IP Library Granted Patent US 9,102,864
Granted Patent B2
US 9,102,864 · App. 14/230,264 · Granted Aug 11, 2015

Extraction of hydrocarbons from hydrocarbon-containing materials and/or processing of hydrocarbon-containing materials

Inventors: Liang-tseng Fan (Manhattan, KS); Shahram Reza Shafie (Austin, TX); Julius Michael Tollas (The Woodlands, TX); William Arthur Fitzhugh Lee (Spicewood, TX)
Assignee: GREEN SOURCE HOLDINGS LLC
C09K8/64C09K8/58C10G1/04C10G21/27E21B43/16
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Quick Facts
Patent No.
US 9,102,864
App. No.
14/230,264
Granted
Aug 11, 2015
Kind
B2
Abstract

A method of extracting hydrocarbon-containing organic matter from a hydrocarbon-containing material includes the steps of providing a first liquid comprising a turpentine liquid; contacting the hydrocarbon-containing material with the turpentine liquid to form an extraction mixture; extracting the hydrocarbon material into the turpentine liquid; and separating the extracted hydrocarbon material from a residual material not extracted.

Claims (26)

1. A method for increasing recovery of hydrocarbon-containing organic matter from a production well coupled to a hydrocarbon-containing sub-surface formation, the subsurface formation comprising hydrocarbon-containing material by contacting the hydrocarbon-containing organic matter with a substantially surfactant-free non-aqueous hydrocarbon-extracting composition comprising the steps of:

providing an injection well, said injection being in fluid communication with the sub-surface formation;

providing said substantially surfactant-free non-aqueous hydrocarbon-extracting composition, wherein said composition consists essentially of a turpentine liquid;

injecting the substantially surfactant-free non-aqueous hydrocarbon-extracting composition through the injection well and into the formation, wherein the substantially surfactant-free non-aqueous hydrocarbon-extracting composition and the hydrocarbon-containing organic matter from the hydrocarbon containing sub-surface formation form an extraction mixture comprising at least a portion of the hydrocarbon-containing organic matter extracted into turpentine liquid;

recovering the extraction mixture from the formation through the production well; and

separating the extraction mixture to produce a hydrocarbon product stream and a hydrocarbon-extracting liquid stream.

2. The method of claim 1 , wherein said turpentine liquid is selected from the group consisting of natural turpentine, synthetic turpentine, mineral turpentine, pine oil, α-pinene, β-pinene, α-terpineol, β-terpineol, γ-terpineol, terpene resins, α-terpene, β-terpene, γ-terpene, geraniol, 3-carene, dipentene (p-mentha-1,8-diene), nopol, pinane, 2-pinane hydroperoxide, terpin hydrate, 2-pinanol, dihydromycenol, isoborneol, p-menthan-8-ol, a-terpinyl acetate, citronellol, p-menthan-8-yl acetate, 7-hydroxydihydrocitronellal, menthol, anethole, camphene; p-cymene, anisaldeyde, 3,7-dimethyl-1,6-octadiene, isobornyl acetate, ocimene, alloocimene, alloocimene alcohols, 2-methoxy-2,6-dimethyl-7,8-epoxyoctane, camphor, citral, 7-methoxydihydro-citronellal, 10-camphorsulphonic acid, cintronellal, menthone, and mixtures thereof.

3. The method of claim 1 , wherein said contacting comprises mixing.

4. The method of claim 1 , wherein the substantially surfactant-free non-aqueous hydrocarbon-extracting composition consists essentially of at least about 30% by volume α-terpineol and at least about 15% pinene.

5. The method of claim 1 , wherein the substantially surfactant-free non-aqueous hydrocarbon-extracting composition consists essentially of at least about 50% by volume α-terpineol and at least about 20% by volume α- and/or β-pinene.

6. The method of claim 5 , wherein the substantially surfactant-free non-aqueous hydrocarbon-extracting composition includes at least one of α-terpene, β-terpene or γ-terpene.

7. The method of claim 1 , wherein substantially surfactant-free non-aqueous hydrocarbon-extracting composition consists essentially of α-terpineol and β-terpineol, wherein the ratio of α-terpineol to β-terpineol is at least about 1.3:1.

8. The method of claim 1 , wherein the substantially surfactant-free non-aqueous hydrocarbon-extracting composition consists essentially of α-terpineol and β-terpineol, wherein the ratio of α-terpineol to α- and/or β-pinene is at least about 2:1.

9. The method of claim 1 , wherein the substantially surfactant-free non-aqueous hydrocarbon-extracting composition consists essentially of a mixture of α-terpineol, β-terpineol, α-terpene, and β-terpene.

10. The method of claim 1 , wherein the substantially surfactant-free non-aqueous hydrocarbon-extracting composition consists essentially of a mixture of α-terpineol, and α- and/or β-pinene.

11. The method of claim 1 , wherein the substantially surfactant-free non-aqueous hydrocarbon-extracting composition consists essentially of:

about 40-60% α-terpineol,

pine oil,

about 5-20% β-pinene, and

about 0-10% p-cymene.

12. The method of claim 11 , wherein said substantially surfactant-free non-aqueous hydrocarbon-extracting composition contains about 5% p-cymene.

13. The method of claim 1 , wherein the substantially surfactant-free non-aqueous hydrocarbon-extracting composition consists essentially of:

about 40-60% α-terpineol,

about 5-10% α-pinene,

about 5-20% β-pinene, and

about 0-10% p-cymene.

Assignments (1)
CHANGE OF NAME Recorded May 6, 2015
From: GREEN SOURCE ENERGY LLC
To: GREEN SOURCE HOLDINGS LLC
Reel/Frame 035599/0932 →
Continuity (7)
Division 13777430 · Feb 26, 2013
Division 12404016 · Mar 13, 2009
Continuation In Part 12298993
Continuation In Part 12174139 · Jul 16, 2008
Continuation In Part 12053126 · Mar 21, 2008
Provisional Application 60973964 · Sep 20, 2007
Related Publication 20140209303A1 · Jul 31, 2014