IP Library Granted Patent US 7,482,310
Granted Patent B1
US 7,482,310 · App. 10/988,216 · Granted Jan 27, 2009

Method of fracturing subterranean formations utilizing emulsions comprising acrylamide copolymers

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Quick Facts
Patent No.
US 7,482,310
App. No.
10/988,216
Granted
Jan 27, 2009
Kind
B1
Abstract

A method of treating a subterranean formation penetrated by a well bore including: (a) preparing a fracturing fluid containing a mixture resulting from: (I) providing a water-in-oil emulsion composition that includes: (i) 5% to 99% by weight of a water-in-oil emulsion polymer comprising a polymer or copolymer containing repeat units from an acrylamide monomer; (ii) 0.5% to 90% by weight of a carrier solvent; and (iii) 0 to 90% by weight of a fluidizing agent; and adding (iv) 0.1% to 10% by weight of one or more inorganic microparticles, where the total of all components is 100% by weight; and (II) adding the water-in-oil emulsion composition to water; and (b) contacting the subterranean formation with the fracturing fluid.

Claims (70)

1. A method of treating a subterranean formation penetrated by a well bore comprising:

(a) preparing a fracturing fluid containing a mixture resulting from:

(I) providing a water-in-oil emulsion composition comprising:

(i) 5% to 99% by weight of a water-in-oil emulsion comprising:

(1) 10% to 90% by weight of a hydrophobic oil phase;

(2) 0.5% to 10% by weight of a surfactant system; and

(3) 5% to 90% by weight of a polymer-containing aqueous phase comprising water and a polymer or copolymer containing repeat units from an acrylamide monomer, wherein the polymer or copolymer comprises from 2% by weight to 89.5% by weight of the water-in-oil emulsion;

(ii) 0.5% to 90% by weight of a carrier solvent; and

(iii) 0 to 90% by weight of a fluidizing agent;

and adding

(iv) 0.1% to 10% by weight of one or more inorganic microparticles, where the total of all components is 100% by weight; and

(II) adding the water-in-oil emulsion composition to water; and

(b) contacting the subterranean formation with the fracturing fluid.

2. The method of claim 1 , wherein the fracturing fluid further comprises (v) 1% to 50% by weight of a proppant material.

3. The method of claim 2 , wherein the proppant material is selected from the group consisting of resin coated or uncoated sand, sintered bauxite, ceramic materials and glass beads.

4. The method of claim 2 , wherein the proppant material is present in the fracturing fluid in an amount in the range of from about 0.1 to about 10 pounds of proppant material per gallon of the fracturing fluid.

5. The method of claim 1 , the oil phase comprises one or more oils selected from the group consisting of mineral oil, synthetic oil, modified oil, paraffinic oil, benzene, xylene, toluene, kerosene, napthas, petroleums, blends of aromatic and aliphatic hydrocarbons containing 4 or greater carbon atoms, and vegetable oil.

6. The method of claim 1 , wherein the surfactant system comprises of one or more surfactants selected from the group consisting of alkanolamides, polyoxyethylene derivatives of sorbitan esters, sorbitan monooleate, sorbitan monostearate, C 6 -C 22 linear or branched alkyl ethoxylates with 1 to 30 oxyethylene units, C 6 -C 22 linear or branched alkyl propoxylate with 1 to 30 oxypropylene units, C 6 -C 22 linear or branched alkyl ethoxylate/propoxylate with 1 to 30 combined oxyethylene and propoxylate units, alkylaryl ethoxylates containing a C 6 -C 22 aryl group with 1 to 30 oxyethylene units, hexadecyl sodium phthalate, cetyl sodium phthalate, stearyl sodium phthalate and ethylene oxide condensates of fatty acid amides.

7. The method of claim 1 , wherein the polymer or copolymer of the aqueous phase is selected from non-ionic poly(acrylamide) homopolymer, non-ionic copolymers, anionic copolymers, cationic copolymers, amphoteric copolymers and ampholytic copolymers.

8. The method of claim 1 , wherein the polymer or copolymer comprises one or more repeat units according to formula I:

wherein each occurrence of R 1 is independently selected from H, methyl and ethyl; n is an integer from 10 to 10,000,000; Z is —NR 2 —; and each occurrence of R 2 is independently selected from the group consisting of H, C 1 -C 22 linear, branched or cyclic alkyl, aryl, alkaryl, aralkyl or alkenyl, a group —R 3 —NR 2 2 , a group —R 3 —N + R 2 3 X, and a group —R 3 —SO 3 Y, wherein R 2 is as previously defined, R 3 is a divalent linking group selected from the group consisting of C 1 -C 22 linear, branched or cyclic alkylene, arylene, alkarylene, aralkylene or alkenylene, poly(ethyleneoxide) and poly(propyleneoxide); Y is H or an alkali metal ion; and X is a halide or methylsulfate.

9. The method of claim 1 , wherein the copolymer of the aqueous phase further comprises repeat units derived from acrylamidopropyl-trimethyl ammonium chloride, methacrylamidopropyltrimethyl ammonium chloride, methacryloyloxyethyl trimethyl ammonium chlorides methacryloyloxyethyl trimethyl ammonium methylsulfate, acryloyloxyethyl trimethyl ammonium chloride, dimethyl diallyl ammonium chloride, acrylic acid, methacrylic acid, 2-acrylamido-2-methylpropane sulfonic acid, 2-methacrylamido-2-methylpropane sulfonic acid, C 1 -C 3 alkyl acrylate, C 1 -C 3 alkyl methacrylate, n-alkyl acrylamide, methacrylamide, n-alkylmethacrylamide and diacetone acrylamide.

10. The method of claim 1 , wherein the polymer or copolymer of the aqueous phase has a reduced viscosity, measured using a Ubbelohde Capillary Viscometer at 0.05 g/dl in 1N NaCl at 30° C. and pH of 7 of from 5 to 50 dl/g.

11. The method of claim 1 , wherein the inorganic microparticles (iv) include one or more microparticles selected from the group consisting of fumed silica, precipitated silica, colloidal silica, alumina silicates, surface treated silica, calcium carbonate, talc and borosilicates.

12. The method of claim 1 , wherein the inorganic microparticles (iv) include one or more microparticles selected from the group consisting of fumed silica, precipitated silica, silica flour, diatomites and colloidal silica.

13. The method of claim 1 , wherein the carrier solvent (ii) is one or more selected from the group consisting of mineral oil, synthetic oil, modified oil, paraffinic oil, vegetable oil, ethylene carbonate, propylene carbonate, glycols, polyglycols, and glycol ethers.

14. The method of claim 1 , wherein the carrier solvent (ii) is a solvent characterized as having Hansen Solubility parameters at 25° C. of:

δ d of from 13 to 18;

δ p of from 6 to 12;

δ h of at least 20; and

δ t of at least 20.

15. The method of claim 1 , wherein the water is selected from the group consisting of fresh water, unsaturated brine and saturated brine.

16. The method of claim 1 , wherein the fracturing fluid further comprises one or more polymers selected from the group consisting of hydroxypropylguar, carboxymethylhydroxypropylguar, carboxymethylguar, hydroxyethyl cellulose, grafted hydroxyethyl cellulose, carboxymethyl cellulose and carboxymethylhydroxyethyl cellulose.

17. The method of claim 1 , wherein the water-in-oil emulsion composition is present in the treating fluid in an amount in the range of from about 0.01% to about 10% by weight of the fracturing fluid.

18. The method of claim 1 , wherein the fracturing fluid further comprises from 0.01% to 0.1% by weight of a surfactant selected from the group consisting of C 2 -C 24 linear, branched and cyclic alkyl phenol ethoxylates, C 2 -C 24 linear, branched and cyclic alkyl ethoxylates, alkyl sulfonates, alkyl aryl sulfonates such as the salts of dodecylbenzene sulfonic acid, alkyltrimethylammonium chloride, branched alkyl ethoxylated alcohols, phenol-formaldehyde nonionic resin blends, cocobetaines, dioctyl sodium sulfosuccinate, imidazolines, alpha olefin sulfonates, linear alkyl ethoxylated alcohols and trialkyl benzylammonium chloride.

19. The method of claim 1 , wherein the fracturing fluid further comprises from 0.01% to 1% by weight a fluid loss control agent selected from the group consisting of silica flour, starches, waxes and resins.

20. The method of claim 1 , wherein the fracturing fluid further comprises from 0.01 to 2% by weight of a delayed breaker for causing the treating fluid to revert to a thin fluid comprising oxidizers and encapsulated oxidizers selected from the group consisting of sodium persulfate, potassium persulfate, ammonium persulfate, magnesium peroxide, sodium chlorite, sodium bromate, halogenated isocyanurate, and hypochlorites.

21. The method of claim 1 , further comprising the step of (c) mixing a proppant material with at least a portion of the fracturing fluid.

22. The method of claim 1 , wherein the polymer or copolymer containing repeat units from an acrylamide monomer further comprises one or more repeat units according to Formula I:

wherein each occurrence of R 1 is independently selected from H, methyl and ethyl; n is an integer from 10 to 10,000,000; and each occurrence of R 2 is independently selected from the group consisting of H, C 1 -C 22 linear, branched or cyclic alkyl, aryl, alkaryl, aralkyl or alkenyl, a group —R 3 —NR 2 2 , a group —R 3 —N + R 2 3 X, and a group —R 3 —SO 3 Y, wherein R 1 is as previously defined; R 3 is a divalent linking group selected from the group consisting of C 1 -C 22 linear, branched or cyclic alkylene, arylene, alkarylene, aralkylene or alkenylene, poly(ethyleneoxide) and poly(propyleneoxide); Y is H or an alkali metal ion; and X is a halide or methylsulfate.

23. A method of treating a subterranean formation penetrated by a well bore comprising:

(a) preparing a fracturing fluid containing a mixture resulting from:

(I) providing a water-in-oil emulsion composition comprising:

(i) 5% to 99% by weight of a water-in-oil emulsion comprising a polymer or copolymer containing repeat units from an acrylamide monomer;

(ii) 0.5% to 90% by weight of a carrier solvent; and

(iii) 0 to 90% by weight of a fluidizing agent;

and adding

(iv) 0.1% to 10% by weight of one or more inorganic microparticles, where the total of all components is 100% by weight; and

(II) adding the water-in-oil emulsion composition to water; and

(b) contacting the subterranean formation with the fracturing fluid, wherein the fracturing fluid further comprises 0.01% to 0.3% by weight of a pH adjusting compound for elevating the pH of the treating fluid selected from the group consisting of sodium hydroxide, potassium hydroxide and lithium hydroxide.

24. A method of treating a subterranean formation penetrated by a well bore comprising:

(a) preparing a fracturing fluid containing a mixture resulting from:

(I) providing a water-in-oil emulsion composition comprising:

(i) 5% to 99% by weight of a water-in-oil emulsion comprising a polymer or copolymer containing repeat units from an acrylamide monomer;

(ii) 0.5% to 90% by weight of a carrier solvent; and

(iii) 0 to 90% by weight of a fluidizing agent;

and adding

(iv) 0.1% to 10% by weight of one or more inorganic microparticles, where the total of all components is 100% by weight; and

(II) adding the water-in-oil emulsion composition to water; and

(b) contacting the subterranean formation with the fracturing fluid, wherein the fracturing fluid further comprises from 0.01% to 0.3% by weight of a pH adjusting compound selected from the group consisting of sodium hydroxide, potassium hydroxide, lithium hydroxide, ammonia, sodium carbonate, potassium carbonate, sodium bicarbonate, potassium bicarbonate, sodium diacetate, potassium diacetate, sodium phosphate, potassium phosphate, sodium dihydrogen phosphate, potassium dihydrogen phosphate, and mixtures thereof.

25. A method of treating a subterranean formation penetrated by a well bore comprising:

(a) preparing a fracturing fluid containing a mixture resulting from:

(I) providing a water-in-oil emulsion composition comprising:

(i) 5% to 99% by weight of a water-in-oil emulsion comprising a polymer or copolymer containing repeat units from an acrylamide monomer;

(ii) 0.5% to 90% by weight of a carrier solvent; and

(iii) 0 to 90% by weight of a fluidizing agent;

and adding

(iv) 0.1% to 10% by weight of one or more inorganic microparticles, where the total of all components is 100% by weight; and

(II) adding the water-in-oil emulsion composition to water; and

(b) contacting the subterranean formation with the fracturing fluid, wherein the fracturing fluid further comprises from 0.1% to 10% by weight of a clay stabilizer selected from the group consisting of potassium chloride, sodium chloride, ammonium chloride, tetramethyl ammonium chloride and temporary clay stabilizers.

Assignments (15)
RELEASE OF SECURITY INTEREST FILED OCTOBER 31, 2019 AT REEL/FRAME 050897/0314 Recorded Sep 1, 2023
From: BARCLAYS BANK PLC
To: KEANE FRAC, LP; C&J SPEC-RENT SERVICES, INC. N/K/A NEXTIER COMPLETION SOLUTIONS INC.; KING MERGER SUB II LLC; C&L WELL SERVICES, INC.; KEANE GROUP HOLDINGS, LLC
Reel/Frame 064802/0830 →
RELEASE OF SECURITY INTEREST FILED OCTOBER 31, 2019 AT REEL/FRAME 050897/0470 Recorded Sep 1, 2023
From: BANK OF AMERICA, N.A.
To: KEANE FRAC, LP; C&J SPEC-RENT SERVICES, INC. N/K/A NEXTIER COMPLETION SOLUTIONS INC.; KING MERGER SUB II LLC; C&J WELL SERVICES, INC.; KEANE GROUP HOLDINGS, LLC
Reel/Frame 064803/0057 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 6, 2020
From: C&J WELL SERVICES, INC.
To: NEXTIER COMPLETION SOLUTIONS INC.
Reel/Frame 052043/0620 →
ABL SECURITY AGREEMENT Recorded Oct 31, 2019
From: C&J SPEC-RENT SERVICES, INC.; C&J WELL SERVICES, INC.; KING MERGER SUB II LLC (F/K/A C&J ENERGY SERVICES, INC.); KEANE FRAC, LP; KEANE GROUP HOLDINGS, LLC
To: BANK OF AMERICA, N.A.
Reel/Frame 050897/0470 →
TL SECURITY AGREEMENT Recorded Oct 31, 2019
From: C&J SPEC-RENT SERVICES, INC.; C&J WELL SERVICES, INC.; KING MERGER SUB II LLC (F/K/A C&J ENERGY SERVICES, INC.); KEANE FRAC, LP; KEANE GROUP HOLDINGS, LLC
To: BARCLAYS BANK PLC
Reel/Frame 050897/0314 →
RELEASE OF SECURITY INTEREST Recorded Jan 13, 2017
From: CORTLAND CAPITAL MARKET SERVICES LLC
To: C&J SPEC-RENT SERVICES, INC.
Reel/Frame 040969/0952 →
RELEASE OF SECURITY INTEREST Recorded Jan 13, 2017
From: CORTLAND CAPITAL MARKET SERVICES LLC
To: C&J WELL SERVICES, INC.
Reel/Frame 040974/0861 →
SECURITY AGREEMENT Recorded Aug 12, 2016
From: C&J WELL SERVICES, INC.; C&J SPEC-RENT SERVICES, INC.; C&J ENERGY PRODUCTION SERVICES-CANADA LTD.
To: CORTLAND CAPITAL MARKET SERVICES LLC, AS ADMINISTRATIVE AGENT
Reel/Frame 039665/0148 →
SUCCESSOR AGENT AGREEMENT Recorded Jul 21, 2016
From: BANK OF AMERICA, N.A., AS ADMINISTRATIVE AGENT
To: CORTLAND CAPITAL MARKET SERVICES LLC, AS ADMINISTRATIVE AGENT
Reel/Frame 039421/0624 →
CHANGE OF NAME Recorded Jun 30, 2015
From: NABORS COMPLETION & PRODUCTION SERVICES CO.
To: C&J WELL SERVICES, INC.
Reel/Frame 036050/0511 →
CHANGE OF NAME Recorded Jun 25, 2015
From: SUPERIOR WELL SERVICES, INC.
To: NABORS COMPLETION & PRODUCTION SERVICES CO.
Reel/Frame 036028/0831 →
SECURITY INTEREST Recorded Apr 1, 2015
From: NABORS COMPLETION & PRODUCTION SERVICES CO.
To: BANK OF AMERICA, N.A., AS ADMINISTRATIVE AGENT
Reel/Frame 035310/0163 →
CHANGE OF NAME Recorded Mar 6, 2015
From: SUPERIOR WELL SERVICES, INC.
To: NABORS COMPLETION & PRODUCTION SERVICES CO.
Reel/Frame 035139/0083 →
CORRECTIVE ASSIGNMENT PREVIOUSLY RECORDED AT REEL 016299 FRAME 0007. Recorded Aug 26, 2005
From: REESE, RHYS R.; REY, PAUL
To: KROFF CHEMICAL COMPANY, INC.; SUPERIOR WELL SERVICES, INC.
Reel/Frame 016517/0512 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 24, 2005
From: REESE, RHYS R.; REY, PAUL
To: KROFF CHEMICAL COMPANY, INC.
Reel/Frame 016299/0007 →