Vapor-depositing metal oxide on surfaces for wells or pipelines to reduce scale
US-2016290103-A1 · Oct 6, 2016 · US
US9593276B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9593276-B2 |
| Application number | US-201213725376-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 21, 2012 |
| Priority date | Dec 21, 2012 |
| Publication date | Mar 14, 2017 |
| Grant date | Mar 14, 2017 |
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The present invention relates to a polymer including at least one monomer comprising a switchable-amphiphilic functional group. Various embodiments provide a methods of treating a subterranean formation with the polymer, compositions including the polymer, and methods of making compositions including the polymer.
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What is claimed is: 1. A method of treating a subterranean formation comprising: bubbling a gas comprising CO 2 through a combined polymer and liquid comprising water, the liquid comprising water comprising an aqueous fluid comprising, a drilling fluid, stimulation fluid, fracking fluid, spotting fluid, clean-up fluid, production fluid, completion fluid, remedial treatment fluid, abandonment fluid, pill, acidizing fluid, a cementing fluid, or a combination thereof, and the polymer comprising at least one monomer comprising a switchable-amphiphilic functional group, the switchable-amphiphilic functional group comprising an amidine group, wherein the monomer comprising the switchable-amphiphilic functional group has the structure: wherein linking group L 2 independently at each occurrence is (C 5 -C 20 )alkylene, A is the switchable-amphiphilic functional group, having the structure: X − is a counterion, R 1 , R 2 , and R 3 are independently at each occurrence (C 1 -C 5 )alkyl, and bubbling the gas comprising CO 2 through the combined polymer and liquid ionizes the amidine group and forms a latex comprising the liquid and solid particles comprising the polymer; and placing the latex in the subterranean formation; wherein a degree of ionization of the polymer at a first location in the subterranean formation is different than a degree of ionization of the polymer at a second location in the subterranean formation. 2. The method of claim 1 , further comprising increasing an aqueous emulsion of the polymer by ionizing a greater number of the switchable-amphiphilic functional groups. 3. The method of claim 2 , wherein increasing the aqueous emulsion comprises bubbling a gas comprising CO 2 through the liquid comprising water. 4. The method of claim 1 , further comprising decreasing an aqueous emulsion of the polymer by neutralizing the switchable-amphiphilic functional group. 5. The method of claim 4 , wherein lessening the aqueous emulsion comprises at least one of bubbling a gas comprising at least one of a noble gas and N 2 through the aqueous emulsion and applying sufficient heat to the aqueous emulsion. 6. The method of claim 2 , wherein the increasing of the emulsion is performed prior to the placing the polymer in the subterranean formation. 7. The method of claim 4 , wherein the lessening of the emulsion is performed prior to the placing the polymer in the subterranean formation. 8. The method of claim 1 , wherein after the bubbling of the gas comprising CO 2 , the switchable-amphiphilic functional groups in the polymer are predominantly in an ionized form. 9. The method of claim 1 , wherein the drilling fluid, stimulation fluid, fracking fluid, spotting fluid, clean-up fluid, production fluid, completion fluid, remedial treatment fluid, abandomnent fluid, pill, acidizing fluid, and a cementing fluid is a pill, water-based drilling fluid, an aqueous mixture comprising at least one of cement and cement kiln dust, or a combination thereof. 10. The method of claim 1 , wherein the monomer comprising the switchable-amphiphilic functional group is or a salt thereof. 11. The method of claim 1 , wherein the polymer is a copolymer comprising at least two different monomers, wherein in addition to the monomer comprising the switchable-amphi phi lie functional group the polymer further comprises monomer M 2 , wherein M 2 is derived from a compound comprising a vinyl functional group. 12. The method of claim 1 , wherein the polymer is a random copolymer having the following structure wherein the copolymer comprises n units of M 1 and m units of M 2 ; wherein monomers M 1 and M 2 have a random arrangement within the polymer; wherein monomers M 1 and M 2 independently at each occurrence have the orientation shown or the opposite orientation; wherein L 1 is —C(O)—NH—; wherein E independently at each occurrence is selected from the group consisting of hydrogen, F, Cl, Br, I, (C 1 -C 10 )alkoxy, and (C 1 -C 10 )alkyl; wherein D independently at each occurrence is selected from the group consisting of Q, (C 1 -C 10 )alkyl, (C 2 -C 10 )alkenyl, (C 2 -C 10 )alkynyl, (C 1 -C 10 )haloalkyl, (C 1 -C 10 )alkoxy, (C 1 -C 10 )haloalkoxy, (C 4 -C 10 )cycloalkyl(C 0 -C 10 )alkyl, (C 1 -C 10 )heterocyclyl(C 0 -C 10 )alkyl, (C 6 -C 10 )aryl(C 0 -C 10 )alkyl, and (C 1 -C 10 )heteroaryl(C 0 -C 10 )alkyl; wherein each alkyl, alkenyl, alkynyl, haloalkyl, alkoxy, haloalkoxy, cycloalkyl, aryl, heterocyclyl, and heteroaryl is independently unsubstituted or further substituted with at least one J″; wherein Q independently at each occurrence is selected from the group consisting of F, Cl, Br, I, OR″, CF 3 , OCF 3 , R″, CN, C(O), S(O), N(R″) 2 , SR″, S(O)R″, SO 2 R″, SO 2 N(R″) 2 , SO 3 R″, C(O)R″, C(O)C(O)R″, C(O)CH 2 C(O)R″, C(S)R″, C(O)OR″, OC(O)R″, OC(O)OR″, C(O)N(R″) 2 , OC(O)N(R″) 2 , C(S)N(R″) 2 , (CH 2 ) 0-2 NHC(O)R″, N(R″)N(R″)C(O)R″, N(R″)N(R″)C(O)OR″, N(R″)N(R″)C(O)N(R″) 2 , N(R″)SO 2 R″, N(R″)SO 2 N(R″) 2 , N(R″)C(O)OR″, N(R″)C(O)R″, N(R″)C(S)R″, N(R″)C(O)N(R″) 2 , N(R″)C(S)N(R″) 2 , N(C(O)R″)C(O)R″, N(OR″)R″, C(═NH)N(R″) 2 , and C(O)N(OR″)R″; wherein J″ independently at each occurrence is selected from the group consisting of F, Cl, Br, I, OR″, CN, CF 3 , OCF 3 , R″, O, S, C(O), S(O), methylenedioxy, ethylenedioxy, N(R″) 2 , SR″, S(O)R″, SO 2 R″, SO 2 N(R″) 2 , SO 3 R″, C(O)R″, C(O)C(O)R″, C(O)CH 2 C(O)R″, C(S)R″, C(O)OR″, OC(O)R″, OC(O)OR″, C(O)N(R″) 2 , OC(O)N(R″) 2 , C(S)N(R″) 2 , (CH 2 ) 0-2 NHC(O)R″, N(R″)N(R″)C(O)R″, N(R″)N(R″)C(O)OR″, N(R″)N(R″)C(O)N(R″) 2 , N(R″)SO 2 R″, N(R″)SO 2 N(R″) 2 , N(R″)C(O)OR″, N(R″)C(O)R″, N(R″)C(S)R″, N(R″)C(O)N(R″) 2 , N(R″)C(S)N(R″) 2 , N(C(O)R″)C(O)R″, N(OR″)R″, C(═NH)N(R″) 2 , C(O)N(OR″)R″, and C(═NOR″)R″; and wherein R″ is independently at each occurrence is selected from the group consisting of hydrogen, (C 1 -C 10 )alkyl, (C 4 -C 10 )cycloalkyl, (C 4 -C 10 )cycloalkyl(C 1 -C 10 )alkyl, (C 6 -C 10 )aryl, (C 1 -C 10 )aralkyl, (C 1 -C 10 )heterocyclyl, (C 1 -C 10 )heterocyclyl(C 1 -C 10 )alkyl, (C 1 -C 10 )heteroaryl, and (C 1 -C 10 )heteroaryl(C 1 -C 10 )alkyl, wherein each alkyl, cycloalkyl, cycloalkylalkyl, aryl, aralkyl, heterocyclyl, heterocyclylalkyl, heteroaryl, and heteroarylalkyl is independently unsubstituted or substituted with 1-3 J″. 13. The method of claim 1 , wherein the polymer has the following structure: wherein the copolymer comprises n units M 1 , and m units of M 2 , and L 1 is —C(O)—NH—. 14. The method of claim 1 , wherein the mole percent of the monomer comprising the switchable-amphiphilic functional group is about 0.001%-20%. 15. The method of claim 1 , wherein the polymer comprises polymer particles having an average diameter of about 10 nm-1000 nm. 16. The method of claim 1 , wherein the polymer has a degree of polymerization of about 10 to 10,000,000. 17. The method of claim 1 , wherein the drilling fluid, stimulation fluid, fracking flui
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