US4453497A
Expired / Lapsed
US
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Augmented heat transfer method and apparatus
Assignee: Struthers Thermo-Flood Corp
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Filing: 1982-12-21
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Granted: 1984-06-12
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Expires: 2002-12-21
Abstract
Abstract The operation of gas turbines in combined cycle or cogeneration plants utilizing circulating fluidized beds is improved by increasing the temperature of the air supplied them. The temperature of bed solids circulating through an external heat exchanger is raised by combusting fuel in a combustion-augmenting zone through which the circulating solids pass. The gaseous products are combustion from that zone are introduced into the fluidized bed combustor. Thus the fluidized bed combustor operates at temperatures affording optimum sulfur removal by sulfur absorbing materials, the combustion-augmenting zone operates at an appreciably higher temperature to provide increased heat transfer to the compressed air for the gas turbine, and the off gases from the combustion-augmenting zone, which may be high in sulfur, are cooled in the combustor so as to bring about their desulfurization therein. Suitable apparatus is provided.
Inventors
- 👤 James S. Davis
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 02:37
CPC Classifications
F; F23; F23C; F23C10/00; F23C10/002; B; B01; B01J; B01J8/00; B01J8/18; B01J8/24; B01J8/26; B01J8/38; B01J8/384; B01J8/388; F02; F02C; F02C3/00; F02C3/20; F02C3/205; Y; Y02; Y02E; Y02E20/00; Y02E20/16
Claims Analysis
Total Claims: 14
Claim 1
Independent Claim
230 words
The method of heating a fluid by the combustion of carbonaceous fuel containing sulfur together with particulate sulfur sorbing material to a temperature higher than the temperature range in which the sulfur sorbing material effectively sorbes sulfur from the carbonaceous fuel without increasing the sulfur content of the gaseous products of combustion beyond that associated with said temperature range, comprising combusting the carbonaceous fuel containing sulfur together with the particles of sulfur-sorbing material in a fluidized bed within said temperature range, and not exceeding about 1700° F., drawing off the gaeous products of combustion and entrained fluidized bed solids therefrom, circulating said fluidized bed solids through a separate combustion-augmenting chamber in tandem with a heat exchanging chamber in heat-exchanging relation in the heat exchanging chamber only with the fluid to be heated therein and back to said fluidized bed, introducing additional fuel into the separate combustion-augmenting chamber and combusting that fuel in that chamber to raise the temperature of the circulating fluidized bed solids in that chamber above said range, and not less than about 1600° F., thereby raising the temperature of the fluid heated by said solids in the heat exchanging chamber above said range, and generating sulfur-containing gaseous products of combustion, drawing off from the combustion-augmenting chamber the sulfur-containing gaseous products of combustion there generated, returning them to the fluidized bed, and removing sulfur therefrom in that bed.
Claim 2
Independent Claim
230 words
The method of heating a fluid by the combustion of carbonaceous fuel containing sulfur together with particulate sulfur sorbing material to a temperature higher than the temperature range in which the sulfur sorbing material effectively sorbes sulfur from the carbonaceous fuel without increasing the sulfur content of the gaseous products of combustion beyond that associated with said temperature range, comprising combusting the carbonaceous fuel containing sulfur together with the particles of sulfur-sorbing material in a fluidized bed within said temperature range, and not exceeding about 1700° F., drawing off the gaeous products of combustion and entrained fluidized bed solids therefrom, circulating said fluidized bed solids through a separate combustion-augmenting chamber in tandem with a heat exchanging chamber in heat-exchanging relation in the heat exchanging chamber only with the fluid to be heated therein and back to said fluidized bed, introducing additional fuel into the separate combustion-augmenting chamber and combusting that fuel in that chamber to raise the temperature of the circulating fluidized bed solids in that chamber above said range, and not less than about 1600° F., thereby raising the temperature of the fluid heated by said solids in the heat exchanging chamber above said range, and generating sulfur-containing gaseous products of combustion, drawing off from the combustion-augmenting chamber the sulfur-containing gaseous products of combustion there generated, returning them to the fluidized bed, and removing sulfur therefrom in that bed.
Claim 3
Dependent Claim
18 words
The method of claim 1 in which the additional fuel introduced into the combustion-augmenting chamber is injected therein.
Claim 4
Dependent Claim
17 words
The method of claim 1 in which a fluidizing gas is introduced into the combustion augmenting chamber.
Claim 5
Dependent Claim
27 words
The method of claim 1 in which the sulfur-sorbing material is limestone and the temperature range maintained in the fluidized bed is about 1450° to 1700° F.
Claim 6
Dependent Claim
20 words
The method of claim 4 in which the temperature maintained in the combustion-augmenting chamber is about 1600° to 1900° F.
Claim 7
Dependent Claim
12 words
The method of claim 1 in which the fluid is a gas.
Claim 8
Dependent Claim
53 words
The method of claim 1 in which the fluid is a first fluid, the heat exchanging chamber is a first heat exchanging chamber, and in which the heated first fluid from the first heat exchanging chamber is circulated through a second heat exchanging chamber thereby raising the temperature of a second fluid therein.
Claim 9
Dependent Claim
16 words
The method of claim 7 in which the first fluid is a high heat capacity fluid.
Claim 10
Dependent Claim
16 words
The method of claim 8 in which the high heat capacity fluid is a molten metal.
Claim 11
Dependent Claim
180 words
In apparatus for heating a fluid by combustion of carbonaceous fuel containing sulfur together with particulate sulfur-sorbing material in a fluidized bed combustor and circulating entrained fluidized bed solids from the combustor through a heat exchanger external thereto so as to heat a fluid therein, the improvement comprising a combustion-augmenting chamber external of the combustor connected to receive entrained heated fluidized bed solids at temperature not exceeding about 1700° F. from the combustor and deliver them to said heat exchanger, means for introducing additional fuel into the combustion-augmenting chamber and combusting it therein to raise the temperature of the fluidized bed solids therein above the temperature range in which desulfurization by the sulfur-sorbing material is effective, and not less than about 1600° F. whereby the fluidized bed solids from the combustion-augmenting chamber raise the temperature of the fluid in the heat exchanger correspondingly, and means for returning the sulfur-containing gaseous products of combustion generated in the combustion-augmenting chamber to the combustor, whereby those products of combustion are cooled in the combustor to the said combustor temperature range and desulfurized therein.
Claim 12
Dependent Claim
180 words
In apparatus for heating a fluid by combustion of carbonaceous fuel containing sulfur together with particulate sulfur-sorbing material in a fluidized bed combustor and circulating entrained fluidized bed solids from the combustor through a heat exchanger external thereto so as to heat a fluid therein, the improvement comprising a combustion-augmenting chamber external of the combustor connected to receive entrained heated fluidized bed solids at temperature not exceeding about 1700° F. from the combustor and deliver them to said heat exchanger, means for introducing additional fuel into the combustion-augmenting chamber and combusting it therein to raise the temperature of the fluidized bed solids therein above the temperature range in which desulfurization by the sulfur-sorbing material is effective, and not less than about 1600° F. whereby the fluidized bed solids from the combustion-augmenting chamber raise the temperature of the fluid in the heat exchanger correspondingly, and means for returning the sulfur-containing gaseous products of combustion generated in the combustion-augmenting chamber to the combustor, whereby those products of combustion are cooled in the combustor to the said combustor temperature range and desulfurized therein.
Claim 13
Dependent Claim
24 words
Apparatus of claim 10 in which the fluidized bed solids circulate through tubes in the heat exchanger and the fluid passes around those tubes.
Claim 14
Dependent Claim
46 words
Apparatus of claim 11 in which the fluid is a first fluid and including a second heat exchanger and means for circulating the first fluid through the second heat exchanger in heat-exchanging relation with a second fluid therein, thereby raising the temperature of the second fluid.
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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) | 1987-06-12 | 1987-12-12 | 1988-06-12 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-06-12 | 1991-12-12 | 1992-06-12 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-06-12 | 1995-12-12 | 1996-06-12 | $7700.00 | Window Closed / Lapsed |