Patent US4006533A successfully refreshed from Google Patents.
US4006533A
Expired / Lapsed
US
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Treating gas and granular material in panel bed
Assignee: Individual
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Filing: 1974-08-28
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Granted: 1977-02-08
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Expires: 1994-08-28
Abstract
Abstract There is provided a puffback technique for cleaning a panel bed contactor suitable for chemical or physical treatment of gas and granular material. Free surfaces for entry of gas are supported cooperatively by louvers. A puffback technique is provided for cleaning the gas entry surfaces to rid them of granular material "spent" by the treatment, including accumulated dust if the treatment includes filtration to remove dust from a gas. The puffback consists of a reverse transient flow across the panel bed of an intensity moderated so that the reverse pressure differential exceeds a first critical minimum for a time interval between about 5 and 150 milliseconds (preferably less than 50 milliseconds if the treatment includes filtration) and achieves a top value beyond a second critical minimum. After the panel bed is first filled with a granular gas-treating material, the bed is preferably loosened before treating operations begin, and the loosening can be accomplished by discharging a controlled quantity of material from the bottom of the bed.
Inventors
- 👤 Arthur M. Squires
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 18:26
CPC Classifications
F; F26; F26B; F26B17/00; F26B17/12; F26B17/122; F26B3/00; F26B3/02; F26B3/06
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
337 words
A method of contacting gas and granular material with each other to effect physical or chemical treatment of at least one of them, comprising: a. arranging granular material having apertured outer walls in a bed having a plurality of transversely disposed upwardly spaced gas entry portions separated by interposed supporting members having outer and inner edges with respect to the bed wherein said gas entry portions have gas entry faces substantially contiguous with said outer edges and said bed having gas exit portions spaced from said inner edges; b. forwardly flowing gas in a substantially continuing flow during said treatment through the gas entry portions of the granular material bed and outwardly from the gas exit portions to effect said treatment of one of said gas and granular material; c. thereafter causing a transient flow of gas to move in the direction in reverse to the flow of said gas in (b); and d. causing said transient reverse flow to produce first, a rise in the pressure difference at a given rate of rise between the gas exit portions and the gas entry portions and subsequently a fall in the pressure difference between the gas exit portions and the gas entry portions, said pressure difference produced by said transient reverse flow remaining greater than a first critical minimum difference for a time interval between about 5 and about 50 milliseconds, said first critical pressure difference being that at which a steady flow of gas in said reverse direction just produces a localized spill of granular material from the gas entry faces, and the pressure difference produced by said transient reverse flow peaking to a top value beyond a second critical minimum difference, which is the pressure difference at which a transient flow of gas in the reverse direction producing said pressure difference at said given rate of rise just initiates a body movement of the granular material supported by said members toward the gas entry faces to spill a portion of the granular material from the bed.
Claim 2
Independent Claim
337 words
A method of contacting gas and granular material with each other to effect physical or chemical treatment of at least one of them, comprising: a. arranging granular material having apertured outer walls in a bed having a plurality of transversely disposed upwardly spaced gas entry portions separated by interposed supporting members having outer and inner edges with respect to the bed wherein said gas entry portions have gas entry faces substantially contiguous with said outer edges and said bed having gas exit portions spaced from said inner edges; b. forwardly flowing gas in a substantially continuing flow during said treatment through the gas entry portions of the granular material bed and outwardly from the gas exit portions to effect said treatment of one of said gas and granular material; c. thereafter causing a transient flow of gas to move in the direction in reverse to the flow of said gas in (b); and d. causing said transient reverse flow to produce first, a rise in the pressure difference at a given rate of rise between the gas exit portions and the gas entry portions and subsequently a fall in the pressure difference between the gas exit portions and the gas entry portions, said pressure difference produced by said transient reverse flow remaining greater than a first critical minimum difference for a time interval between about 5 and about 50 milliseconds, said first critical pressure difference being that at which a steady flow of gas in said reverse direction just produces a localized spill of granular material from the gas entry faces, and the pressure difference produced by said transient reverse flow peaking to a top value beyond a second critical minimum difference, which is the pressure difference at which a transient flow of gas in the reverse direction producing said pressure difference at said given rate of rise just initiates a body movement of the granular material supported by said members toward the gas entry faces to spill a portion of the granular material from the bed.
Claim 3
Independent Claim
337 words
A method of treating a gas involving the separation and removal of particulate material by means of a filter of granular material which comprises a. arranging granular material having apertured outer walls in a bed having a plurality of transversely disposed upwardly spaced gas entry portions separated by interposed supporting members having outer and inner edges with respect to the bed wherein said gas entry portions have gas entry faces substantially contiguous with said outer edges and said bed having gas exit portions spaced from said inner edges; b. forwardly flowing gas in a substantially continuing flow during said treatment through the gas entry portions of the granular material bed and outwardly from the gas exit portions to effect said treatment of one of said gas and granular material; c. thereafter causing a transient flow of gas to move in the direction in reverse to the flow of said gas in (b); and d. causing said transient reverse flow to produce first, a rise in the pressure difference at a given rate of rise between the gas exit portions and the gas entry portions and subsequently a fall in the pressure difference between the gas exit portions and the gas entry portions, said pressure difference produced by said transient reverse flow remaining greater than a first critical minimum difference for a time interval between about 5 and about 50 milliseconds, said first critical pressure difference being that at which a steady flow of gas in said reverse direction just produces a localized spill of granular material from the gas entry faces, and the pressure difference produced by said transient reverse flow peaking to a top value beyond a second critical minimum difference, which is the pressure difference at which a transient flow of gas in the reverse direction producing said pressure difference at said given rate of rise just initiates a body movement of the granular material supported by said members toward the gas entry faces to spill a portion of the granular material from the bed.
Claim 4
Independent Claim
337 words
A method of treating a gas involving the separation and removal of particulate material by means of a filter of granular material which comprises a. arranging granular material having apertured outer walls in a bed having a plurality of transversely disposed upwardly spaced gas entry portions separated by interposed supporting members having outer and inner edges with respect to the bed wherein said gas entry portions have gas entry faces substantially contiguous with said outer edges and said bed having gas exit portions spaced from said inner edges; b. forwardly flowing gas in a substantially continuing flow during said treatment through the gas entry portions of the granular material bed and outwardly from the gas exit portions to effect said treatment of one of said gas and granular material; c. thereafter causing a transient flow of gas to move in the direction in reverse to the flow of said gas in (b); and d. causing said transient reverse flow to produce first, a rise in the pressure difference at a given rate of rise between the gas exit portions and the gas entry portions and subsequently a fall in the pressure difference between the gas exit portions and the gas entry portions, said pressure difference produced by said transient reverse flow remaining greater than a first critical minimum difference for a time interval between about 5 and about 50 milliseconds, said first critical pressure difference being that at which a steady flow of gas in said reverse direction just produces a localized spill of granular material from the gas entry faces, and the pressure difference produced by said transient reverse flow peaking to a top value beyond a second critical minimum difference, which is the pressure difference at which a transient flow of gas in the reverse direction producing said pressure difference at said given rate of rise just initiates a body movement of the granular material supported by said members toward the gas entry faces to spill a portion of the granular material from the bed.
Claim 5
Dependent Claim
51 words
The method of claim 2 including the step of loosening said granular material in said bed by discharging a controlled quantity of said material from substantially the bottom of said bed to produce a downward motion of said material in the bed including material at substantially the top of the 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) | 1980-02-08 | 1980-08-09 | 1981-02-08 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-02-08 | 1984-08-09 | 1985-02-08 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-02-08 | 1988-08-09 | 1989-02-08 | $7700.00 | Window Closed / Lapsed |