US4287023A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Waste heat recovery
Assignee: Phillips Petroleum Co
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Filing: 1979-08-23
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Granted: 1981-09-01
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Expires: 1999-08-23
Abstract
Abstract A fixed fluidized particulate solids bed heat recovery vessel or steam generator having indirect heat exchange means within a bed of fluidized carbonaceous solids, such as coke, pelleted carbon black and the like, and introduction of a gas containing entrained solids to effect fluidization of the bed of carbonaceous solids wherein in a preferred embodiment, the reaction effluent from a carbon black reaction zone comprising carbon black suspended in a non-oxidizing gas is preferably quenched, e.g., using water and/or cooled recycled reaction effluent and is then further cooled using a fluidized fixed bed of carbonaceous solids having a cooling coil within the fluidized bed.
Inventors
- 👤 William T. Cooper
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-27 21:40
CPC Classifications
F; F22; F22B; F22B31/00; F22B31/0007; F22B31/0069; C; C09; C09C; C09C1/00; C09C1/44; C09C1/48; C09C1/56; C09C1/58; F28; F28D; F28D13/00; C01; C01P; C01P2004/00; C01P2004/60; C01P2006/00; C01P2006/10; C01P2006/32; Y; Y02; Y02P; Y02P20/00; Y02P20/10
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
266 words
A process for conducting indirect heat exchange between a gas stream containing suspended light solids and a heat exchange fluid in an indirect heat exchange zone containing fluidized fixed bed solids which comprises: (a) introducing a gas stream containing entrained solids into an inlet connected to a lower portion of an enlarged heat exchange zone containing a fluidized fixed bed of particulate carbonaceous solids and a heat exchange coil extending into said fluidized bed and having a heat exchange fluid flowing through said coil, said heat exchange zone being so sized that the actual gas passage space in said enlarged zone occupied by said fluidized fixed bed is substantially the same cross-sectional area as that of the gas inlet and gas outlet which prevents the suspended solids from accumulating in the fluidized bed and allows the suspended solids to flow in an entrained manner in the gas stream, (b) flowing said gas stream through said fluidized bed of particulate carbonaceous solids at a flow rate sufficient to maintain fluidized conditions and at a rate such that said gas is heated or cooled by the heat exchange fluid in said coil, (c) removing said gas stream containing suspended solids at a different temperature from an upper portion of said heat exchange zone, (d) passing said gas stream containing suspended solids to a gas-solids separation zone to separate suspended solids therefrom and recover cooled gas substantially reduced in suspended solids content, and (e) quenching said gas stream containing entrained solids prior to step (a) with water and at least a portion of said cooled gas recovered in (d).
Claim 2
Dependent Claim
266 words
A process for conducting indirect heat exchange between a gas stream containing suspended light solids and a heat exchange fluid in an indirect heat exchange zone containing fluidized fixed bed solids which comprises: (a) introducing a gas stream containing entrained solids into an inlet connected to a lower portion of an enlarged heat exchange zone containing a fluidized fixed bed of particulate carbonaceous solids and a heat exchange coil extending into said fluidized bed and having a heat exchange fluid flowing through said coil, said heat exchange zone being so sized that the actual gas passage space in said enlarged zone occupied by said fluidized fixed bed is substantially the same cross-sectional area as that of the gas inlet and gas outlet which prevents the suspended solids from accumulating in the fluidized bed and allows the suspended solids to flow in an entrained manner in the gas stream, (b) flowing said gas stream through said fluidized bed of particulate carbonaceous solids at a flow rate sufficient to maintain fluidized conditions and at a rate such that said gas is heated or cooled by the heat exchange fluid in said coil, (c) removing said gas stream containing suspended solids at a different temperature from an upper portion of said heat exchange zone, (d) passing said gas stream containing suspended solids to a gas-solids separation zone to separate suspended solids therefrom and recover cooled gas substantially reduced in suspended solids content, and (e) quenching said gas stream containing entrained solids prior to step (a) with water and at least a portion of said cooled gas recovered in (d).
Claim 3
Dependent Claim
20 words
A process according to claim 1 wherein said gas stream is at a higher temperature than said heat exchange fluid.
Claim 4
Dependent Claim
34 words
A process according to claim 1 wherein said gas stream contains suspended carbon black and the inlet temperature of said gas stream is about 2000° F. and the outlet temperature is about 1200° F.
Claim 5
Dependent Claim
40 words
A process according to claim 1 wherein said fluidized particulate carbonaceous solid is coke, said gas stream is at a substantially higher temperature than said heat exchange fluid, and said heat exchange fluid is water which is converted to steam.
Claim 6
Dependent Claim
14 words
A process according to claim 4 wherein said fluidized coke is calcined petroleum coke.
Claim 7
Dependent Claim
42 words
A process according to claim 1 wherein said fluidized particulate carbonaceous solid is pelleted carbon black, said gas stream is at a substantially higher temperature than said heat exchange fluid, and said heat exchange fluid is water which is converted to steam.
Claim 8
Dependent Claim
25 words
A process according to claim 1 wherein the solids separated from said gas in said gas-solids separation zone is passed to wet pelleting and drying.
Claim 9
Dependent Claim
24 words
A process according to claim 7 wherein said gas stream contains suspended carbon black and said fluidized bed is coke or pelleted carbon black.
Claim 10
Dependent Claim
14 words
A process according to claim 8 wherein said fluidized bed is calcined petroleum coke.
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) | 1984-08-31 | 1985-03-02 | 1985-09-01 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-08-31 | 1989-03-02 | 1989-09-01 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-08-31 | 1993-03-02 | 1993-09-01 | $7700.00 | Window Closed / Lapsed |