US4674560A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process and apparatus for control of the heat transfer produced in a fluidized bed
Assignee: Areva NP SAS
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Filing: 1985-03-07
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Granted: 1987-06-23
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Expires: 2005-03-07
Abstract
Abstract Process and 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
2026-11-04 08:20
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: 3
Claim 1
Independent Claim
198 words
Process for the control of heat transfer between a circulating bed of solid particles and a heat exchanger (6) placed inside an enclosure (1) supplied with solid particles, provided at its base with means (3) for fluidizing the particles by circulation of an upward stream of gas at a controllable velocity and connected to a device (4) for recovering particles of sufficiently fine particle size to be entrained with the gases, taking into account the velocity of the latter, at least a part of the recovered particles being reintroduced into the fluidized bed via a recycle circuit (5), the heat exchange coefficient of the exchanger (6) being placed at each moment to the heat transfer demand of the plant by varying in the same direction the concentration of solid particles in the circulating bed, said process including the steps of (a) increasing the concentration of particles in the circulating bed by introducing into the recycle circuit (5) a controlled flow of inert particles of a particle size sufficiently fine so that they may be entrained with the gases; and (b) reducing the concentration of the circulating bed by withdrawing a controlled flow of particles from the recycle circuit.
Claim 2
Dependent Claim
198 words
Process for the control of heat transfer between a circulating bed of solid particles and a heat exchanger (6) placed inside an enclosure (1) supplied with solid particles, provided at its base with means (3) for fluidizing the particles by circulation of an upward stream of gas at a controllable velocity and connected to a device (4) for recovering particles of sufficiently fine particle size to be entrained with the gases, taking into account the velocity of the latter, at least a part of the recovered particles being reintroduced into the fluidized bed via a recycle circuit (5), the heat exchange coefficient of the exchanger (6) being placed at each moment to the heat transfer demand of the plant by varying in the same direction the concentration of solid particles in the circulating bed, said process including the steps of (a) increasing the concentration of particles in the circulating bed by introducing into the recycle circuit (5) a controlled flow of inert particles of a particle size sufficiently fine so that they may be entrained with the gases; and (b) reducing the concentration of the circulating bed by withdrawing a controlled flow of particles from the recycle circuit.
Claim 3
Dependent Claim
81 words
Control process as claimed in claim 1, including the steps of (a) subjecting the substance to be treated in the fluidized bed to a reaction producing fine residues which are entrained with the gases and are withdrawn from the recycle circuit by a variable-rate withdrawal device (50); and (b) changing the withdrawal rate of the residues in the direction opposite to the desired change in the heat transfer coefficient to maintain the required concentration of fine particles in the fluidized bed.
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) | 1990-06-22 | 1990-12-22 | 1991-06-23 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1994-06-22 | 1994-12-22 | 1995-06-23 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1998-06-22 | 1998-12-22 | 1999-06-23 | $7700.00 | Window Closed / Lapsed |