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US4320795A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for heat transfer with dilute phase fluidized bed

Assignee: Shell USA Inc
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Filing: 1977-03-14
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Granted: 1982-03-23
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Expires: 1997-03-14
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Abstract

Abstract A process for the transfer of heat between solids is described in which a particulate solid is allowed to fall at a substantially uniform rate through a dilute phase fluidized bed of another particulate solid.

Inventors

  • 👤 John E. Gwyn
  • 👤 Scott C. Roberts

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-27 19:02
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/02

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 142 words
Process for the transfer of heat between solid materials comprising, providing a relatively hot particulate heat carrier, countercurrently contacting a solid material subdivided to a particle size fluidizable in gas in the form of an upwardly moving dilute phase fluidized mass in gas in a vertically-oriented heat exchange zone with the relatively hot particulate heat carrier, the heat carrier being introduced in the upper portion of the heat exchange zone and having a particle size and density such that it falls through the dilute phase fluidized mass at a substantially uniform rate, and collects in the lower portion of the heat exchange zone as a relatively cool particulate heat carrier, the contacting producing a solid material at elevated temperature, removing the relatively cool heat carrier, and removing the solid material at elevated temperature from the upper portion of the heat exchange zone.
Claim 2
Dependent Claim 142 words
Process for the transfer of heat between solid materials comprising, providing a relatively hot particulate heat carrier, countercurrently contacting a solid material subdivided to a particle size fluidizable in gas in the form of an upwardly moving dilute phase fluidized mass in gas in a vertically-oriented heat exchange zone with the relatively hot particulate heat carrier, the heat carrier being introduced in the upper portion of the heat exchange zone and having a particle size and density such that it falls through the dilute phase fluidized mass at a substantially uniform rate, and collects in the lower portion of the heat exchange zone as a relatively cool particulate heat carrier, the contacting producing a solid material at elevated temperature, removing the relatively cool heat carrier, and removing the solid material at elevated temperature from the upper portion of the heat exchange zone.
Claim 3
Dependent Claim 146 words
Process for the transfer of heat between solid particles comprising, providing a relatively cool particulate heat carrier, countercurrently contacting a solid material having an elevated temperature and subdivided to a particle size fluidizable in gas in the form of a relatively hot upwardly moving dilute-phase fluidized mass in gas in a vertically-oriented heat exchange zone with the relatively cool particulate heat carrier, the heat carrier being introduced in the upper portion of the heat exchange zone and having a particle size and density such that it falls through the dilute phase fluidized mass at a substantially uniform rate, and collects in the lower portion of the heat exchange zone as a relatively warm particulate heat carrier, the contacting producing a relatively cool solid material, removing the relatively warm heat carrier, and removing the relatively cool solid material from the upper portion of the heat exchange zone.
Claim 4
Dependent Claim 146 words
Process for the transfer of heat between solid particles comprising, providing a relatively cool particulate heat carrier, countercurrently contacting a solid material having an elevated temperature and subdivided to a particle size fluidizable in gas in the form of a relatively hot upwardly moving dilute-phase fluidized mass in gas in a vertically-oriented heat exchange zone with the relatively cool particulate heat carrier, the heat carrier being introduced in the upper portion of the heat exchange zone and having a particle size and density such that it falls through the dilute phase fluidized mass at a substantially uniform rate, and collects in the lower portion of the heat exchange zone as a relatively warm particulate heat carrier, the contacting producing a relatively cool solid material, removing the relatively warm heat carrier, and removing the relatively cool solid material from the upper portion of the heat exchange zone.
Claim 5
Dependent Claim 13 words
The method of claim 1 wherein the subdivided solid material is oil shale.
Claim 6
Dependent Claim 13 words
The method of claim 2 wherein the subdivided solid material is oil shale.

References Cited (Backward Citations)

US2725348A Cited
US2741549A Cited
US2743216A Cited
US2776935A Cited
US2955077A Cited
FR1487133A Cited
US3855070A Cited
US3921307A Cited
US4064018A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1985-03-22 1985-09-21 1986-03-23 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1989-03-22 1989-09-21 1990-03-23 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1993-03-22 1993-09-21 1994-03-23 $7700.00 Window Closed / Lapsed

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