US4137053A
Expired / Lapsed
US
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Gasification process
Assignee: Chevron USA Inc
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Filing: 1978-03-17
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Granted: 1979-01-30
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Expires: 1998-03-17
Abstract
Abstract A continuous process and apparatus are disclosed for the retorting or gasification of hydrocarbon-containing solids such as oil shale, coal, tar sands, etc., wherein the solids are retorted or gasified in a combined entrained and fluidized bed. A solid fluidized heat-transfer material flows downwardly through a conversion zone. Subdivided hydrocarbon-containing solids are introduced into a central portion of the conversion zone, with smaller particles of the solids being entrained and moving upwardly through the conversion zone countercurrent to the flow of the fluidized heat-transfer material, and larger particles of the solids being fluidized and moving downwardly through the conversion zone concurrent with the flow of the heat-transfer material. A fluidizing gas is injected into a lower portion of the conversion zone and a portion of the solids is combusted, providing the necessary heat for the conversion reactions. Substantially plug flow of the heat-transfer solid and the hydrocarbon-containing solids is maintained by including in the conversion zone means for impeding back mixing, such as a packing material filling the conversion zone.
Inventors
- 👤 David S. Mitchell
- 👤 David R. Sageman
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-27 16:04
CPC Classifications
C; C10; C10J; C10J3/00; C10J3/46; C10J3/54; C10J3/48; C10J3/485; C10J3/72; C10J3/74; C10J3/82; C10J3/84; C10J2300/00; C10J2300/09; C10J2300/0913; C10J2300/093; C10J2300/0946; C10J2300/0953; C10J2300/0956; C10J2300/0959; C10J2300/0966; C10J2300/0969; C10J2300/0973; C10J2300/0976; C10J2300/0983; C10J2300/0993; C10J2300/18; C10J2300/1807; C10J2300/1846
Claims Analysis
Total Claims: 14
Claim 1
Independent Claim
299 words
A continuous process for gasifying hydrocarbon-containing solids in a vertically elongated gasification zone, said gasification zone including means for substantially impeding vertical back mixing of vertically moving solids substantially throughout said gasification zone, which comprises: (a) introducing particulate solid heat-transfer material at an elevated temperature into an upper portion of said gasification zone; (b) maintaining an upward flow of a steam-containing fluidization gas through said gasification zone at a rate sufficient to maintain said heat-transfer material in a fluidized state; (c) introducing into an intermediate level of said gasification zone a first portion of hydrocarbon-containing solids which is entrained by said fluidization gas and flows upwardly in plug flow through said gasification zone and reacts with said fluidization gas forming a first portion of partially gasified solids and a first portion of combustible gas; (d) introducing into an intermediate level of said gasification zone a second portion of hydrocarbon-containing solids which is fluidized by said fluidization gas and which reacts with said fluidization gas forming a second portion of partially gasified solids and a second portion of combustible gas; (e) reacting said second portion of said partially gasified solids in a lower level of said gasification zone with an oxygen-containing gas thereby forming combusted solids and a noncombustion-supporting fluidization gas, whereby said heat-transfer material is heated to an elevated temperature; (f) maintaining a substantially net downward plug flow of said heat-transfer material and said second portion of said hydrocarbon-containing solids through said gasification zone by withdrawing from a bottom portion of said gasification zone a first effluent stream comprising said heat-transfer material, said effluent stream being withdrawn at an elevated temperature; (g) withdrawing from an upper portion of said gasification zone a second effluent stream comprising a product combustible gas and said first portion of said partially gasified solids.
Claim 2
Dependent Claim
299 words
A continuous process for gasifying hydrocarbon-containing solids in a vertically elongated gasification zone, said gasification zone including means for substantially impeding vertical back mixing of vertically moving solids substantially throughout said gasification zone, which comprises: (a) introducing particulate solid heat-transfer material at an elevated temperature into an upper portion of said gasification zone; (b) maintaining an upward flow of a steam-containing fluidization gas through said gasification zone at a rate sufficient to maintain said heat-transfer material in a fluidized state; (c) introducing into an intermediate level of said gasification zone a first portion of hydrocarbon-containing solids which is entrained by said fluidization gas and flows upwardly in plug flow through said gasification zone and reacts with said fluidization gas forming a first portion of partially gasified solids and a first portion of combustible gas; (d) introducing into an intermediate level of said gasification zone a second portion of hydrocarbon-containing solids which is fluidized by said fluidization gas and which reacts with said fluidization gas forming a second portion of partially gasified solids and a second portion of combustible gas; (e) reacting said second portion of said partially gasified solids in a lower level of said gasification zone with an oxygen-containing gas thereby forming combusted solids and a noncombustion-supporting fluidization gas, whereby said heat-transfer material is heated to an elevated temperature; (f) maintaining a substantially net downward plug flow of said heat-transfer material and said second portion of said hydrocarbon-containing solids through said gasification zone by withdrawing from a bottom portion of said gasification zone a first effluent stream comprising said heat-transfer material, said effluent stream being withdrawn at an elevated temperature; (g) withdrawing from an upper portion of said gasification zone a second effluent stream comprising a product combustible gas and said first portion of said partially gasified solids.
Claim 3
Dependent Claim
17 words
The process of claim 1 wherein said hydrocarbon-containing solids comprise coal and said heat-transfer material comprises sand.
Claim 4
Dependent Claim
48 words
The process of claim 2 comprising the additional step of introducing said first portion of said partially gasified solids into a lower portion of said gasification zone, whereby said first portion of said partially gasified solids is combusted and entrained through said gasification zone by said fluidization gas.
Claim 5
Dependent Claim
22 words
The process of claim 1 wherein said first portion of said solids comprises 5 to 60 weight percent of said hydrocarbon-containing solids.
Claim 6
Dependent Claim
22 words
The process of claim 1 wherein said first portion of said solids comprises 20 to 50 weight percent of said hydrocarbon-containing solids.
Claim 7
Dependent Claim
275 words
A continuous process for gasifying hydrocarbon-containing solids in a vertically elongated vessel substantially filled with a packing material, which comprises: (a) introducing particulate solid heat-transfer material at an elevated temperature into an upper portion of said vessel; (b) maintaining an upward flow of a steam-containing fluidization gas through said vessel at a rate sufficient to maintain said heat-transfer material in a fluidized state; (c) introducing into an intermediate level of said vessel a first portion of hydrocarbon-containing solids which is entrained by said fluidization gas and flows upwardly in plug flow through said vessel and reacts with said fluidization gas forming a first portion of partially gasified solids and a first portion of combustible gas; (d) introducing into an intermediate level of said vessel a second portion of hydrocarbon-containing solids which is fluidized by said fluidization gas and which reacts with said fluidization gas forming a second portion of partially gasified solids and a second portion of combustible gas; (e) reacting said second portion of said partially gasified solids in a lower level of said vessel with an oxygen-containing gas thereby forming combusted solids, a noncombustion-supporting fluidization gas, and whereby said heat-transfer material is heated to an elevated temperature; (f) maintaining a substantially net downward plug flow of said heat-transfer material and said second portion of said hydrocarbon-containing solids through said vessel by withdrawing from a bottom portion of said vessel a first effluent stream comprising said heat-transfer material, said effluent stream being withdrawn at an elevated temperature; (g) withdrawing from an upper portion of said vessel a second effluent stream comprising a product combustible gas and said first portion of said partially gasified solids.
Claim 8
Dependent Claim
275 words
A continuous process for gasifying hydrocarbon-containing solids in a vertically elongated vessel substantially filled with a packing material, which comprises: (a) introducing particulate solid heat-transfer material at an elevated temperature into an upper portion of said vessel; (b) maintaining an upward flow of a steam-containing fluidization gas through said vessel at a rate sufficient to maintain said heat-transfer material in a fluidized state; (c) introducing into an intermediate level of said vessel a first portion of hydrocarbon-containing solids which is entrained by said fluidization gas and flows upwardly in plug flow through said vessel and reacts with said fluidization gas forming a first portion of partially gasified solids and a first portion of combustible gas; (d) introducing into an intermediate level of said vessel a second portion of hydrocarbon-containing solids which is fluidized by said fluidization gas and which reacts with said fluidization gas forming a second portion of partially gasified solids and a second portion of combustible gas; (e) reacting said second portion of said partially gasified solids in a lower level of said vessel with an oxygen-containing gas thereby forming combusted solids, a noncombustion-supporting fluidization gas, and whereby said heat-transfer material is heated to an elevated temperature; (f) maintaining a substantially net downward plug flow of said heat-transfer material and said second portion of said hydrocarbon-containing solids through said vessel by withdrawing from a bottom portion of said vessel a first effluent stream comprising said heat-transfer material, said effluent stream being withdrawn at an elevated temperature; (g) withdrawing from an upper portion of said vessel a second effluent stream comprising a product combustible gas and said first portion of said partially gasified solids.
Claim 9
Dependent Claim
17 words
The process of claim 6 wherein said hydrocarbon-containing solids comprise coal and said heat-transfer material comprises sand.
Claim 10
Dependent Claim
46 words
The process of claim 7 comprising the additional step of introducing said first portion of said partially gasified solids into a lower portion of said vessel, whereby said first portion of said partially gasified solids is combusted and entrained through said vessel by said fluidization gas.
Claim 11
Dependent Claim
22 words
The process of claim 6 wherein said first portion of said solids comprises 20 to 60 weight percent of said hydrocarbon-containing solids.
Claim 12
Dependent Claim
22 words
The process of claim 6 wherein said first portion of said solids comprises 20 to 50 weight percent of said hydrocarbon-containing solids.
Claim 13
Dependent Claim
252 words
A process for gasifying hydrocarbon-containing solids in a vertically elongated gasification zone, said gasification zone containing means for impeding vertical back mixing of vertically moving solids substantially throughout said gasification zone, which comprises the steps of: (a) introducing particulate solid heat-transfer material into an upper end of said gasification zone at an elevated temperature and withdrawing heat-transfer material from a lower end of said gasification zone; (b) passing a fluidization gas stream upwardly through said gasification zone at a rate sufficient to substantially fluidize said heat-transfer material, whereby said heat-transfer material substantially flows downwardly through said gasification zone in plug flow; (c) introducing said hydrocarbon-containing solids into an intermediate vertical level of said gasification zone, said fluidization gas stream having a superficial velocity such that a first portion of said hydrocarbon-containing solids is entrained in said fluidization gas stream and flows upwardly in plug flow through said gasification zone and a second portion of said hydrocarbon-containing solids is fluidized by said fluidization gas stream and flows downwardly through said gasification zone with said heat-transfer material; (d) heating said hydrocarbon-containing solids and forming a product gas and partially gasified solids by contacting said hydrocarbon-containing solids with steam in said fluidization gas stream and with said heat-transfer material; (e) heating said heat transfer material and said fluidization gas stream by combusting downwardly flowing partially gasified solids formed from said second portion of said hydrocarbon-containing solids; and (f) removing said product gas from said upper end of said gasification zone in said fluidization gas stream.
Claim 14
Dependent Claim
252 words
A process for gasifying hydrocarbon-containing solids in a vertically elongated gasification zone, said gasification zone containing means for impeding vertical back mixing of vertically moving solids substantially throughout said gasification zone, which comprises the steps of: (a) introducing particulate solid heat-transfer material into an upper end of said gasification zone at an elevated temperature and withdrawing heat-transfer material from a lower end of said gasification zone; (b) passing a fluidization gas stream upwardly through said gasification zone at a rate sufficient to substantially fluidize said heat-transfer material, whereby said heat-transfer material substantially flows downwardly through said gasification zone in plug flow; (c) introducing said hydrocarbon-containing solids into an intermediate vertical level of said gasification zone, said fluidization gas stream having a superficial velocity such that a first portion of said hydrocarbon-containing solids is entrained in said fluidization gas stream and flows upwardly in plug flow through said gasification zone and a second portion of said hydrocarbon-containing solids is fluidized by said fluidization gas stream and flows downwardly through said gasification zone with said heat-transfer material; (d) heating said hydrocarbon-containing solids and forming a product gas and partially gasified solids by contacting said hydrocarbon-containing solids with steam in said fluidization gas stream and with said heat-transfer material; (e) heating said heat transfer material and said fluidization gas stream by combusting downwardly flowing partially gasified solids formed from said second portion of said hydrocarbon-containing solids; and (f) removing said product gas from said upper end of said gasification zone in said fluidization gas stream.
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) | 1982-01-29 | 1982-07-31 | 1983-01-30 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1986-01-29 | 1986-07-31 | 1987-01-30 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1990-01-29 | 1990-07-31 | 1991-01-30 | $7700.00 | Window Closed / Lapsed |