Sealant compositions for use in subterranean formation operations
US-9796902-B2 · Oct 24, 2017 · US
US12049588B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12049588-B2 |
| Application number | US-202318129662-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 31, 2023 |
| Priority date | Dec 4, 2019 |
| Publication date | Jul 30, 2024 |
| Grant date | Jul 30, 2024 |
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This disclosure describes the composition and methods of use for a novel delayed polymer gelation system for high temperature and high salinity applications. This polymer gelation system includes a polymer of acrylamide, AMPS and 500-5000 ppm polyethylene glycol diacrylate in inverse emulsion form, and a polyethyleneimine (PEI) with a MW of 2,000-30,000 daltons as the crosslinking agent.
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What is claimed is: 1. A polymer system comprising: a polymer comprising: acrylamide; 2-acrylamido-2-methylpropane sulfonic acid (AMPS); polyethylene glycol diacrylate; and sodium formate; a crosslinker comprising polyethyleneimine; and a temperature stabilizer; wherein the polymer is in inverse emulsion form. 2. The polymer system of claim 1 wherein the polymer is at a concentration of about 25-35%. 3. The polymer system of claim 1 wherein the polymer comprises: about 50-90% acrylamide; about 10-50% AMPS; about 500-5000 ppm polyethylene glycol diacrylate; and about 100-2000 ppm sodium formate; wherein the crosslinker comprises about 100-1500 ppm polyethyleneimine. 4. The polymer system of claim 3 wherein the polymer comprises: about 80% acrylamide; about 20% AMPS; about 500 ppm polyethylene glycol diacrylate; and about 400 ppm sodium formate; wherein the crosslinker comprises about 1200 ppm polyethyleneimine. 5. The polymer system of claim 3 wherein the polymer comprises: about 60% acrylamide; about 40% AMPS; about 500 ppm polyethylene glycol diacrylate; and about 400 ppm sodium formate; wherein the crosslinker comprises about 200 ppm polyethyleneimine. 6. The polymer system of claim 1 wherein the crosslinker comprises polyethyleneimine at a molecular weight of about 2,000-30,000 daltons. 7. The polymer system of claim 6 wherein the polyethyleneimine has a molecular weight of about 10,000 daltons. 8. The polymer system of claim 1 wherein the temperature stabilizer comprises about 0.02-0.1 wt % thiourea. 9. The polymer system of claim 1 wherein the viscosity of the polymer system is about 1-10 cp before gelation. 10. The polymer system of claim 1 wherein the polymer system undergoes gelation at a temperature between about 80-130 degrees Celsius and wherein the polymer gel is formed in a brine with total dissolved solids in the range of about 50,000 mg/L to 200,000 mg/L. 11. A method of improving sweep efficiency for an oil-bearing zone comprising: preparing a polymer system comprising: a polymer comprising: acrylamide; 2-acrylamido-2-methylpropane sulfonic acid (AMPS); polyethylene glycol diacrylate; and sodium formate; a crosslinker comprising polyethyleneimine; and a temperature stabilizer; wherein the polymer is in inverse emulsion form; and injecting the polymer system into a wellbore to improve the sweep efficiency. 12. The method of claim 11 wherein the polymer is at a concentration of about 25-35% in the inverse emulsion. 13. The method of claim 11 wherein the polymer comprises about 50-90% acrylamide; about 10-50% AMPS; about 500-5000 ppm polyethylene glycol diacrylate; and about 100-2000 ppm sodium formate; wherein the crosslinker comprises about 100-1500 ppm polyethyleneimine. 14. The method of claim 13 wherein the polymer comprises about 80% acrylamide; about 20% AMPS; about 500 ppm polyethylene glycol diacrylate; and about 400 ppm sodium formate; wherein the crosslinker comprises about 1200 ppm polyethyleneimine. 15. The method of claim 13 wherein the polymer comprises about 60% acrylamide; about 40% AMPS; about 500 ppm polyethylene glycol diacrylate; and about 400 ppm sodium formate; wherein the crosslinker comprises about 200 ppm polyethyleneimine. 16. The method of claim 11 wherein the crosslinker comprises polyethyleneimine at a molecular weight of about 2,000-30,000 daltons. 17. The method of claim 16 wherein the polyethyleneimine has a molecular weight of about 10,000 daltons. 18. The method of claim 11 wherein the temperature stabilizer comprises about 0.02-0.1 wt % thiourea. 19. The method of claim 11 wherein the viscosity of the polymer system is about 1-10 cp before gelation. 20. The method of claim 11 wherein the polymer system undergoes gelation at a temperature between about 80-130 degrees Celsius and wherein the polymer gel is formed in a brine with total dissolved solids in the range of about 50,000 mg/L to 200,000 mg/L.
Enhanced recovery methods for obtaining hydrocarbons · CPC title
containing cross-linking agents · CPC title
obtained by reactions only involving carbon-to-carbon unsaturated bonds · CPC title
Oil-based compositions · CPC title
characterised by the use of specific polymers {(polymeric surfactants C09K8/584)} · CPC title
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