Process for preparing an internal olefin sulfonate
US-9221750-B2 · Dec 29, 2015 · US
US9475979B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9475979-B2 |
| Application number | US-201213659454-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 24, 2012 |
| Priority date | Oct 24, 2011 |
| Publication date | Oct 25, 2016 |
| Grant date | Oct 25, 2016 |
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The present invention relates to a surfactant mixture comprising at least three ionic surfactants which differ in terms of the hydrocarbyl moiety (R 1 )(R 2 )—CH—CH 2 — and are of the general formula (I) where R 1 , R 2 , A 0 , k, X, o, Y, a, b, M are each as defined in the description and the claims. The invention further relates to the use and preparation thereof, and to aqueous surfactant formulations comprising the mixtures, and to processes for producing mineral oil by means of Winsor type III microemulsion flooding, in which the aqueous surfactant formulation is injected into a mineral oil deposit through injection wells and crude oil is withdrawn from the deposit through production wells.
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The invention claimed is: 1. A process for producing mineral oil by means of Winsor type III microemulsion flooding, comprising injecting an aqueous surfactant formulation into a mineral oil deposit through at least one injection well for the purpose of lowering the interfacial tension between oil and water to <0.1 mN/m, and withdrawing crude oil from the deposit through at least one production well; wherein the aqueous surfactant formulation comprises a surfactant mixture comprising at least three ionic surfactants which differ in terms of the hydrocarbyl moiety (R 1 )(R 2 )—CH—CH 2 — and are of the general formula (I) where R 1 is a linear saturated or unsaturated aliphatic hydrocarbyl radical having 8 to 10 carbon atoms; R 2 is a linear saturated or unsaturated aliphatic hydrocarbyl radical having 10 to 12 carbon atoms; where R 1 and R 2 radicals are selected such that the at least 3 ionic surfactants of the general formula (I) give rise to hydrocarbyl radicals (R 1 )(R 2 )CHCH 2 — with 20 carbon atoms, 22 carbon atoms, and 24 carbon atoms; wherein the C 20 surfactant of the general formula (I) is present within a range from 10 to 30%, the C 22 surfactant of the general formula (I) within a range from 5% to 25% and the C 24 surfactant of the general formula (I) within a range from 55% to 85%, based on the molar sum formed from these three surfactants; each A 0 is independently ethylene, propylene or butylene; k is an integer from 1 to 99, X is a branched or unbranched hydrocarbylene group which has 1 to 10 carbon atoms and may be substituted by an OH group; o is 0 or 1; M b+ is a cation; Y a− is a sulfate group, sulfonate group, carboxylate group or phosphate group; b is 1, 2 or 3 and a is 1 or 2. 2. The process according to claim 1 , wherein k is an integer in the range from 4 to 50. 3. The process according to claim 1 , wherein the (—O—X—) o —Y a− radical in formula (I) is OS(O) 2 O − , OCH 2 CH 2 S(O) 2 O − , OCH 2 CH(OH)CH 2 S(O) 2 O − , O(CH 2 ) 3 S(O) 2 O − , S(O) 2 O − , CH 2 C(O)O − or CH 2 CH(R′)C(O)O − , where R′ is hydrogen or an alkyl radical having 1 to 4 carbon atoms. 4. The process according to claim 1 , wherein (—O-A 0 -) k in formula (I) represents n butyleneoxy, m propyleneoxy and 1 ethyleneoxy groups, where n+m+l=k. 5. The process according to claim 4 , wherein the n butyleneoxy, m propyleneoxy and 1 ethyleneoxy groups are arranged in blocks. 6. The process according to claim 5 , wherein the (R 1 )(R 2 )—CH—CH 2 — radical in formula (I) is followed, representing (—O-A 0 -) k , by a butyleneoxy block with n butyleneoxy groups, followed by a propyleneoxy block with m propyleneoxy groups, and finally an ethyleneoxy block with 1 ethyleneoxy groups. 7. The process according to claim 4 , wherein m is an integer from 4 to 15, l is an integer from 0 to 25, and n is an integer from 2 to 15. 8. The process according to claim 1 , wherein the aqueous surfactant formulation further comprises surfactants of the formula and of the formula where R 1 , R 2 , A 0 , X, Y a− , M b+ , k, o, a and b are each as defined for formula (I). 9. The process according to claim 8 , wherein the proportion of surfactants of the formula (I) in relation to the sum of the amounts of surfactants of the formulae (I), (II) and (III) is in the range from 80% by weight to 99% by weight. 10. A method of Winsor type III microemulsion flooding comprising injecting into a mineral oil deposit a surfactant mixture comprising at least three ionic surfactants which differ in terms of the hydrocarbyl moiety (R 1 )(R 2 )—CH—CH 2 — and are of the general formula (I) where R 1 is a linear saturated or unsaturated aliphatic hydrocarbyl radical having 8 to 10 carbon atoms; R 2 is a linear saturated or unsaturated aliphatic hydrocarbyl radical having 10 to 12 carbon atoms; where R 1 and R 2 radicals are selected such that the at least 3 ionic surfactants of the general formula (I) give rise to hydrocarbyl radicals (R 1 )(R 2 )CHCH 2 — with 20 carbon atoms, 22 carbon atoms, and 24 carbon atoms; wherein the C 20 surfactant of the general formula (I) is present within a range from 10 to 30%, the C 22 surfactant of the general formula (I) within a range from 5% to 25% and the C 24 surfactant of the general formula (I) within a range from 55% to 85%, based on the molar sum formed from these three surfactants; each A 0 is independently ethylene, propylene or butylene; k is an integer from 1 to 99, X is a branched or unbranched hydrocarbylene group which has 1 to 10 carbon atoms and may be substituted by an OH group; o is 0 or 1; M b+ is a cation; Y a− is a sulfate group, sulfonate group, carboxylate group or phosphate group; b is 1, 2 or 3 and a is 1 or 2. 11. The method according to claim 1 , wherein the aqueous surfactant formulation has a total surfactant content of 0.05 to 5% by weight based on the total amount of the aqueous surfactant formulation.
characterised by the use of specific surfactants · CPC title
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