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US4384614A Expired / Lapsed US ⏱️ 0.0 years remaining

Method of retorting oil shale by velocity flow of super-heated air

Assignee: Justheim Petroleum Co
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Filing: 1981-05-11
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Granted: 1983-05-24
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Expires: 2001-05-11
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Abstract

Abstract Oil shale is retorted, preferably in situ, by passing velocity flow of super-heated air through one or more conduit-like passages in direct contact with exposed surfaces of oil shale. Kerogen pyrolysis products are recovered by condensation of the vapors and collection of the condensate and by collection of the gases and separation of the valuable gases from the normally waste gases. Some of the waste gases may be recycled with the air for controlling combustion of the kerogen content of the shale.

Inventors

  • 👤 Clarence I. Justheim

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 14:54
CPC Classifications
E; E21; E21B; E21B43/00; E21B43/16; E21B43/24; E21B43/243; E21B43/247; E21B43/30; E21B43/305; E21B43/34; E21B43/35; E21B43/40

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 272 words
A process for retorting oil shale and recovering pyrolysis products therefrom, comprising forming a series of vertically spaced, conduit-like, bore passages and an insulated, substantially vertical, inflow header in successive communication with corresponding ends of said passages in a mass of oil shale for the supply of and for the flow of super-hot air as velocity streams against, along, and past said oil shale in direct contact with exposed surfaces of said oil shale, and forming a second, substantially vertical, outflow header in successive communication with the corresponding opposite ends of said passages; flowing streams of unconfined, super-hot air through said passages from a source in common by way of said inflow header, said streams having volume and velocity sufficient to entrain and carry oil shale pyrolysis products through said passages to a common location of recovery, the temperature of said air being sufficiently high to delaminate and deeply fissure the oil shale contacted by said streams between said passages and to establish intercommunication between said passages for fluid flow therebetween in contact with said oil shale; continuing the flow of said streams and entrained pyrolysis products from said passages by way of said outflow header to condensing means for vapor components of said pyrolysis products; separating from the resulting liquid condensate any solid particles entrained by said streams and entrapped by said condensate; flowing gaseous components of said streams from said condensing means to gas collecting means; separating valuable and normally waste gases from said gaseous components of the streams; and recovering both the liquid condensate, substantially free of solid particles, and said valuable gas an end products of the process.
Claim 2
Dependent Claim 272 words
A process for retorting oil shale and recovering pyrolysis products therefrom, comprising forming a series of vertically spaced, conduit-like, bore passages and an insulated, substantially vertical, inflow header in successive communication with corresponding ends of said passages in a mass of oil shale for the supply of and for the flow of super-hot air as velocity streams against, along, and past said oil shale in direct contact with exposed surfaces of said oil shale, and forming a second, substantially vertical, outflow header in successive communication with the corresponding opposite ends of said passages; flowing streams of unconfined, super-hot air through said passages from a source in common by way of said inflow header, said streams having volume and velocity sufficient to entrain and carry oil shale pyrolysis products through said passages to a common location of recovery, the temperature of said air being sufficiently high to delaminate and deeply fissure the oil shale contacted by said streams between said passages and to establish intercommunication between said passages for fluid flow therebetween in contact with said oil shale; continuing the flow of said streams and entrained pyrolysis products from said passages by way of said outflow header to condensing means for vapor components of said pyrolysis products; separating from the resulting liquid condensate any solid particles entrained by said streams and entrapped by said condensate; flowing gaseous components of said streams from said condensing means to gas collecting means; separating valuable and normally waste gases from said gaseous components of the streams; and recovering both the liquid condensate, substantially free of solid particles, and said valuable gas an end products of the process.
Claim 3
Dependent Claim 22 words
A process according to claim 1, wherein the passages are bore holes driven through a block of the oil shale in situ.
Claim 4
Dependent Claim 22 words
A process according to claims 1 or 2, wherein the temperature of the air introduced into the passages is approximately 2000° F.
Claim 5
Dependent Claim 29 words
A process according to claim 2, wherein condensing means is located at the surface and communicates with the downstream ends of the passages by way of the outflow header.
Claim 6
Dependent Claim 45 words
A process according to claim 4, wherein a sump is provided in the in situ workings for receiving any liquid flowing into or formed in the outflow header; and the liquid in said sump is brought to the surface as a crude shale oil product.
Claim 7
Dependent Claim 32 words
A process according to claim 1, wherein some of the normally waste gas is recycled with the air to control the extent of combustion of the kerogen content of the oil shale.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1986-05-23 1986-11-22 1987-05-24 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1990-05-23 1990-11-22 1991-05-24 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1994-05-23 1994-11-22 1995-05-24 $7700.00 Window Closed / Lapsed

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