed furnace according to claim 4, wherein the means for mixing gases is located in the reactor passage.
Claim 8
Dependent Claim
33 words
The fluid bed furnace according to claim 4, wherein the reactor passage has a length such that gases will need up to 5 seconds to pass through the reactor passage during normal operation.
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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) | 1995-04-14 | 1995-10-14 | 1996-04-14 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1999-04-14 | 1999-10-14 | 2000-04-14 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2003-04-14 | 2003-10-14 | 2004-04-14 | $7700.00 | Window Closed / Lapsed |