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US3783528A Expired / Lapsed US ⏱️ 0.0 years remaining

Reactor staging

Assignee: Badger Co Inc
•
Filing: 1971-01-05
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Granted: 1974-01-08
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Expires: 1991-01-05
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Abstract

Abstract Catalyst staging of a fluidized catalyst bed in a reactor is achieved by providing horizontal ridges or flanges which interrupt downward flow of catalyst as a dense layer along vertical interior surfaces of the reactor.

Inventors

  • 👤 H Sheely

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-26 02:07
CPC Classifications
B; B01; B01J; B01J8/00; B01J8/18; B01J8/24; B01J8/26; B01J8/28; B01J8/005; B01J8/0055; B01J8/006; B01J8/1836; C; C07; C07C; C07C17/00; C07C17/093; C07C17/15; B01J2208/00; B01J2208/00008; B01J2208/00017; B01J2208/00106; B01J2208/00115; B01J2208/00132; B01J2208/00141; B01J2208/00327; B01J2208/00336; B01J2208/00353; B01J2208/00796; B01J2208/00823; B01J2208/00831; B01J2208/0084

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 216 words
Apparatus comprising in combination a vertical elongate vessel adapted to contain a body of subdivided solids, means for introducing a stream of gas into the bottom of said vessel at a velocity sufficient to maintain said body of solids in a dense turbulent fluidized state, means for withdrawing a stream of gas from the upper portion of said vessel, and means for dividing said fluidized body into at least two stages with limited downflow of solids from a higher stage to a lower stage, said means comprising a plurality of substantially continuous ridges on an inner vertical surface of said vessel surrounding said body, said ridges being spaced along said vertical surface with the spacing of said ridges being in the range of 6 to 12 inches for a vessel internal diameter of up to 3 feet and in the range of 1 to 3 feet for a vessel internal diameter in excess of 3 feet, each of said ridges comprising a single substantially horizontally extending ring having one edge flush with said surface and another edge that projects from said surface a distance in the range of one-half to 2 inches sufficient for said ring to interrupt downflow of subdivided solids along said surface without materially increasing the resistance to gas flow through said vessel.
Claim 2
Dependent Claim 216 words
Apparatus comprising in combination a vertical elongate vessel adapted to contain a body of subdivided solids, means for introducing a stream of gas into the bottom of said vessel at a velocity sufficient to maintain said body of solids in a dense turbulent fluidized state, means for withdrawing a stream of gas from the upper portion of said vessel, and means for dividing said fluidized body into at least two stages with limited downflow of solids from a higher stage to a lower stage, said means comprising a plurality of substantially continuous ridges on an inner vertical surface of said vessel surrounding said body, said ridges being spaced along said vertical surface with the spacing of said ridges being in the range of 6 to 12 inches for a vessel internal diameter of up to 3 feet and in the range of 1 to 3 feet for a vessel internal diameter in excess of 3 feet, each of said ridges comprising a single substantially horizontally extending ring having one edge flush with said surface and another edge that projects from said surface a distance in the range of one-half to 2 inches sufficient for said ring to interrupt downflow of subdivided solids along said surface without materially increasing the resistance to gas flow through said vessel.

References Cited (Backward Citations)

US2581134A Cited
US2655273A Cited
US2750681A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1977-01-07 1977-07-09 1978-01-08 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1981-01-07 1981-07-09 1982-01-08 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1985-01-07 1985-07-09 1986-01-08 $7700.00 Window Closed / Lapsed

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