Oil recovery method using unique salinity for oil recovery surfactant system

Claim 3

A method according to claim 1 comprising in addition preparing a surfactant system having an optimal salinity at or near the unique salinity, utilizing the relationship that with increasing water solubility of the cosurfactant, the optimal salinity increases and with decreasing water solubility of the cosurfactant, the optimal salinity decreases.

Claim 4

A method according to claim 1 wherein said relatively water insoluble cosurfactant has a water solubility within the range of 0.5 to 5 grams per 100 grams of water at room temperature and said relatively water soluble cosurfactant has a water solubility within the range of 10 grams per 100 grams of water to infinite solubility at room temperature.

Claim 5

A method according to claim 1 wherein said electrolyte comprises sodium chloride.

Claim 6

A method according to claim 1 wherein said surfactant comprises a petroleum sulfonate.

Claim 7

A method according to claim 1 wherein said surfactant consists essentially of a petroleum sulfonate having an average equivalent weight within the range of 375 to 500.

Claim 8

A method according to claim 1 wherein said cosurfactant is present in said aqueous surfactant-cosurfactant-electrolyte systems in an amount within the range of 1 to 7 weight percent based on the weight of said systems, and said surfactant is present in an amount within the range of 1 to 7 weight percent based on the weight of said systems.

Claim 9

A method according to claim 7 wherein said cosurfactants are alcohols, said surfactant is a petroleum sulfonate having an average equivalent weight within the range of 375 to 500, and said electrolyte comprises sodium chloride.

Claim 10

A method according to claim 1 comprising in addition preparing a surfactant system using a cosurfactant having a water solubility no greater than 10 g per 100 g of water at room temperature, having an optimal salinity at or near the unique salinity using the relationship that decreasing the cosurfactant concentration increases the optimal salinity.

Claim 11

A process for recovering oil from a subterranean oil-bearing reservoir comprising the steps of: (1) injecting into said reservoir a surfactant system at or near unique salinity corresponding to one prepared by: (a) preparing a series of aqueous surfactant-cosurfactant-electrolyte systems at varying electrolyte concentrations using a relatively water insoluble cosurfactant, mixing oil corresponding to that in said oil-bearing reservoir with the thus produced systems, allowing the resulting mixtures to equilibrate and determining the salinity at which the microemulsion phase formed on said equilibration has approximately equal volumes of oil and water, thus giving the optimal salinity concentration for this surfactant-cosurfactant combination; (b) preparing a second series of aqueous surfactant-cosurfactant-electrolyte systems at varying electrolyte concentrations using a relatively water soluble cosurfactant, mixing said oil corresponding to said oil in said reservoir with the thus produced systems, allowing the resulting mixtures to equilibrate and determining the salinity at which the microemulsion phase formed on said equilibration has approximately equal volumes of oil and water, thus giving the optimum salinity concentration for this surfactant-cosurfactant combination; (c) preparing at least one series of aqueous surfactant-cosurfactant-electrolyte systems using a cosurfactant having a water solubility intermediate that of said first and second cosurfactants, mixing said oil corresponding to said oil in said reservoir with the thus produced systems, allowing the resulting mixtures to equilibrate and determining the salinity at which the microemulsion phase formed on said equilibration has approximately equal volumes of oil and water, thus giving the optimum salinity concentration for each surfactant-cosurfactant combination; (d) utilizing said systems of (a), (b) and (c) at optimal salinity to remove oil from a core and plotting the percentage oil recovered versus the salinity of each system; (e) determining from said plot of (d) the unique salinity at which maximum oil recovery is obtained; (f) preparing said surfactant system having an optimum salinity at or near said unique salinity of (e) for said injecting utilizing at least one of the relationships that: (i) the optimal salinity increases with increasing water solubility of said cosurfactant and decreases with decreasing water solubility of said cosurfactant; and (ii) with cosurfactants having a water solubility no greater than 10 g per 100 grams of water at room temperature, the optimal salinity increases with decreasing cosurfactant concentration and decreases with increasing cosurfactant concentration. (2) thereafter injecting a drive fluid into said reservoir and forcing said oil towards at least one recovery well; and (3) recovering said oil.

Claim 12

A process for recovering oil from a subterranean oil-bearing reservoir comprising the steps of: (1) injecting into said reservoir a surfactant system at or near unique salinity corresponding to one prepared by: (a) preparing a series of aqueous surfactant-cosurfactant-electrolyte systems at varying electrolyte concentrations using a relatively water insoluble cosurfactant, mixing oil corresponding to that in said oil-bearing reservoir with the thus produced systems, allowing the resulting mixtures to equilibrate and determining the salinity at which the microemulsion phase formed on said equilibration has approximately equal volumes of oil and water, thus giving the optimal salinity concentration for this surfactant-cosurfactant combination; (b) preparing a second series of aqueous surfactant-cosurfactant-electrolyte systems at varying electrolyte concentrations using a relatively water soluble cosurfactant, mixing said oil corresponding to said oil in said reservoir with the thus produced systems, allowing the resulting mixtures to equilibrate and determining the salinity at which the microemulsion phase formed on said equilibration has approximately equal volumes of oil and water, thus giving the optimum salinity concentration for this surfactant-cosurfactant combination; (c) preparing at least one series of aqueous surfactant-cosurfactant-electrolyte systems using a cosurfactant having a water solubility intermediate that of said first and second cosurfactants, mixing said oil corresponding to said oil in said reservoir with the thus produced systems, allowing the resulting mixtures to equilibrate and determining the salinity at which the microemulsion phase formed on said equilibration has approximately equal volumes of oil and water, thus giving the optimum salinity concentration for each surfactant-cosurfactant combination; (d) utilizing said systems of (a), (b) and (c) at optimal salinity to remove oil from a core and plotting the percentage oil recovered versus the salinity of each system; (e) determining from said plot of (d) the unique salinity at which maximum oil recovery is obtained; (f) preparing said surfactant system having an optimum salinity at or near said unique salinity of (e) for said injecting utilizing at least one of the relationships that: (i) the optimal salinity increases with increasing water solubility of said cosurfactant and decreases with decreasing water solubility of said cosurfactant; and (ii) with cosurfactants having a water solubility no greater than 10 g per 100 grams of water at room temperature, the optimal salinity increases with decreasing cosurfactant concentration and decreases with increasing cosurfactant concentration. (2) thereafter injecting a drive fluid into said reservoir and forcing said oil towards at least one recovery well; and (3) recovering said oil.

Claim 13

A method according to claim 10 wherein said electrolyte comprises sodium chloride, said surfactant comprises a petroleum sulfonate having an average equivalent weight within the range of 375 to 500, said cosurfactants are alcohols, said surfactant is present in said surfactant-cosurfactant-electrolyte systems in a concentration within the range of 1 to 7 weight percent based on the weight of said systems and said cosurfactant is present in said systems in a concentration within the range of 1 to 7 weight percent based on the weight of said system.

Claim 16

A process for recovering oil from an oil-bearing reservoir comprising the steps of: (a) preparing a first surfactant-cosurfactant-electrolyte-water system having an optimal salinity essentially corresponding to a unique salinity thereof, said optimal salinity being the salinity concentration at which a microemulsion phase having approximately equal volumes of oil and water forms on mixing the reservoir oil or equivalent with a surfactant system, said unique salinity being the salinity concentration at which maximum oil recovery is obtained for the reservoir oil or equivalent-surfactant combination obtained by the proper selection of the cosurfactant and cosurfactant concentration; (b) preparing a second surfactant system having the unique salinity changed from that of said system of (a) toward that of connate water in said oil-bearing reservoir using the relationship that with decreasing surfactant hydrophobic content, the unique salinity is increased and with increasing surfactant hydrophobic content, the unique salinity is decreased; (c) injecting said surfactant system of (b) into said reservoir; (d) thereafter injecting a drive fluid, thus forcing said oil toward at least one recovery well; and (e) recovering said oil.

Claim 17

A process for recovering oil from an oil-bearing reservoir comprising the steps of: (a) preparing a first surfactant-cosurfactant-electrolyte-water system having an optimal salinity essentially corresponding to a unique salinity thereof, said optimal salinity being the salinity concentration at which a microemulsion phase having approximately equal volumes of oil and water forms on mixing the reservoir oil or equivalent with a surfactant system, said unique salinity being the salinity concentration at which maximum oil recovery is obtained for the reservoir oil or equivalent-surfactant combination obtained by the proper selection of the cosurfactant and cosurfactant concentration; (b) preparing a second surfactant system having the unique salinity changed from that of said system of (a) toward that of connate water in said oil-bearing reservoir using the relationship that with decreasing surfactant hydrophobic content, the unique salinity is increased and with increasing surfactant hydrophobic content, the unique salinity is decreased; (c) injecting said surfactant system of (b) into said reservoir; (d) thereafter injecting a drive fluid, thus forcing said oil toward at least one recovery well; and (e) recovering said oil.

Claim 18

A method according to claim 13 wherein said electrolyte comprises sodium chloride, said surfactant comprises a petroleum sulfonate having an average equivalent weight within the range of 375 to 500, said cosurfactants are alcohols, said surfactant is present in said surfactant-cosurfactant-electrolyte systems in a concentration within the range of 1 to 7 weight percent based on the weight of water in said systems and said cosurfactant is present in said systems in a concentration within the range of 1 to 7 weight percent based on the weight of said water in said systems.

Claim 19

A method according to claim 14 wherein said connate water has a higher salinity than the unique salinity of said surfactant system of (a) and said surfactant system of (b) is prepared by utilizing a lower equivalent weight sulfonate.

Claim 20

A method according to claim 14 wherein said connate water has a lower salinity than said unique salinity of said surfactant system of (a) and said surfactant system of (b) is prepared by utilizing a petroleum sulfonate having a higher equivalent weight.

Claim 21

A process for recovering oil from an oil-bearing reservoir comprising the steps of: (a) preparing a surfactant-cosurfactant-electrolyte-water system having an optimal salinity essentially corresponding to a unique salinity thereof, said optimal salinity being the salinity concentration at which a microemulsion phase having approximately equal volumes of oil and water forms on mixing the reservoir oil or equivalent with a surfactant system, said unique salinity being the salinity concentration at which maximum oil recovery is obtained for the reservoir oil or equivalent-surfactant combination obtained by the proper selection of the cosurfactant and cosurfactant concentration; (b) injecting a preflush into said reservoir to shift the connate water salinity toward the unique salinity of the surfactant system of (a); (c) injecting said surfactant system of (a) into said reservoir; (d) thereafter injecting a drive fluid, thus forcing said oil toward at least one recovery well; and (e) recovering said oil.

Claim 22

A process for recovering oil from an oil-bearing reservoir comprising the steps of: (a) preparing a surfactant-cosurfactant-electrolyte-water system having an optimal salinity essentially corresponding to a unique salinity thereof, said optimal salinity being the salinity concentration at which a microemulsion phase having approximately equal volumes of oil and water forms on mixing the reservoir oil or equivalent with a surfactant system, said unique salinity being the salinity concentration at which maximum oil recovery is obtained for the reservoir oil or equivalent-surfactant combination obtained by the proper selection of the cosurfactant and cosurfactant concentration; (b) injecting a preflush into said reservoir to shift the connate water salinity toward the unique salinity of the surfactant system of (a); (c) injecting said surfactant system of (a) into said reservoir; (d) thereafter injecting a drive fluid, thus forcing said oil toward at least one recovery well; and (e) recovering said oil.