Use of organic acids or a salt thereof in surfactant-based enhanced oil recovery formulations and techniques

1. A process for recovering fossil fluids from a fossil fluid-bearing subterranean formation comprising injecting a surfactant formulation comprising a nonionic surfactant, an organic acid selected from the group consisting of diglycolic acid, glycolic acid and a salt thereof, and injection water, wherein the organic acid and nonionic surfactant are present at a ratio ranging between about 0.05 parts by weight organic acid/15 parts by weight nonionic surfactant to about 2 parts by weight organic acid/10 parts by weight nonionic surfactant into one or more injection wells such that oil is subsequently produced from one or more producing wells and wherein the nonionic surfactant is an alkoxylated alkylphenol comprising 10 to 30 alkylene oxide units and wherein the surfactant formulation further comprises an alkylaryl sulfonate represented by the formula (II)

wherein R a is hydrogen or an alkyl group containing 1 to 3 carbon atoms, R b is hydrogen or an alkyl group containing 1 to 3 carbon atoms, R c is an alkyl group containing 8 to 40 carbon atoms and A is a monovalent cation

and wherein the alkylaryl sulfonate is added to the surfactant formulation at a ratio of between about 1:15 parts by weight of alkylaryl sulfonate to nonionic surfactant to about 1:5 parts by weight of alkylaryl sulfonate to nonionic surfactant.

2. The process of claim 1 , wherein the alkoxylated alkylphenol has one or more linear or branched C 1 to C 25 alkyl groups attached.

3. The process of claim 1 , wherein the nonionic surfactant is an alkoxylated linear or branched saturated aliphatic alcohol compound comprising 5 to 30 carbon atoms.

4. The process of claim 1 , wherein the nonionic surfactant is an alkoxylated Guerbet alcohol of formula (I)

R 2 —O—BO t —P u -EO w —H  (I)

wherein R 2 corresponds to an aliphatic, branched hydrocarbon group C n H 2n+1 derived from a Guerbet alcohol where n ranges from 12 to 36; BO corresponds to a butoxy group; t is a number ranging from 0 to 50; PO corresponds to a propoxy group; u is a number ranging from 0 to 50; EO corresponds to an ethoxy group; and w is a number ranging from 0 to 50 with the proviso that t+u+w≥1.

5. The process according to claim 1 , wherein the organic acid is glycolic acid or a glycolic acid salt.

6. The process according to claim 5 , wherein the glycolic acid salt is at least one of sodium glycolate and disodium glycolate.

7. The process according to claim 1 , wherein the injection water is seawater, brine, fresh water from an aquifer, river or lake, or a mixture thereof.

8. The process according to claim 1 , wherein the surfactant formulation further comprises an alkali metal hydroxide, alkali metal carbonate, or alkali metal chloride.

9. The process according to claim 1 , wherein the alkylaryl sulfonate is added to the surfactant formulation at a ratio of between about 1:12.5 parts by weight of alkylaryl sulfonate to nonionic surfactant to about 1:7.5 parts by weight of alkylaryl sulfonate to nonionic surfactant.

10. The process according to claim 1 , wherein the organic acid and nonionic surfactant are present at a ratio ranging between about 0.05 parts by weight organic acid/15 parts by weight nonionic surfactant to about 1.25 parts by weight organic acid/9 parts by weight nonionic surfactant.

11. The process according to claim 3 , wherein the alkoxylated linear or branched saturated aliphatic alcohol comprises 10 to 30 alkylene oxide units.

12. The process according to claim 1 , wherein the surfactant formulation further comprises a solvent.

13. The process according to claim 1 , wherein the subterranean formation temperature condition is between about 80° F. and about 300° F.

14. The process according to claim 1 , wherein the injection well and producing well are the same well.

15. The process according to claim 1 , wherein the injection well and producing well are adjacent to one another.