US4798668A — Extraction of hydrocarbon-containing solids

Claim 1

Independent Claim 122 words

A process for recovering hydrocarbon liquids from oil shale solids which comprises: (a) heating said solids in a nonoxidizing atmosphere to a temperature between about 550° F. and about 900° F. in the absence of an added liquid organic solvent to produce heat treated oil shale solids; (b) extracting hydrocarbons from said heat treated oil shale solids by contacting said solids in an extraction zone with a liquid organic solvent passed downwardly through said heat treated oil shale solids in such quantities that said solvent trickles through said solids so that there is a discontinuous liquid phase in contact with said solids through the entire extraction zone; and (c) recovering said extracted hydrocarbons from said liquid organic solvent as said hydrocarbon liquids.

Claim 2

Dependent Claim 122 words

A process for recovering hydrocarbon liquids from oil shale solids which comprises: (a) heating said solids in a nonoxidizing atmosphere to a temperature between about 550° F. and about 900° F. in the absence of an added liquid organic solvent to produce heat treated oil shale solids; (b) extracting hydrocarbons from said heat treated oil shale solids by contacting said solids in an extraction zone with a liquid organic solvent passed downwardly through said heat treated oil shale solids in such quantities that said solvent trickles through said solids so that there is a discontinuous liquid phase in contact with said solids through the entire extraction zone; and (c) recovering said extracted hydrocarbons from said liquid organic solvent as said hydrocarbon liquids.

Claim 3

Dependent Claim 32 words

A process as defined by claim 1 wherein said heat treated oil shale solids are passed horizontally through said extraction zone as said liquid organic solvent is passed downwardly through said solids.

Claim 4

Dependent Claim 26 words

A process as defined by claim 1 wherein said oil shale solids are heated in step (a) by contacting said solids with a hot nonoxidizing gas.

Claim 5

Dependent Claim 42 words

A process as defined by claim 3 wherein said hot, nonoxidizing gas comprises a gas selected from the group consisting of hydrogen, carbon dioxide, nitrogen, helium, carbon monoxide, methane, steam, an oxygen-free flue gas and a recycle gas generated within said process.

Claim 6

Dependent Claim 18 words

A process as defined by claim 3 wherein said heating step is carried out at about atmospheric pressure.

Claim 7

Dependent Claim 26 words

A process as defined by claim 3 wherein said heating step is carried out at a pressure below the critical pressure of said hot nonoxidizing gas.

Claim 8

Dependent Claim 18 words

A process as defined by claim 3 wherein said liquid organic solvent comprises liquids derived from oil shale.

Claim 9

Dependent Claim 32 words

A process as defined by claim 3 wherein said oil shale solids are contacted with said hot nonoxidizing gas in the absence of added ammonia, added amines and added condensable, hydrocarbon vapors.

Claim 10

Dependent Claim 24 words

A process as defined by claim 7 wherein said liquids derived from said oil shale boil between about 400° F. and about 850° F.

Claim 11

Dependent Claim 27 words

A process as defined by claim 1 wherein a non-oxidizing gas is passed downwardly through said heat treated oil shale solids cocurrently with said liquid organic solvent.

Claim 12

Dependent Claim 32 words

A process as defined by claim 1 wherein said heat treated oil shale solids are contacted with said liquid organic solvent in said extraction zone in the absence of an aqueous phase.

Claim 13

Dependent Claim 35 words

A process as defined by claim 11 wherein said heat treated oil shale solids are contacted with said liquid organic solvent in said extraction zone at a temperature between about ambient and about 600° F.

Claim 14

Dependent Claim 48 words

A process as defined by claim 3 including the additional step of contacting the extracted solids from step (b) with a second liquid organic solvent having a lower boiling point than the solvent used in step (b) under conditions such that additional hydrocarbons are extracted from said solids.

Claim 15

Dependent Claim 32 words

A process as defined by claim 3 wherein said heat treated oil shale solids are contacted with said liquid organic solvent in said extraction zone in the presence of an added amine.

Claim 16

Dependent Claim 138 words

A process for recovering hydrocarbon liquids from oil shale solids which comprises: (a) heating said oil shale solids to a temperature between about 550° F. and about 900° F. by contacting said solids with a hot first nonoxidizing gas in the absence of an added liquid organic solvent; (b) extracting hydrocarbons from said heat treated oil shale solids by passing a second nonoxidizing gas cocurrently with a liquid organic solvent downwardly through said heat treated oil shale solids in an extraction zone wherein the flow rates of said second nonoxidizing gas and said liquid organic solvent are such that said solvent trickles through said solids so that there is a discontinuous liquid phase in contact with said solids through the entire extraction zone; and (c) recovering said extracted hydrocarbons from said liquid organic solvent as said hydrocarbon liquids.

Claim 17

Dependent Claim 138 words

A process for recovering hydrocarbon liquids from oil shale solids which comprises: (a) heating said oil shale solids to a temperature between about 550° F. and about 900° F. by contacting said solids with a hot first nonoxidizing gas in the absence of an added liquid organic solvent; (b) extracting hydrocarbons from said heat treated oil shale solids by passing a second nonoxidizing gas cocurrently with a liquid organic solvent downwardly through said heat treated oil shale solids in an extraction zone wherein the flow rates of said second nonoxidizing gas and said liquid organic solvent are such that said solvent trickles through said solids so that there is a discontinuous liquid phase in contact with said solids through the entire extraction zone; and (c) recovering said extracted hydrocarbons from said liquid organic solvent as said hydrocarbon liquids.

Claim 18

Dependent Claim 37 words

A process as defined by claim 15 wherein said heat treated oil shale solids are passed horizontally through said extraction zone as said liquid organic solvent and said second non-oxidizing gas are passed downwardly through said solids.

Claim 19

Dependent Claim 33 words

A process as defined by claim 15 wherein said oil shale solids are contacted with said hot first nonoxidizing gas at a pressure below the critical pressure of said first hot non-oxidizing gas.

Claim 20

Dependent Claim 33 words

A process as defined by claim 15 wherein said oil shale solids are contacted with said first hot nonoxidizing gas in the absence of added ammonia, added amines and added condensable, hydrocarbon vapors.

Claim 21

Dependent Claim 34 words

A process as defined by claim 15 wherein said second nonoxidizing gas and said liquid organic solvent are passed downwardly through said heat treated oil shale solids in the absence of an aqueous phase.

Claim 22

Dependent Claim 14 words

A process as defined by claim 15 wherein said second nonoxidizing gas comprises nitrogen.

Annuity Stage	Window Opens	Payment Deadline	Surcharge Period Until	Estimated Fee	Status
3.5 Years (Year 4)	1992-01-17	1992-07-18	1993-01-17	$2000.00	Window Closed / Lapsed
7.5 Years (Year 8)	1996-01-17	1996-07-18	1997-01-17	$3760.00	Window Closed / Lapsed
11.5 Years (Year 12)	2000-01-17	2000-07-18	2001-01-17	$7700.00	Window Closed / Lapsed

Extraction of hydrocarbon-containing solids

Abstract

Inventors

Bibliographic Details

Claims Analysis

References Cited (Backward Citations)

USPTO Annuity & Maintenance Windows

Assigned Categories & Tags

Assign Category Tag