Process for producing mineral oil using surfactants based on a mixture of C32 guerbet-, C34 guerbet-, C36 guerbet-containing alkyl alkoxylates

Patent metadata

Field	Value
Publication number	US-9701893-B2
Application number	US-201514832425-A
Country	US
Kind code	B2
Filing date	Aug 21, 2015
Priority date	Apr 23, 2010
Publication date	Jul 11, 2017
Grant date	Jul 11, 2017

Abstract

The present invention relates to a process for mineral oil extraction by means of Winsor type III microemulsion flooding, in which an aqueous surfactant formulation comprising at least three ionic surfactants which are different with regard to the alkyl moiety (R 1 )(R 2 )—CH—CH 2 — and are of the general formula (R 1 )(R 2 )—CH—CH 2 —O-(D) n -(B) m -(A) l -XY a− a/bM b+ is injected through injection boreholes into a mineral oil deposit, and crude oil is withdrawn from the deposit through production boreholes. The invention further relates to surfactant formulations of ionic surfactants of the general formula.

First claim

The invention claimed is:

1. A process for mineral oil extraction by means of Winsor type III microemulsion flooding, the process comprising;
injecting an aqueous surfactant formulation comprising at least three ionic surfactants, for the purpose of lowering the interfacial tension between oil and water to <0.1 mN/m, through at least one injection borehole into a mineral oil deposit, and
withdrawing the mineral oil from the deposit through at least one production borehole, wherein the at least three surfactants each of which are different with regard to the alkyl moiety (R 1 )(R 2 )—CH—CH 2 —, and are of the general formula (I)
(R 1 )(R 2 )—CH—CH 2 —O-(D) n -(B) m -(A) l -XY a− a/b M b+   (I)

where
R 1 is a linear or branched, saturated or unsaturated, aliphatic hydrocarbyl radical having 14 to 16 carbon atoms,
R 2 is a linear or branched, saturated or unsaturated, aliphatic hydrocarbyl radical having 16 to 18 carbon atoms, and

the at least three different ionic surfactants of the general formula (I) each respectively includes an alkyl radical having 32 carbon atoms, 34 carbon atoms and 36 carbon atoms, wherein
A is ethyleneoxy,
B is propyleneoxy,
D is butyleneoxy,
l is from 0 to 99,
m is from 0 to 99,
n is from 0 to 99,
X is an alkyl or alkylene group having 0 to 10 carbon atoms,
M b+ is a cation,
Y a− is selected from the group of sulfate groups, sulfonate groups, carboxylate groups and phosphate groups,
b is 1, 2 or 3, and
a is 1 or 2,
where the A and B groups may be distributed randomly, alternatingly, or in the form of two, three, four or more blocks in any sequence and the sum of l+m+n is in the range from 0 to 99.

2. The process according to claim 1 , wherein the concentration of all surfactants together is 0.05 to 5% by weight, based on the total amount of the aqueous surfactant formulation.

3. The process according to claim 1 , wherein n is from 2 to 15.

4. The process according to claim 1 , wherein the aqueous surfactant formulation further comprises surfactants of formulae (II) and (III)
(R 1 )—CH 2 —CH 2 —O-(D) n -(B) m -(A) l -XY a− a/b M b+   (II)

(R 2 )—O-(D) n -(B) m -(A) l -XY a− a/b M b+   (III),

where R 1 , R 2 , A, B, D, X, Y − , M + , m, n and l are each as defined above, and the surfactants of the formula (I) account for between 80 and 99% by weight of a total amount of the surfactants of formulae (I), (II) and (III).

5. The process according to claim 4 , wherein for each of the at least three different ionic surfactants of the general formula (I)
m is from 5 to 9,
n is from 2 to 15, and
Y − is selected from the group of sulfate groups, sulfonate groups, and carboxylate groups, where
the A, B and D groups are present to an extent of more than 80% in block form in the sequence D, B, A beginning from (R 1 )(R 2 )—CH—CH 2 , the sum of l+m+n is in the range from 7 to 50, and the block D consists to an extent of 80% and more of 1,2-butylene oxide.

6. The process according to claim 4 , wherein the aqueous surfactant formulation further comprises surfactants of formula (I) account for between 85 and 99% by weight of the total amount of the surfactants of formulae (I), (II) and (III).

7. The process according to claim 1 , wherein the surfactant with the alkyl radical with 32 carbon atoms has R 1 /R 2 of 14/16, the alkyl radical with 34 carbon atoms has R 1 /R 2 of 14/18 or 16/16, and the alkyl radical with 36 carbon atoms has R 1 /R 2 of 16/18.

8. The process according to claim 1 , wherein R 1 and R 2 are linear saturated alkyl radicals.

9. The process according to claim 1 , wherein the at least three ionic surfactants of the general formula (I) account for at least at least 40% by weight, based on the total weight of the surfactant mixture.

10. The process according to claim 7 , wherein the at least three ionic surfactants of the general formula (I) account for at least at least 40% by weight, based on the total weight of the surfactant mixture.

11. The process according to claim 1 , wherein the sum of l+m+n is within the range from 4 to 50.

12. The process according to claim 4 , wherein for each of the at least three different ionic surfactants of the general formula (I)
m is from 4 to 15,
n is from 0 to 15, and
Y − is selected from the group of sulfate groups, sulfonate groups and carboxylate groups, where
the A and B groups are present to an extent of more than 80% in block form in the sequence D, B, A beginning from (R 1 )(R 2 )—CH—CH 2 , the sum of l+m is in the range from 4 to 50.

13. A process for mineral oil extraction by means of Winsor type III microemulsion flooding, the process comprising;
injecting an aqueous surfactant formulation comprising at least three ionic surfactants, for the purpose of lowering the interfacial tension between oil and water to <0.1 mN/m, through at least one injection borehole into a mineral oil deposit, and
withdrawing the mineral oil from the deposit through at least one production borehole, wherein the at least three surfactants which are different with regard to the alkyl moiety (R 1 )(R 2 )—CH—CH 2 — and are of the general formula (I)
(R 1 )(R 2 )—CH—CH 2 —O-(D) n -(B) m -(A) l -XY a− a/b M b+   (I)

where
R 1 is a linear or branched, saturated or unsaturated, aliphatic hydrocarbyl radical having 14 to 16 carbon atoms,
R 2 is a linear or branched, saturated or unsaturated, aliphatic hydrocarbyl radical having 16 to 18 carbon atoms,
A is ethyleneoxy,
B is propyleneoxy,
D is butyleneoxy,
l is from 0 to 99,
m is from 5 to 9,
n is from 2 to 15,
X is an alkyl or alkylene group having 0 to 10 carbon atoms,
M b+ is a cation,
Y a− is selected from the group of sulfate groups, sulfonate groups, and carboxylate groups,
b is 1, 2 or 3, and
a is 1 or 2,
where the A, B and D groups are present to an extent of more than 80% in block form in the sequence D, B, A beginning from (R 1 )(R 2 )—CH—CH 2 , the sum of l+m+n is in the range from 7 to 50, and the block D consists to an extent of 80% or more of 1,2-butylene oxide.

14. A process for mineral oil extraction by means of Winsor type HI microemulsion flooding, the process comprising;
injecting an aqueous surfactant formulation comprising at least three ionic surfactants, for the purpose of lowering the interfacial tension between oil and water to <0.1 mN/m, through at least one injection borehole into a mineral oil deposit, and
withdrawing the mineral oil from the deposit through at least one production borehole, wherein the at least three surfactants which are different with regard to the alkyl moiety (R 1 )(R 2 )—CH—CH 2 — and are of the general formula (I)
(R 1 )(R 2 )—CH—CH 2 —O-(D) n -(B) m -(A) l -XY a− a/b M b+   (I)

where
R 1 is a linear or branched, saturated or unsaturated, aliphatic hydrocarbyl radical having 14 to 16 carbon atoms,
R 2 is a linear or branched, saturated or unsaturated, aliphatic hydrocarbyl radical having 16 to 18 carbon atoms,
A is ethyleneoxy,
B is propyleneoxy,
D is butyleneoxy,
l is from 0 to 99,
m is from 4 to 15,
n is from 0 to 15,
X is an alkyl or alkylene group having 0 to 10 carbon atoms,
M b+ is a cation,
Y a− is selected from the group of sulfate groups, sulfonate groups, and carboxylate groups,
b is 1, 2 or 3, and
a is 1 or 2,
where the A and B groups are present to an extent of more than 80% in block form in the sequence D, B, A beginning from (R 1 )(R 2 )—CH—CH 2 , the sum of l+m is in the range from 4 to 50.

Assignees

• Basf Se

Inventors

• Bittner Christian
• OETTER Günter
• Tinsley Jack
• Spindler Christian
• Alvarez-Juergenson Gabriela
• Vogel Sophie
• Neumann Petra
• Wloka Veronika
• Bock Martin

Classifications

• C09K8/584 Primary

  characterised by the use of specific surfactants · CPC title

• C09K8/86 Primary

  containing organic compounds · CPC title

• E21B43/16

  Enhanced recovery methods for obtaining hydrocarbons · CPC title