US4569696A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for thermal and pneumatic treatment of granular solids
Assignee: Gas Technology Institute
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Filing: 1984-08-10
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Granted: 1986-02-11
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Expires: 2004-08-10
Abstract
Abstract Granular solids are thermally and pneumatically treated to remove organic and inorganic chemical additives which are bonded to the granular solids or in admixture with them, to provide a purified granular solid product which is suitable for reuse, for example foundry sand for use in high strength molded cores, or for other productive uses, such as landfill. Granular solid feed material is preheated in a dilute phase zone of a fluidized bed, organic chemical additives are thermally oxidized in a dense phase zone of the fluidized bed, and remaining inorganic chemical additives are separated and removed from the granular solids in a contiguous pneumatic impaction zone. The purified granular solids are removed from the pneumatic impaction zone and organic and inorganic materials are elutriated from the fluidized bed and removed from the head space.
Inventors
- 👤 William A. Sandstrom
- 👤 Jitendra G. Patel
- 👤 John R. Bush
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-23 15:00
CPC Classifications
B; B22; B22C; B22C5/00; B22C5/18; Y; Y10; Y10S; Y10S241/00; Y10S241/10
Claims Analysis
Total Claims: 19
Claim 1
Independent Claim
359 words
A process for thermally and pneumatically treating granular solids to remove organic and inorganic materials therefrom comprising: feeding said granular solids to an upper portion of a dilute phase portion of a vertical fluidized bed, said dilute phase having a density about 0.02 to about 0.05 pounds per cubic foot; passing said granular solids downward through said dilute phase portion countercurrent to an upward flowing hot oxidizing/fluidizing gas, said granular solids having an average retention time of about 0.25 to about 0.75 second in said dilute phase portion and increasing said granular solids average temperature about 200° to about 500° F. by thermal transfer with said hot oxidizing/fluidizing gas; passing said granular solids downward from said dilute phase portion to a dense phase portion of said fluidized bed, said dense phase having a density about 50 to about 70 pounds per cubic foot and maintaining said dense phase at about 1000° to about 2000° F., said granular solids having an average retention time in said dense phase sufficient for desired thermal oxidation of organic materials; passing said granular solids downward to a contiguous pneumatic physical impaction and heat recovery zone and directing said granular solids into at least one nozzle, introducing pressurized oxidizing/fluidizing gas to said nozzle(s) entraining said granular solids in a gas stream from said nozzle(s) directed toward an impaction target, impacting said gas stream carrying said granular solids on said target dislodging inorganic material adhering to said granular solids, recovering said granular solids by passing them downwardly from a lowermost said target and entraining said inorganic material in said oxidizing/fluidizing gas stream passing upwardly from an uppermost said target, said granular solids decreasing their average temperature and said gas stream increasing its average temperature thereby preheating said oxidizing/fluidizing gas stream; passing said preheated oxidizing/fluidizing gas stream with said inorganic material entrained upwardly through said dense phase portion additionally entraining said oxidized organic materialand continuing passing said oxidizing/fluidizing gas upwardly through said dilute phase portion fluidizing said bed and providing oxidant for thermal oxidation; and removing said gas entraining said inorganic and organic material from a head space above said dilute phase portion of said fluidized bed.
Claim 2
Dependent Claim
359 words
A process for thermally and pneumatically treating granular solids to remove organic and inorganic materials therefrom comprising: feeding said granular solids to an upper portion of a dilute phase portion of a vertical fluidized bed, said dilute phase having a density about 0.02 to about 0.05 pounds per cubic foot; passing said granular solids downward through said dilute phase portion countercurrent to an upward flowing hot oxidizing/fluidizing gas, said granular solids having an average retention time of about 0.25 to about 0.75 second in said dilute phase portion and increasing said granular solids average temperature about 200° to about 500° F. by thermal transfer with said hot oxidizing/fluidizing gas; passing said granular solids downward from said dilute phase portion to a dense phase portion of said fluidized bed, said dense phase having a density about 50 to about 70 pounds per cubic foot and maintaining said dense phase at about 1000° to about 2000° F., said granular solids having an average retention time in said dense phase sufficient for desired thermal oxidation of organic materials; passing said granular solids downward to a contiguous pneumatic physical impaction and heat recovery zone and directing said granular solids into at least one nozzle, introducing pressurized oxidizing/fluidizing gas to said nozzle(s) entraining said granular solids in a gas stream from said nozzle(s) directed toward an impaction target, impacting said gas stream carrying said granular solids on said target dislodging inorganic material adhering to said granular solids, recovering said granular solids by passing them downwardly from a lowermost said target and entraining said inorganic material in said oxidizing/fluidizing gas stream passing upwardly from an uppermost said target, said granular solids decreasing their average temperature and said gas stream increasing its average temperature thereby preheating said oxidizing/fluidizing gas stream; passing said preheated oxidizing/fluidizing gas stream with said inorganic material entrained upwardly through said dense phase portion additionally entraining said oxidized organic materialand continuing passing said oxidizing/fluidizing gas upwardly through said dilute phase portion fluidizing said bed and providing oxidant for thermal oxidation; and removing said gas entraining said inorganic and organic material from a head space above said dilute phase portion of said fluidized bed.
Claim 3
Dependent Claim
23 words
The process of claim 1 wherein said granular solids average retention time in said dilute phase is about 0.50 to about 0.70 second.
Claim 4
Dependent Claim
25 words
The process of claim 1 wherein said increase of said granular solids average temperature in said dilute phase is about 300° to about 400° F.
Claim 5
Dependent Claim
23 words
The process of claim 1 wherein the superficial gas velocity in said dense phase is about 1 to about 3 feet per second.
Claim 6
Dependent Claim
23 words
The process of claim 1 wherein the superficial gas velocity in said dense phase is about 1.5 to about 2.5 feet per second.
Claim 7
Dependent Claim
28 words
The process of claim 1 wherein said granular solids comprise foundry sand and the average retention time in said dense phase is about 30 to about 90 minutes.
Claim 8
Dependent Claim
24 words
The process of claim 1 wherein said contiguous pneumatic physical impaction and heat recovery zone comprises from about 1 to about 8 said nozzles.
Claim 9
Dependent Claim
24 words
The process of claim 1 wherein said contiguous pneumatic physical impaction and heat recovery zone comprises from about 2 to about 6 said nozzles.
Claim 10
Dependent Claim
26 words
The process of claim 1 wherein said gas temperature increases about 800° to about 1100° F. passing through said pneumatic physical impaction and heat recovery zone.
Claim 11
Dependent Claim
27 words
The process of claim 1 wherein said granular solids temperature decreases about 100° to about 300° F. passing through said pneumatic physical impaction and heat recovery zone.
Claim 12
Dependent Claim
27 words
The process of claim 1 wherein said gas introduced to said nozzle(s) comprises less than about two-thirds the total said oxidizing/fluidizing gas passing through said fluidized bed.
Claim 13
Dependent Claim
20 words
The process of claim 1 wherein said granular solids comprise particles about 0.1 mm to about 2.0 mm average diameters.
Claim 14
Dependent Claim
22 words
The process of claim 1 wherein said gas removed from said head space comprises about 2 to about 6 volume percent oxygen.
Claim 15
Dependent Claim
22 words
The process of claim 1 wherein said gas removed from said head space comprises about 4 to about 6 volume percent oxygen.
Claim 16
Dependent Claim
38 words
The process of claim 1 wherein said passing of granular solids downward to a contiguous pneumatic physical impaction and heat recovery zone comprises passing said solids through a Venturi conduit controlling retention of solids in said fluidized bed.
Claim 17
Dependent Claim
17 words
The process of claim 1 wherein said process is conducted at about atmospheric or slightly negative pressure.
Claim 18
Dependent Claim
21 words
The process of claim 1 wherein said process is conducted at a pressure of about -1 to about +5 inches water.
Claim 19
Dependent Claim
30 words
The process of claim 1 wherein said gas introduced to said nozzle(s) comprises about 40 to about 60 percent of the total said oxidizing/fluidizing gas passing through said fluidized bed.
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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) | 1989-02-10 | 1989-08-12 | 1990-02-11 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1993-02-10 | 1993-08-12 | 1994-02-11 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1997-02-10 | 1997-08-12 | 1998-02-11 | $7700.00 | Window Closed / Lapsed |