IP Library Granted Patent US 12,043,796
Granted Patent B2
US 12,043,796 · App. 17/431,882 · Granted Jul 23, 2024

Injection fluids comprising alkoxylated alcohols and the use of such fluids in oil recovery processes

Inventors: Renke Rommerskirchen (Nottuln, DE); Thomas Sottmann (Stuttgart, DE); Harun Bilgili (Stuttgart, DE); Julian Fischer (Stuttgart, DE)
Assignee: Sasol Chemie GmbH & Co KG
C09K8/594
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Quick Facts
Patent No.
US 12,043,796
App. No.
17/431,882
Granted
Jul 23, 2024
Kind
B2
Abstract

The present invention is concerned with an injection fluid comprising liquid or super-critical carbon dioxide (CO 2 ) and alkoxylated alcohols and the use of such fluids in oil recovery processes. More specifically, the invention it relates to the reduction of the miscibility pressure during CO 2 injection oil recovery processes by the use of alkox-ylated alcohols. Further, the invention relates to an oil recovery process injecting CO 2 and alkoxylated alcohols.

Claims (72)

1. A method for flooding of oil wells by carbon dioxide injection, the method comprising:

i) providing an injection fluid comprising one or more alkoxylated alcohols having the following structure:

R—O-(AO) m+n —H  (I)

wherein

R is a linear alkyl group having from C4 to C8 carbon atoms, and/or a branched alkyl group having from C4 to C18 carbon atoms;

AO is EO and/or PO, independent of each m or n;

m is 0 to 12;

n is 0 to 12; and

m+n is at least 1;

and at least liquid or supercritical carbon dioxide;

ii) injecting the injection fluid into a reservoir comprising a hydrocarbonaceous fluid, the reservoir being operated at a pressure below the minimum miscibility pressure, where the minimum miscibility pressure is the minimum pressure that has to be applied to the carbon dioxide injected for achieving a multiple contact miscible flood;

wherein

(A) the miscibility pressure between the injection fluid and the hydrocarbonaceous fluid is lowered by 4.9% to 30.3% compared to the miscibility pressure between the hydrocarbonaceous fluid and carbon dioxide only, or

(B) the swelling factor of the hydrocarbonaceous fluid is increased by the injection fluid compared to the swelling factor of the hydrocarbonaceous fluid including the carbon dioxide only, or

(C) both (A) and (B);

iii) recovering the hydrocarbonaceous fluid from the reservoir.

2. The method of claim 1 wherein

a) the injection fluid comprises less than 1 wt. % water; or

b) wherein the injection fluid consists of the one or more alkoxylated alcohols and the liquid or supercritical carbon dioxide; or

c) wherein the injection fluid consists of the one or more alkoxylated alcohols, the liquid or supercritical carbon dioxide and a linear C4 to C9 alcohol or a branched alcohol having 4 to 18 carbon atoms or both.

3. The method of claim 1 , wherein the alkoxylated alcohols have the following structure

R—O-(A′O) m -(A″O) n —H  (II)

wherein

R is a linear alkyl group having from C4 to C8 carbon atoms, and/or a branched alkyl group having from C4 to C18 carbon atoms;

m is 1 to 12;

n is 1 to 12;

A′O is an ethoxy group (EO) and A″O is a propoxy group (PO); or

A′O is a propoxy group (PO) and A″O is an ethoxy group (EO).

4. The method of claim 1 , wherein

m is 1 to 8; and

n is 1 to 8.

5. The method of claim 1 , wherein the swelling factor of the hydrocarbonaceous fluid is increased by the injection fluid by 4% to 7% compared to the swelling factor of the hydrocarbonaceous fluid including carbon dioxide only.

6. The method of claim 1 , wherein R is a linear C4 to C8 alkyl group.

7. The method of claim 1 , wherein R is a branched alkyl group having 4 to 18 carbon atoms.

8. The method of claim 1 , wherein R is a branched alkyl group having 8 to 14 carbon atoms.

9. The method of claim 1 , wherein AO is EO.

10. The method of claim 1 , wherein AO is PO.

11. The method of claim 1 , wherein m+n is from 1 to 8.

12. The method of claim 1 , wherein m+n is from 1 to 6.

13. The method of claim 1 , wherein the hydrocarbonaceous fluid is a crude oil and the reservoir is a well.

14. The method of claim 1 , wherein the miscibility pressure between the injection fluid and the hydrocarbonaceous fluid is lowered compared to the miscibility pressure between the hydrocarbonaceous fluid and carbon dioxide only by 8.2% to 30.3%.

15. The method of claim 1 , wherein the miscibility pressure between the injection fluid and the hydrocarbonaceous fluid is lowered compared to the miscibility pressure between the hydrocarbonaceous fluid and carbon dioxide only by 16.3% to 30.3%.

16. The method of claim 1 , wherein the injection fluid does not comprise water.

17. A method comprising:

i) adding one or more alkoxylated alcohols having the following structure:

R—O-(AO) m+n —H  (I)

wherein

R is a linear alkyl group having from C4 to C8 carbon atoms, and/or a branched alkyl group having from C4 to C18 carbon atoms;

AO is EO and/or PO, independent of each m or n;

m is 0 to 12;

n is 0 to 12; and

m+n is at least 1

into an injection fluid comprising at least liquid or supercritical carbon dioxide,

ii) injecting the injection fluid into a reservoir, the reservoir being operated at a pressure below the minimum miscibility pressure, where the minimum miscibility pressure is the minimum pressure that has to be applied to the carbon dioxide injected for achieving a multiple contact miscible flood; and

wherein

(A) the miscibility pressure between the injection fluid and the hydrocarbonaceous fluid is lowered by 4.9% to 30.3% compared to the miscibility pressure between the hydrocarbonaceous fluid and carbon dioxide only, or

(B) the swelling factor of the hydrocarbonaceous fluid is increased by the injection fluid compared to the swelling factor of the hydrocarbonaceous fluid including the carbon dioxide only, or

(C) both (A) and (B); and

iii) recovering hydrocarbonaceous fluid from the reservoir.

18. A method comprising:

i) adding one or more alkoxylated alcohols having the following structure:

R—O-(AO) m+n —H  (I)

wherein

R is a linear alkyl group having from C4 to C8 carbon atoms, and/or a branched alkyl group having from C4 to C18 carbon atoms;

AO is EO and/or PO, independent of each m or n;

m is 0 to 12;

n is 0 to 12; and

m+n is at least 1

into an injection fluid comprising at least liquid or supercritical carbon dioxide,

ii) injecting the injection fluid into a reservoir, the reservoir being operated at a pressure below the minimum miscibility pressure, where the minimum miscibility pressure is the minimum pressure that has to be applied to the carbon dioxide injected for achieving a multiple contact miscible flood; and

wherein the miscibility pressure between the injection fluid and the hydrocarbonaceous fluid is lowered by 4.9% to 30.3% compared to the miscibility pressure between the hydrocarbonaceous fluid and carbon dioxide; and

iii) recovering hydrocarbonaceous fluid from the reservoir.

Assignments (5)
MERGER Recorded Jun 5, 2024
From: SASOL CHEMICALS GMBH
To: SASOL CHEMIE GMBH & CO. KG
Reel/Frame 067626/0677 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 21, 2022
From: SOTTMANN, THOMAS; BILGILI, HARUN; FISCHER, JULIAN
To: UNIVERSITAT STUTTGART
Reel/Frame 058724/0241 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 21, 2022
From: UNIVERSITAT STUTTGART
To: SASOL GERMANY GMBH
Reel/Frame 058724/0363 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 21, 2022
From: ROMMERSKIRCHEN, RENKE
To: SASOL GERMANY GMBH
Reel/Frame 058724/0415 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 21, 2022
From: SASOL GERMANY GMBH
To: SASOL CHEMICALS GMBH
Reel/Frame 058724/0463 →
Priority Claims (1)
EP 19158014 · Feb 19, 2019 · regional
Continuity (1)
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