Weak gel system for chemical enhanced oil recovery
US-2017145292-A1 · May 25, 2017 · US
US11787888B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11787888-B2 |
| Application number | US-201917413988-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 17, 2019 |
| Priority date | Dec 26, 2018 |
| Publication date | Oct 17, 2023 |
| Grant date | Oct 17, 2023 |
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The present disclosure relates to the technical field of oilfield chemicals, and discloses an acrylamide copolymer, wherein the acrylamide copolymer comprises a structural unit A, a structural unit B and a structural unit C, wherein the structural unit A has a structure shown in Formula (1), the structural unit B has a structure shown in Formula (2), and the structural unit C has a structure shown in Formula (3) and/or Formula (4); wherein R 1 is methyl or H, R 2 is —OH, —NH 2 , —COOH or C 2 -C 12 alkyl, n is an integer between 0 and 6, and a, b and c are each independently selected from integers between 0 and 2.
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The invention claimed is: 1. An acrylamide copolymer, wherein the acrylamide copolymer comprises a structural unit A, a structural unit B, and a structural unit C, wherein the structural unit A has a structure shown in Formula (1), the structural unit B has a structure shown in Formula (2), and the structural unit C has a structure shown in Formula (3) and/or Formula (4); wherein R 1 is methyl or H, R 2 is —OH, —NH 2 , —COOH or C 2 -C 12 alkyl, n is an integer in a range of 0-6, and a, b and c are each independently selected from integers in a range of 0-2. 2. The acrylamide copolymer of claim 1 , wherein the content of the structural unit A is within a range of 85-95 wt %, the content of the structural unit B is within a range of 0.5-5 wt %, and the content of the structural unit C is within a range of 1-10 wt %, based on the total weight of the acrylamide copolymer. 3. The acrylamide copolymer of claim 1 , wherein the viscosity average molecular weight of the acrylamide copolymer is within a range of 27,000,000-32,000,000. 4. A method for preparing an acrylamide copolymer, comprising: (1) subjecting a monomer mixture to a polymerization reaction in water under the conditions of solution polymerization and in the presence of an initiator, so as to obtain a copolymer colloid; wherein the monomer mixture comprises (meth)acrylamide, monomer X, and monomer Y, wherein the monomer X has a structure shown in Formula (5), and the monomer Y has a structure shown in Formula (6) and/or Formula (7); wherein R 2 is —OH, —NH 2 , —COOH or C 2 -C 12 alkyl, n is an integer in a range of 0-6, and a, b and c are each independently selected from integers in a range of 0-2; and (2) subjecting the copolymer colloid to a hydrolysis reaction to prepare the acrylamide copolymer. 5. The method of claim 4 , wherein the monomer mixture is used in an amount of 20-40 parts by weight relative to 100 parts by weight of water. 6. The method of claim 4 , wherein the conditions of the solution polymerization reaction comprise: the solution polymerization reaction is carried out in an inert atmosphere, the initiator is an oxidation-reduction system initiator, the temperature is in a range of 20-40° C., the time is in a range of 8-10 h, and the pH is in a range of 6-10. 7. The method of claim 6 , wherein the oxidation-reduction system initiator is a persulfate oxidizer and a sulfite reducer. 8. The method of claim 4 , wherein the conditions of the hydrolysis reaction comprise that the temperature is in a range of 80-90° C. and the time is in a range of 2-3 h. 9. The acrylamide copolymer of claim 2 , wherein the content of the structural unit A is within a range of 88-95 wt %, the content of the structural unit B is within a range of 0.5-3 wt %, and the content of the structural unit C is within a range of 1-9 wt %, based on the total weight of the acrylamide copolymer. 10. The acrylamide copolymer of claim 3 , wherein the viscosity average molecular weight of the acrylamide copolymer is within a range of 27,000,000-32,000,000. 11. The method of claim 5 , wherein the (meth) acrylamide is used in an amount of 85-95 wt. %, the monomer X is used in an amount of 0.5-5 wt. %, and the monomer Y is used in an amount of 1-10 wt. %, based on the total amount of the monomer mixture. 12. The method of claim 11 , wherein the (meth) acrylamide is used in an amount of 88-95 wt %, the monomer X is used in an amount of 0.5-3 wt %, and the monomer Y is used in an amount of 1-9 wt %, based on the total amount of the monomer mixture. 13. The method of claim 4 , wherein the solution polymerization conditions further comprise: the polymerization is performed in the presence of an emulsifier, a complexing agent, urea, and an accelerator. 14. The method of claim 13 , wherein the used amount of the oxidation-reduction system initiator is 0.015-0.15 part by weight, the used amount of the emulsifier is 0.05-1 part by weight, the used amount of the complexing agent is 0.01-0.1 part by weight, the used amount of the urea is 0.5-5 parts by weight, and the used amount of the accelerator is 0.2-1 part by weight, relative to 100 parts by weight of the monomer mixture. 15. The method of claim 13 , wherein the emulsifier is sodium dodecyl sulfate and/or sodium dodecyl benzene sulfonate. 16. The method of claim 13 , wherein the complexing agent is disodium ethylenediaminetetraacetate. 17. The method of claim 13 , wherein the accelerator is pentamethyl diethylenetriamine.
Acrylamide; Methacrylamide · CPC title
Aqueous solvent · CPC title
containing oxygen in addition to the carbonamido oxygen {, e.g. N-methylolacrylamide, N-(meth)acryloylmorpholine} · CPC title
by a heterocyclic ring containing nitrogen · CPC title
characterised by the use of specific polymers {(polymeric surfactants C09K8/584)} · CPC title
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