Solids free gellable treatment fluids
US-2016083641-A1 · Mar 24, 2016 · US
US10544354B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10544354-B2 |
| Application number | US-201415030712-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 12, 2014 |
| Priority date | Feb 12, 2014 |
| Publication date | Jan 28, 2020 |
| Grant date | Jan 28, 2020 |
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Various embodiments disclosed relate to methods, compositions, and systems for enhanced oil recovery including a viscosifier polymer. In various embodiments, the present invention provides a method of enhanced oil recovery that can include obtaining or providing a composition that includes a viscosifier polymer. The viscosifier polymer includes an ethylene repeating unit including a —C(O)NH2 group and an ethylene repeating unit including an —S(O)2OR1 group, where the repeating units are in block, alternate, or random configuration. At each occurrence R1 can be independently selected from the group consisting of —H and a counterion. The method can include placing the composition in a subterranean formation downhole via an injection wellbore. The method can also include extracting material comprising petroleum from the subterranean formation downhole via a production wellbore.
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What is claimed is: 1. A method of enhanced oil recovery, the method comprising: placing in a subterranean formation via an injection wellbore a crosslinked gel, wherein the crosslinked gel comprises: a viscosifier polymer, wherein the viscosifier polymer comprises an ethylene repeating unit comprising a —C(O)NH 2 group and an ethylene repeating unit comprising an —S(O) 2 OR 1 group, wherein ethylene repeating units having the structure: wherein at each occurrence R 1 is independently selected from the group consisting of —H and a counterion, at each occurrence R 3 , R 4 , and R 5 are independently selected from the group consisting of —H, —CH 3 , —CH 2 CH 3 , at each occurrence L 1 and L 2 are independently selected from the group consisting of a substituted or unsubstituted C 1 -C 40 hydrocarbyl interrupted or terminated with 0, 1, 2, or 3 of at least one of —NR 3 —, —S—, and —O—, wherein n is about 5,000 to about 75,000, and z is about 2,500 to about 170,000 and the repeating units are in block, alternate, or random configuration, wherein the repeating unit is independently in the orientation shown or in the opposite orientation a secondary viscosifier, and a crosslinker, wherein the crosslinker comprises at least one of chromium, aluminum, antimony, zirconium, titanium, calcium, boron, iron, silicon, copper, zinc, magnesium, and an ion thereof; and extracting material comprising petroleum from the subterranean formation downhole via a production wellbore. 2. The method of claim 1 , wherein the method is a method of at least one of chemical flooding, polymer flooding, alkaline polymer flooding, alkali-polymer-surfactant enhanced oil recovery, micellar polymer flooding, and surfactant polymer flooding. 3. The method of claim 1 , wherein the placing of the composition in the subterranean formation downhole comprises placing the composition in a producing zone downhole, and wherein the extracting of the material comprising petroleum from the subterranean formation downhole comprises extracting of the material from the producing zone. 4. The method of claim 1 , wherein about 0.001 wt % to about 100 wt % of the composition is the viscosifier polymer. 5. The method of claim 1 , wherein the viscosifier polymer is sufficient such that, as compared to the viscosity provided at a concentration in water at about 25° C. at standard pressure and 100 s −1 , the viscosity provided at the same concentration in water at about 100° C. at standard pressure and 100 s −1 is no more than about 30% to about 50% lower. 6. The method of claim 1 , wherein the viscosifier polymer has about Z 1 mol % of the ethylene repeating unit comprising the —C(O)NH 2 group and has about N 1 mol % of the ethylene repeating unit comprising the —S(O) 2 R 1 group, wherein Z 1 is about 10% to about 90%, and N 1 is about 10% to about 90%. 7. The method of claim 6 , wherein Z 1 +N 1 is about 100%. 8. The method of claim 1 , wherein the viscosifier polymer has a molecular weight of about 5,000,000 g/mol to about 15,000,000 g/mol. 9. The method of claim 1 , wherein L 1 is —C(O)—NH—C(CH 3 ) 2 —CH 2 —. 10. The method of claim 1 , wherein at each occurrence R 3 , R 4 , and R 5 are each —H. 11. The method of claim 1 , wherein at each occurrence —R 1 is independently selected from the group consisting of —H, Na + , K + , Li + , NH 4 + , Zn + , Zn 2+ , Al 3+ , and Mg 2+ . 12. The method of claim 1 , wherein n is 20,000 to about 45,000. 13. The method of claim 1 , wherein z is about 13,500 to about 65,000. 14. The method of claim 1 , wherein the composition further comprises a surfactant. 15. The method of claim 1 , wherein at least one of L 1 or L 2 is the substituted C 1 -C 40 hydrocarbyl. 16. The method of claim 1 , wherein at least one of L 1 or L 2 is the unsubstituted C 1 -C 40 hydrocarbyl. 17. The method of claim 1 , wherein at least one of L 1 or L 2 is the substituted or unsubstituted C 1 -C 40 hydrocarbyl interrupted with 0, 1, 2, or 3 of at least one of —NR 3 , —S—, and —O. 18. The method of claim 1 , wherein at least one of L 1 or L 2 is the substituted or unsubstituted C 1 -C 40 hydrocarbyl terminated with 0, 1, 2, or 3 of at least one of —NR 3 —, —S—, and —O.
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