US4823739A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Apparatus for control of the heat transfer produced in a fluidized bed
Assignee: LUCKY YUPPY PUPPY Co A CORP OF ILLINOIS
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Filing: 1987-03-03
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Granted: 1989-04-25
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Expires: 2007-03-03
Abstract
Abstract Apparatus for control of the heat transfer between a circulating bed of solid particles and a heat exchanger (6) located inside a fluidization enclosure (1) supplied with solid particles and connected to a device for recovering (4) and recycling (5) the particles into the fluidized bed. The heat exchange coefficient of the exchanger (6) is adapted at each moment to the heat transfer requirements of the plant by varying in the same sense the concentration of solid particles in the circulating bed, by increasing or reducing the quantity of circulating particles to increase or reduce, respectively, the exchange coefficient to the value required by the demand. The invention is particularly applicable to steam production boilers operating on coal.
Inventors
- 👤 Michel Marcellin
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 05:54
CPC Classifications
B; B01; B01J; B01J8/00; B01J8/18; B01J8/1809; F; F22; F22B; F22B31/00; F22B31/0007; F22B31/0084; F23; F23C; F23C10/00; F23C10/02; F23C10/04; F23C10/08; F23C10/10; F23C10/18; F23C10/28; F23C10/30; F28; F28D; F28D13/00; B01J2208/00; B01J2208/00008; B01J2208/00017; B01J2208/00026; B01J2208/00035; B01J2208/0007; B01J2208/00106; B01J2208/00168; B01J2208/00256; B01J2208/00327; B01J2208/00336; B01J2208/0038; B01J2208/0053; B01J2208/00548; B01J2208/00654; B01J2208/00663; F23C2206/00; F23C2206/10; F23C2206/101
Claims Analysis
Total Claims: 4
Claim 1
Independent Claim
247 words
In apparatus for controlling the heat transfer produced between a circulating fluidized bed of solid particles and a heat-transfer fluid circulating in a heat exchanger (b) placed inside an enclosure (1) supplied with solid particles and provided at its base with means (3) for injecting an upward stream of fluidizing gas, the fluidized bed comprising a dense phase (b) with a high particle concentration and a dilute phase (C) containing fine particles entrained with the gases escaping from the upper part of the enclosure (1) towards a separating device (4) connected to the base of the enclosure by a circuit (5) for recycling the recovered particles into the fluidized bed, said apparatus comprising means (7) for controlling the solid particle concentration of the dilute phase (C) and the height of the dense phase (B), the improvement wherein the means (7) for controlling the concentration of solid particles comprise a hopper (71) for storing inert particles, a variable rate feed device (72) connecting said hopper to the circuit (5) for recycling the recovered particles, said circuit being provided with a device (50) for withdrawing the particles at a variable rate and being associated with a device (8) for controlling the feed and withdrawal rates as a function of the heat transfer requirement, responding to a change in the heat transfer requirement by a change in the same direction of the rate of supply of inert particles or a change in the opposite direction of the rate of withdrawal.
Claim 2
Dependent Claim
247 words
In apparatus for controlling the heat transfer produced between a circulating fluidized bed of solid particles and a heat-transfer fluid circulating in a heat exchanger (b) placed inside an enclosure (1) supplied with solid particles and provided at its base with means (3) for injecting an upward stream of fluidizing gas, the fluidized bed comprising a dense phase (b) with a high particle concentration and a dilute phase (C) containing fine particles entrained with the gases escaping from the upper part of the enclosure (1) towards a separating device (4) connected to the base of the enclosure by a circuit (5) for recycling the recovered particles into the fluidized bed, said apparatus comprising means (7) for controlling the solid particle concentration of the dilute phase (C) and the height of the dense phase (B), the improvement wherein the means (7) for controlling the concentration of solid particles comprise a hopper (71) for storing inert particles, a variable rate feed device (72) connecting said hopper to the circuit (5) for recycling the recovered particles, said circuit being provided with a device (50) for withdrawing the particles at a variable rate and being associated with a device (8) for controlling the feed and withdrawal rates as a function of the heat transfer requirement, responding to a change in the heat transfer requirement by a change in the same direction of the rate of supply of inert particles or a change in the opposite direction of the rate of withdrawal.
Claim 3
Dependent Claim
169 words
Steam production plant incorporating a fluidized bed boiler, said boiler comprising an enclosure (1), means for supplying said enclosure with fuel substance in the form of solid particles, a heat exchanger (6) through which water flows being located in said enclosure, and means (3) for fluidizing the solid particles by circulating an upward stream of combustive gas, means for regulating the velocity of said combustive gas so as to operate in a circulating bed, fine particles being entrained with the gases, a separating device for recovering said fine particles and for recycling them into the fluidized bed, the boiler (1) being associated with means (7) for introducing inert particles into the fluidized bed at a variable rate and means (50) for withdrawing at a variable rate particles in the recycle circuit (5), said control means (8) selectively effecting an increase in the rate of supply of inert particles or an increase in the rate of withdrawal in response, respectively, to an increase or decrease in the desired steam pressure.
Claim 4
Dependent Claim
169 words
Steam production plant incorporating a fluidized bed boiler, said boiler comprising an enclosure (1), means for supplying said enclosure with fuel substance in the form of solid particles, a heat exchanger (6) through which water flows being located in said enclosure, and means (3) for fluidizing the solid particles by circulating an upward stream of combustive gas, means for regulating the velocity of said combustive gas so as to operate in a circulating bed, fine particles being entrained with the gases, a separating device for recovering said fine particles and for recycling them into the fluidized bed, the boiler (1) being associated with means (7) for introducing inert particles into the fluidized bed at a variable rate and means (50) for withdrawing at a variable rate particles in the recycle circuit (5), said control means (8) selectively effecting an increase in the rate of supply of inert particles or an increase in the rate of withdrawal in response, respectively, to an increase or decrease in the desired steam pressure.
References Cited (Backward Citations)
FR1100221A
Cited
JPS53146001A
Cited
JPS5824710A
Cited
US4419965A
Cited
US4552203A
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US4552078A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1992-04-24 | 1992-10-24 | 1993-04-25 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1996-04-24 | 1996-10-24 | 1997-04-25 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2000-04-24 | 2000-10-24 | 2001-04-25 | $7700.00 | Window Closed / Lapsed |