US4434726A
Expired / Lapsed
US
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Fine particulate feed system for fluidized bed furnace
Assignee: Combustion Engineering Inc
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Filing: 1982-12-27
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Granted: 1984-03-06
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Expires: 2002-12-27
Abstract
Abstract A method and apparatus for feeding solids into the bed of a fluidized bed furnace (18). The feed solids are separated into a fine fraction and a coarse fraction. The coarse fraction is supplied to fluidized bed (16) in an in-bed pneumatic transport feed system or in an over-the-bed feed system. The fine fraction as well as fluidizing air are supplied to fines admission zone (24) wherein the fine fraction and fluidizing air are thoroughly mixed. The mixture of the fine fraction of feed solids and the fludizing air is then passed upwardly through air distribution means (38) into fluidized bed (16).
Inventors
- 👤 Brian C. Jones
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-27 04:33
CPC Classifications
F; F23; F23C; F23C10/00; F23C10/02; F23C10/04; F23C10/08; F23C10/10
Claims Analysis
Total Claims: 16
Claim 1
Independent Claim
153 words
In a fluidized bed furnace of the type having a furnace chamber with an air distributor plate extending transversely across the chamber dividing the chamber into a combustion zone in which the fluidized bed, once established, is confined above the air distributor plate and an air inlet zone below the air distributor plate, a method of introducing particulate feed solids including both a coarse fraction and a fine fraction into the fluidized bed furnace, comprising the steps of: (a) passing the coarse fraction directly to the combustion zone; (b) establishing a flow of fluidizing air up through the air distributor plate and combustion zone; (c) passing the fine fraction to the air inlet zone; (d) mixing the fine fraction with the fluidizing air in the air inlet zone; and (e) passing the mixture of the fine fraction and fluidizing air up through the air distributor plate thence up through the the fluidized bed.
Claim 2
Dependent Claim
153 words
In a fluidized bed furnace of the type having a furnace chamber with an air distributor plate extending transversely across the chamber dividing the chamber into a combustion zone in which the fluidized bed, once established, is confined above the air distributor plate and an air inlet zone below the air distributor plate, a method of introducing particulate feed solids including both a coarse fraction and a fine fraction into the fluidized bed furnace, comprising the steps of: (a) passing the coarse fraction directly to the combustion zone; (b) establishing a flow of fluidizing air up through the air distributor plate and combustion zone; (c) passing the fine fraction to the air inlet zone; (d) mixing the fine fraction with the fluidizing air in the air inlet zone; and (e) passing the mixture of the fine fraction and fluidizing air up through the air distributor plate thence up through the the fluidized bed.
Claim 3
Dependent Claim
53 words
A method of introducing particulate feed solids into a fluidized bed furnace as recited in claim 1 wherein the step of mixing the fine fraction with the fluidizing air comprises introducing the fine feed solids into the fluidizing air in a plurality of streams with each stream directed tangentially to an imaginary circle.
Claim 4
Dependent Claim
24 words
A method of introducing particulate feed solids into a fluidized bed furnace as recited in claim 1 wherein the feed solids comprise crushed coal.
Claim 5
Dependent Claim
26 words
A method of introducing particulate feed solids into a fluidized bed furnace as recited in claim 1 wherein the feed solids comprise crushed coal and limestone.
Claim 6
Dependent Claim
30 words
A method of introducing particulate feed solids into a fluidized bed furnace as recited in claim 1 wherein the fine fraction comprises pulverized coal and the coarse fraction comprises limestone.
Claim 7
Dependent Claim
44 words
A method of introducing particulate feed solids into a fluidized bed furnace as recited in claim 1 wherein the fine fraction is a particular material from the group consisting essentially of pulverized coal, pulverized limestone, recycle material, pulverized bed drain material and mixtures thereof.
Claim 8
Dependent Claim
43 words
A method of introducing particulate feed solids into a fluidized bed furnace as recited in claim 1 further comprising maintaining the upward velocity of the mixture of fine feed solids and fluidizing air greater than the entrainment velocity of the fine feed solids.
Claim 9
Dependent Claim
156 words
In a fluidized bed furnace of the type having a furnace chamber with an air distributor plate extending transversely across the chamber dividing the chamber into a combustion zone in which the fluidized bed, once established, is confined above the air distributor plate and an air inlet zone below the air distributor plate a method of introducing particulate feed solids into the fluidized bed furnace, comprising the steps of: (a) separating the feed solids into a fine fraction and a coarse fraction; (b) passing the coarse fraction directly to the combustion zone; (c) establishing a flow of fluidizing air up through the air distributor plate and combustion zone; (d) passing the fine fraction to the air inlet zone; (e) mixing the fine fraction with the fluidizing air in the air inlet zone; and (f) passing the mixture of the fine fraction and fluidizing air up through the air distributor plate thence up through the fluidized bed.
Claim 10
Dependent Claim
156 words
In a fluidized bed furnace of the type having a furnace chamber with an air distributor plate extending transversely across the chamber dividing the chamber into a combustion zone in which the fluidized bed, once established, is confined above the air distributor plate and an air inlet zone below the air distributor plate a method of introducing particulate feed solids into the fluidized bed furnace, comprising the steps of: (a) separating the feed solids into a fine fraction and a coarse fraction; (b) passing the coarse fraction directly to the combustion zone; (c) establishing a flow of fluidizing air up through the air distributor plate and combustion zone; (d) passing the fine fraction to the air inlet zone; (e) mixing the fine fraction with the fluidizing air in the air inlet zone; and (f) passing the mixture of the fine fraction and fluidizing air up through the air distributor plate thence up through the fluidized bed.
Claim 11
Dependent Claim
53 words
A method of introducing particulate feed solids into a fluidized bed furnace as recited in claim 8 wherein the step of mixing the fine fraction with the fluidizing air comprises introducing the fine feed solids into the fluidizing air in a plurality of streams with each stream directed tangentially to an imaginary circle.
Claim 12
Dependent Claim
24 words
A method of introducing particulate feed solids into a fluidized bed furnace as recited in claim 8 wherein the feed solids comprise crushed coal.
Claim 13
Dependent Claim
26 words
A method of introducing particulate feed solids into a fluidized bed furnace as recited in claim 8 wherein the feed solids comprise crushed coal and limestone.
Claim 14
Dependent Claim
30 words
A method of introducing particulate feed solids into a fluidized bed furnace as recited in claim 8 wherein the fine fraction comprises pulverized coal and the coarse fraction comprises limestone.
Claim 15
Dependent Claim
44 words
A method of introducing particulate feed solids into a fluidized bed furnace as recited in claim 8 wherein the fine fraction is a particular material from the group consisting essentially of pulverized coal, pulverized limestone, recycle material, pulverized bed drain material and mixtures thereof.
Claim 16
Dependent Claim
43 words
A method of introducing particulate feed solids into a fluidized bed furnace as recited in claim 8 further comprising maintaining the upward velocity of the mixture of fine feed solids and fluidizing air greater than the entrainment velocity of the fine feed solids.
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) | 1987-03-06 | 1987-09-05 | 1988-03-06 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-03-06 | 1991-09-05 | 1992-03-06 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-03-06 | 1995-09-05 | 1996-03-06 | $7700.00 | Window Closed / Lapsed |