Alpha-olefin sulfonate dimer surfactant cyclic steam stimulation process for recovering hydrocarbons from a subterranean formation

Claim 2

A cyclic steam-foam process of recovering hydrocarbons from a subterranean formation penetrated by a well comprising: injecting a steam and alpha-olefin sulfonate dimer foam at said well; displacing said steam and alpha-olefin sulfonate dimer foam out into the formation; terminating the injection of said steam and alpha-olefin sulfonate dimer foam; and recovering hydrocarbons from said well.

Claim 3

The process according to claim 1 wherein the alpha-olefin sulfonate dimer comprises of from about 0.01% to about 10% of the water phase of the steam.

Claim 4

The process according to claim 2 wherein a non-condensible gas in an amount of from about 1% to about 50% of the gaseous phase of said steam is injected with said steam at said well.

Claim 5

The process according to claim 3 wherein the non-condensible gas is selected from the group consisting of nitrogen, carbon dioxide, air, flue gas, CH 4 , and carbon monoxide.

Claim 6

The process according to claim 4 wherein the alpha-olefin sulfonate dimer includes alpha-olefin sulfonate dimer in the range of C 10 -C 48 .

Claim 7

The process according to claim 5 wherein said alpha-olefin sulfonate dimer includes a mixture of alpha-olefin sulfonate dimer in the range of C 22 -C 40 .

Claim 8

The process according to claim 5 wherein the alpha-olefin sulfonate dimer is synthesized according to the oligomerization process which comprises heating in the liquid phase the sulfonation product of the reaction of sulfur trioxide with a straight chain alkene hydrocarbon having a carbon atom content in the range of from about 5 to 24, wherein the heating is at a temperature above about 110° C. and below the carbonization temperature of the sulfonate, is effected in the substantial absence of water, and is continued for a period at least sufficient for a significant conversion of the sulfonate feed to the corresponding oligomeric disulfonic acid and wherein the resulting oligomeric sulfonic acid is neutralized with ammonia, an alkali metal base, a calcium base, a magnesium base or a mixture thereof.

Claim 9

The process according to claim 7 wherein said straight chain alkene hydrocarbon is a mixture in the range of C 5 -C 24 .

Claim 10

The process according to claim 8 wherein said straight chain alkene hydrocarbon mixture is in the range of C 11 -C 20 .

Claim 11

The process according to claim 1 wherein the alpha-olefin sulfonate dimer includes alpha-olefin sulfonate dimer in the range of C 10 -C 48 .

Claim 12

The process according to claim 10 wherein the alpha-olefin sulfonate dimer includes a mixture of alpha-olefin sulfonate dimer in the range of C 10 -C 48 .

Claim 13

The process according to claim 11 wherein the alpha-olefin sulfonate dimer is synthesized according to the oligomerization process which comprises heating in the liquid phase the sulfonation product of the reaction of sulfur trioxide with a straight chain alkene hydrocarbon having a carbon atom content in the range of from about 5 to 24, wherein the heating is at a temperature above about 110° C. and below the carbonization temperature of the sulfonate, is effected in the substantial absence of water, and is continued for a period at least sufficient for a significant conversion of the sulfonate feed to the corresponding oligomeric disulfonic acid.

Claim 14

The process according to claim 12 further comprising injecting steam into the formation prior to the injection of said steam and alpha-olefin sulfonate dimer.

Claim 15

The process according to claim 13 wherein steam is injected into the formation after the injection of said steam and alpha-olefin sulfonate dimer.

Claim 16

The process according to claim 14 wherein said steam injection is tapered into a steam and alpha-olefin sulfonate dimer injection which is tapered into a steam injection.

Claim 17

The process according to claim 15 wherein the salt form or the acid form of said alpha-olefin sulfonate dimer is employed.

Claim 18

The process according to claim 16 wherein a non-condensible gas in an amount of from about 1% to about 50% of the gaseous phase of said steam is injected into said steam prior to the injection of said steam at said well.

Claim 19

The process according to claim 17 wherein said straight chain alkene hydrocarbon is a mixture in the range of C 5 -C 24 .

Claim 20

The process according to claim 18 wherein said straight chain alkene hydrocarbon mixture is in the range of C 11 -C 20 .

Claim 21

The process according to claim 1 wherein the alpha-olefin sulfonate dimer comprises of from about 0.1% to about 10% of the water phase of the steam.

Claim 22

The process according to claim 20 wherein said alpha-olefin sulfonate dimer includes alpha-olefin sulfonate dimer in the range of C 10 -C 48 .

Claim 23

The process according to claim 21 wherein the alpha-olefin sulfonate dimer includes a mixture of alpha-olefin sulfonate dimer in the range of C 10 -C 48 .

Claim 24

A cyclic steam process for recovering hydrocarbons from a subterranean hydrocarbon bearing formation penetrated by a well, said process comprising: injecting a steam and alpha-olefin sulfonate dimer at said well and out into said formation and away from said well, wherein said alpha-olefin sulfonate dimer is synthesized according to the oligomerization process which comprises heating in the liquid phase the sulfonation product of the reaction of sulfur trioxide with a straight chain alkene hydrocarbon having a carbon atom content in the range of from about 5 to 24, wherein the heating is at a temperature above about 110° C. and below the carbonization temperature of the sulfonate, is effected in the substantial absence of water, and is continued for a period at least sufficient for a significant conversion of the sulfonate feed to the corresponding oligomeric disulfonic acid and wherein the resulting oligomeric sulfonic acid is neutralized with ammonia, an alkali metal base, a calcium base, a magnesium base or a mixture thereof; terminating the injection of said steam and alpha-olefin sulfonate dimer; and recovering hydrocarbons at said well.

Claim 25

A cyclic steam process for recovering hydrocarbons from a subterranean hydrocarbon bearing formation penetrated by a well, said process comprising: injecting a steam and alpha-olefin sulfonate dimer at said well and out into said formation and away from said well, wherein said alpha-olefin sulfonate dimer is synthesized according to the oligomerization process which comprises heating in the liquid phase the sulfonation product of the reaction of sulfur trioxide with a straight chain alkene hydrocarbon having a carbon atom content in the range of from about 5 to 24, wherein the heating is at a temperature above about 110° C. and below the carbonization temperature of the sulfonate, is effected in the substantial absence of water, and is continued for a period at least sufficient for a significant conversion of the sulfonate feed to the corresponding oligomeric disulfonic acid and wherein the resulting oligomeric sulfonic acid is neutralized with ammonia, an alkali metal base, a calcium base, a magnesium base or a mixture thereof; terminating the injection of said steam and alpha-olefin sulfonate dimer; and recovering hydrocarbons at said well.

Claim 26

The process according to claim 23 wherein the alpha-olefin sulfonate dimer comprises from about 0.1% to about 10% of the liquid phase of the steam.

Claim 27

The process according to claim 24 wherein said foam further contains a non-condensible gas selected from the group consisting of nitrogen, carbon dioxide, air, flue gas, CH 4 and carbon monoxide.

Claim 28

The process according to claim 25 wherein said straight chain alkene hydrocarbon is a mixture of C 5 -C 24 hydrocarbons.

Claim 29

The process according to claim 26 wherein said mixture is a C 11 -C 20 mixture.

Claim 30

The process according to claim 23 wherein said alpha-olefin sulfonate dimer includes a mixture of alpha-olefin sulfonate dimer in the range of C 22 -C 40 .

Claim 31

Cyclic steam injection process for recovering hydrocarbons from a hydrocarbon containing subterranean formation penetrated by a well, said process sequentially comprises: (a) injecting sufficient wet steam into the hydrocarbon bearing formation to form a steam zone and a hot water zone therein; thereafter (b) continuting to injecting steam and adding alpha-olefin sulfonate dimer thereto, wherein said alpha-olefin sulfonate dimer is about 1% of the water phase of said steam and said alpha-olefin sulfonate dimer is a mixture of alpha-olefin sulfonate dimer within the range of C 10 -C 48 ; thereafter (c) terminating the injection of said steam and alpha-olefin sulfonate dimer; and, thereafter (d) producing hydrocarbons from said hydrocarbon containing subterranean formation through said well.

Claim 32

Cyclic steam injection process for recovering hydrocarbons from a hydrocarbon containing subterranean formation penetrated by a well, said process sequentially comprises: (a) injecting sufficient wet steam into the hydrocarbon bearing formation to form a steam zone and a hot water zone therein; thereafter (b) continuting to injecting steam and adding alpha-olefin sulfonate dimer thereto, wherein said alpha-olefin sulfonate dimer is about 1% of the water phase of said steam and said alpha-olefin sulfonate dimer is a mixture of alpha-olefin sulfonate dimer within the range of C 10 -C 48 ; thereafter (c) terminating the injection of said steam and alpha-olefin sulfonate dimer; and, thereafter (d) producing hydrocarbons from said hydrocarbon containing subterranean formation through said well.

Claim 33

The process according to claim 29 wherein said well is shut in for a predetermined period before producing said hydrocarbons in Step d.

Claim 34

The process according to claim 30 wherein said alpha-olefin sulfonate dimer is synthesized according to the oligomerization process which comprises heating in the liquid phase the sulfonation product of the reaction of sulfur trioxide with a straight chain alkene hydrocarbon having a carbon atom content in the range of from about 5 to 24, wherein the heating is at a temperature above about 110° C. and below the carbonization temperature of the sulfonate, is effected in the substantial absence of water, and is continued for a period at least sufficient for a significant conversion of the sulfonate feed to the corresponding oligormeric disulfonic acid.