US3856441A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Apparatus for pelletizing powdered solid substance in a fluidized bed
Assignee: Ube Corp
•
Filing: 1972-11-03
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Granted: 1974-12-24
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Expires: 1992-11-03
Abstract
Abstract A method of pelletizing powdered solid substance in a fluidized bed in which powdered solid substance is fed and liquid substance is atomized and a gas jet stream for the selective discharge is injected through a selective discharge opening provided at the center portion of a funnel shaped gas distributor to discharge selectively the coarse final pellets. The gas jet stream sets the solid particles in the bed into a forced circulation flow which has the essential role in dispersing powdered solid and liquid substance throughout the bed as well as the role in said selective discharge process.
Inventors
- 👤 Y Suzukawa
- 👤 H Kono
- 👤 A Kuribayashi
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-26 13:32
CPC Classifications
B; B01; B01J; B01J2/00; B01J2/16; C; C22; C22B; C22B1/00; C22B1/14; C22B1/24; C22B1/2406; Y; Y10; Y10S; Y10S264/00; Y10S264/51
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
335 words
Apparatus for pelletizing a powdery solid substance by causing agglomeration to produce pellets of a predetermined minimum size, the combination of, a fluidizing vessel enclosing a fluidizing zone comprising side walls surrounding the periphery of said zone and a bottom wall structure defining the bottom of said zone, said vessel having a bottom pellet-discharge opening and said bottom wall structure extending downwardly toward said opening from said side walls at an acute angle to the horizontal, said bottom wall structure having gas-discharge openings for fluidizing gas, means to supply fluidizing gas through said gas discharge openings, means providing a vertical passageway extending upwardly to and concentric with said pellet-discharge opening, means directing a stream of fluidizing gas upwardly through said passageway at a controlled rate, means for delivering the powdery solid substance at a controlled rate into said vessel, means to deliver an agglomerating liquid to a zone within said vessel remote from said side walls and bottom wall structure, said stream of fluidizing gas being effective to produce an upward flow of gas from said pellet discharge opening and said first-mentioned fluidizing gas cooperating therewith to produce and maintain a fluidizing gas pattern throughout said fluidizing zone with the flow being upwardly from said pelletdischarge opening and thence horizontally to the upper portion of said side wall structure and thence downwardly past said side wall structure and thence along said bottom wall structure generally toward said pellet-discharge opening to complete the path, whereby the powdery solid substance and said liquid are entrained into said fluidizing gas and the liquid wets and agglomerates the powdery solid substance to form pellets the size of which is increased by surface wetting and contact with additional fragments of the solid substance, said stream of fluidizing gas flowing upwardly through said passageway at a controlled rate such that pellets which are smaller than said minimum size are carried upwardly into said fluidized zone and pellets of said minimum size are discharged through said passageway by the action of gravity.
Claim 2
Dependent Claim
335 words
Apparatus for pelletizing a powdery solid substance by causing agglomeration to produce pellets of a predetermined minimum size, the combination of, a fluidizing vessel enclosing a fluidizing zone comprising side walls surrounding the periphery of said zone and a bottom wall structure defining the bottom of said zone, said vessel having a bottom pellet-discharge opening and said bottom wall structure extending downwardly toward said opening from said side walls at an acute angle to the horizontal, said bottom wall structure having gas-discharge openings for fluidizing gas, means to supply fluidizing gas through said gas discharge openings, means providing a vertical passageway extending upwardly to and concentric with said pellet-discharge opening, means directing a stream of fluidizing gas upwardly through said passageway at a controlled rate, means for delivering the powdery solid substance at a controlled rate into said vessel, means to deliver an agglomerating liquid to a zone within said vessel remote from said side walls and bottom wall structure, said stream of fluidizing gas being effective to produce an upward flow of gas from said pellet discharge opening and said first-mentioned fluidizing gas cooperating therewith to produce and maintain a fluidizing gas pattern throughout said fluidizing zone with the flow being upwardly from said pelletdischarge opening and thence horizontally to the upper portion of said side wall structure and thence downwardly past said side wall structure and thence along said bottom wall structure generally toward said pellet-discharge opening to complete the path, whereby the powdery solid substance and said liquid are entrained into said fluidizing gas and the liquid wets and agglomerates the powdery solid substance to form pellets the size of which is increased by surface wetting and contact with additional fragments of the solid substance, said stream of fluidizing gas flowing upwardly through said passageway at a controlled rate such that pellets which are smaller than said minimum size are carried upwardly into said fluidized zone and pellets of said minimum size are discharged through said passageway by the action of gravity.
Claim 3
Dependent Claim
50 words
Apparatus as described in claim 1 wherein said vessel has a gas-discharge outlet at a level above the top of said fluidizing zone, means to separate the solid discharged with gas through said gas-discharge opening and to exhaust the gas and deliver the solid substance back to said fluidizing zone.
Claim 4
Dependent Claim
29 words
Apparatus as described in claim 1 which includes means to supply gas under pressure with said powdery solid substance, and means to supply gas under pressure with said liquid.
Claim 5
Dependent Claim
27 words
Apparatus as described in claim 1 which includes means to collect and remove the pellets which pass downwardly through said passageway, and means to dry the pellets.
Claim 6
Dependent Claim
25 words
Apparatus as described in claim 1 wherein said bottom wall structure comprises a funnel shaped gas distributor with gas discharge openings throughout a frustoconical area.
Claim 7
Dependent Claim
34 words
Apparatus as described in claim 5 which includes a funnel shaped pellet collector positioned to receive the discharged pellets, and valve means to control the discharge of pellets from the bottom of said collector.
Claim 8
Dependent Claim
58 words
Apparatus as described in claim 6 wherein said collector includes means comprising a chamber which is closed except for the gas receiving passageway and for the bottom of said vertical passageway from said pellet-discharge opening through which pellets are discharged and gas flows upwardly, and means to supply a stream of gas to the enclosure formed by collector.
Claim 9
Dependent Claim
32 words
Apparatus as described in claim 7 wherein said liquid is discharged in a vertical direction, and means to supply a jet of gas in an annular stream around the liquid being discharged.
Claim 10
Dependent Claim
39 words
Apparatus as described in claim 7 wherein said solid substance is delivered into said vessel at substantially the top of said bottom wall structure, and means to provide a stream of gas into said vessel with said solid substance.
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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) | 1977-12-23 | 1978-06-24 | 1978-12-24 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1981-12-23 | 1982-06-24 | 1982-12-24 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1985-12-23 | 1986-06-24 | 1986-12-24 | $7700.00 | Window Closed / Lapsed |