US20080200351A1 - Method of recycling fracturing fluids using a self-degrading foaming composition - Google Patents
Method of recycling fracturing fluids using a self-degrading foaming composition Download PDFInfo
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- US20080200351A1 US20080200351A1 US12/148,638 US14863808A US2008200351A1 US 20080200351 A1 US20080200351 A1 US 20080200351A1 US 14863808 A US14863808 A US 14863808A US 2008200351 A1 US2008200351 A1 US 2008200351A1
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- self
- aryl
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- 239000012530 fluid Substances 0.000 title claims abstract description 73
- 239000000203 mixture Substances 0.000 title claims abstract description 46
- 238000005187 foaming Methods 0.000 title claims abstract description 32
- 238000000034 method Methods 0.000 title abstract description 8
- 238000004064 recycling Methods 0.000 title description 14
- 239000006260 foam Substances 0.000 claims abstract description 60
- 239000003945 anionic surfactant Substances 0.000 claims abstract description 15
- 239000002736 nonionic surfactant Substances 0.000 claims abstract description 12
- -1 alkyl naphthalene sulfonate Chemical compound 0.000 claims description 19
- 125000000217 alkyl group Chemical group 0.000 claims description 14
- USIUVYZYUHIAEV-UHFFFAOYSA-N diphenyl ether Chemical compound C=1C=CC=CC=1OC1=CC=CC=C1 USIUVYZYUHIAEV-UHFFFAOYSA-N 0.000 claims description 14
- 239000007789 gas Substances 0.000 claims description 13
- 125000003118 aryl group Chemical group 0.000 claims description 12
- 230000032683 aging Effects 0.000 claims description 11
- 125000004432 carbon atom Chemical group C* 0.000 claims description 10
- 235000014113 dietary fatty acids Nutrition 0.000 claims description 9
- 239000000194 fatty acid Substances 0.000 claims description 9
- 229930195729 fatty acid Natural products 0.000 claims description 9
- 239000001257 hydrogen Substances 0.000 claims description 7
- 229910052739 hydrogen Inorganic materials 0.000 claims description 7
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims description 6
- 125000000278 alkyl amino alkyl group Chemical group 0.000 claims description 6
- 125000004948 alkyl aryl alkyl group Chemical group 0.000 claims description 6
- 125000002877 alkyl aryl group Chemical group 0.000 claims description 6
- 125000003710 aryl alkyl group Chemical group 0.000 claims description 6
- 239000004305 biphenyl Substances 0.000 claims description 6
- 235000010290 biphenyl Nutrition 0.000 claims description 6
- 125000006267 biphenyl group Chemical group 0.000 claims description 6
- 125000001624 naphthyl group Chemical group 0.000 claims description 6
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 claims description 6
- ZUOUZKKEUPVFJK-UHFFFAOYSA-N phenylbenzene Natural products C1=CC=CC=C1C1=CC=CC=C1 ZUOUZKKEUPVFJK-UHFFFAOYSA-N 0.000 claims description 6
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 4
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims description 4
- 239000002202 Polyethylene glycol Substances 0.000 claims description 4
- 239000003349 gelling agent Substances 0.000 claims description 4
- 125000001183 hydrocarbyl group Chemical group 0.000 claims description 4
- 229920001223 polyethylene glycol Polymers 0.000 claims description 4
- 229910052708 sodium Inorganic materials 0.000 claims description 4
- 239000011734 sodium Substances 0.000 claims description 4
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 claims description 3
- ULUAUXLGCMPNKK-UHFFFAOYSA-N Sulfobutanedioic acid Chemical compound OC(=O)CC(C(O)=O)S(O)(=O)=O ULUAUXLGCMPNKK-UHFFFAOYSA-N 0.000 claims description 3
- 229910052783 alkali metal Inorganic materials 0.000 claims description 3
- 150000001340 alkali metals Chemical class 0.000 claims description 3
- 150000001875 compounds Chemical class 0.000 claims description 3
- 150000002314 glycerols Chemical class 0.000 claims description 3
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 claims description 3
- 229910052700 potassium Inorganic materials 0.000 claims description 3
- 239000011591 potassium Substances 0.000 claims description 3
- JNYAEWCLZODPBN-JGWLITMVSA-N (2r,3r,4s)-2-[(1r)-1,2-dihydroxyethyl]oxolane-3,4-diol Chemical class OC[C@@H](O)[C@H]1OC[C@H](O)[C@H]1O JNYAEWCLZODPBN-JGWLITMVSA-N 0.000 claims description 2
- SQAINHDHICKHLX-UHFFFAOYSA-N 1-naphthaldehyde Chemical compound C1=CC=C2C(C=O)=CC=CC2=C1 SQAINHDHICKHLX-UHFFFAOYSA-N 0.000 claims description 2
- 150000003863 ammonium salts Chemical class 0.000 claims description 2
- 239000002280 amphoteric surfactant Substances 0.000 claims description 2
- YRIUSKIDOIARQF-UHFFFAOYSA-N dodecyl benzenesulfonate Chemical compound CCCCCCCCCCCCOS(=O)(=O)C1=CC=CC=C1 YRIUSKIDOIARQF-UHFFFAOYSA-N 0.000 claims description 2
- 150000002431 hydrogen Chemical group 0.000 claims description 2
- 239000004711 α-olefin Substances 0.000 claims description 2
- 239000004971 Cross linker Substances 0.000 claims 5
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical group [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 claims 2
- 229910052796 boron Inorganic materials 0.000 claims 2
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims 1
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical group [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 claims 1
- 239000007864 aqueous solution Substances 0.000 claims 1
- 229910021538 borax Inorganic materials 0.000 claims 1
- 239000004327 boric acid Substances 0.000 claims 1
- 125000005619 boric acid group Chemical group 0.000 claims 1
- 239000003093 cationic surfactant Substances 0.000 claims 1
- 229910021540 colemanite Inorganic materials 0.000 claims 1
- 229940071161 dodecylbenzenesulfonate Drugs 0.000 claims 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims 1
- 239000004328 sodium tetraborate Substances 0.000 claims 1
- 235000010339 sodium tetraborate Nutrition 0.000 claims 1
- TYLSDQJYPYQCRK-UHFFFAOYSA-N sulfo 4-amino-4-oxobutanoate Chemical compound NC(=O)CCC(=O)OS(O)(=O)=O TYLSDQJYPYQCRK-UHFFFAOYSA-N 0.000 claims 1
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 claims 1
- 229910052719 titanium Inorganic materials 0.000 claims 1
- 239000010936 titanium Substances 0.000 claims 1
- 229910021539 ulexite Inorganic materials 0.000 claims 1
- 229910052726 zirconium Inorganic materials 0.000 claims 1
- 239000002888 zwitterionic surfactant Substances 0.000 claims 1
- 230000015572 biosynthetic process Effects 0.000 description 19
- 238000005755 formation reaction Methods 0.000 description 19
- 239000007788 liquid Substances 0.000 description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 18
- 239000004094 surface-active agent Substances 0.000 description 14
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 12
- 239000001569 carbon dioxide Substances 0.000 description 6
- 229910002092 carbon dioxide Inorganic materials 0.000 description 6
- 239000000463 material Substances 0.000 description 6
- 150000003839 salts Chemical class 0.000 description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 5
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical group CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 5
- 239000000654 additive Substances 0.000 description 5
- 238000002156 mixing Methods 0.000 description 4
- BCFOOQRXUXKJCL-UHFFFAOYSA-N 4-amino-4-oxo-2-sulfobutanoic acid Chemical class NC(=O)CC(C(O)=O)S(O)(=O)=O BCFOOQRXUXKJCL-UHFFFAOYSA-N 0.000 description 3
- 0 CC.CC.[1*]C1=CC=C(OC2=CC=CC=C2)C=C1.[1*]CC.[1*]N([2*])C(=O)CC(C)C.[1*]OCOCC(C)COC Chemical compound CC.CC.[1*]C1=CC=C(OC2=CC=CC=C2)C=C1.[1*]CC.[1*]N([2*])C(=O)CC(C)C.[1*]OCOCC(C)COC 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 230000000996 additive effect Effects 0.000 description 3
- 125000000129 anionic group Chemical group 0.000 description 3
- 239000000872 buffer Substances 0.000 description 3
- 239000013530 defoamer Substances 0.000 description 3
- 239000000839 emulsion Substances 0.000 description 3
- 229920006395 saturated elastomer Polymers 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- OMDQUFIYNPYJFM-XKDAHURESA-N (2r,3r,4s,5r,6s)-2-(hydroxymethyl)-6-[[(2r,3s,4r,5s,6r)-4,5,6-trihydroxy-3-[(2s,3s,4s,5s,6r)-3,4,5-trihydroxy-6-(hydroxymethyl)oxan-2-yl]oxyoxan-2-yl]methoxy]oxane-3,4,5-triol Chemical compound O[C@@H]1[C@@H](O)[C@@H](O)[C@@H](CO)O[C@@H]1OC[C@@H]1[C@@H](O[C@H]2[C@H]([C@@H](O)[C@H](O)[C@@H](CO)O2)O)[C@H](O)[C@H](O)[C@H](O)O1 OMDQUFIYNPYJFM-XKDAHURESA-N 0.000 description 2
- OVSKIKFHRZPJSS-UHFFFAOYSA-N 2,4-D Chemical compound OC(=O)COC1=CC=C(Cl)C=C1Cl OVSKIKFHRZPJSS-UHFFFAOYSA-N 0.000 description 2
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 2
- QXNVGIXVLWOKEQ-UHFFFAOYSA-N Disodium Chemical compound [Na][Na] QXNVGIXVLWOKEQ-UHFFFAOYSA-N 0.000 description 2
- 229920000926 Galactomannan Polymers 0.000 description 2
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 description 2
- YDDMAENQLMOJKD-UHFFFAOYSA-N S(=O)(=O)(O)C(C(=O)O)CC(=O)N.C(O)CN.C(CCCCCCCCCCC)(=O)N Chemical compound S(=O)(=O)(O)C(C(=O)O)CC(=O)N.C(O)CN.C(CCCCCCCCCCC)(=O)N YDDMAENQLMOJKD-UHFFFAOYSA-N 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- 239000003570 air Substances 0.000 description 2
- 238000013459 approach Methods 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 239000004088 foaming agent Substances 0.000 description 2
- 150000004676 glycans Chemical class 0.000 description 2
- 229920000591 gum Polymers 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 150000007524 organic acids Chemical class 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 229920001282 polysaccharide Polymers 0.000 description 2
- 239000005017 polysaccharide Substances 0.000 description 2
- 239000012266 salt solution Substances 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- 239000003381 stabilizer Substances 0.000 description 2
- MPNXSZJPSVBLHP-UHFFFAOYSA-N 2-chloro-n-phenylpyridine-3-carboxamide Chemical compound ClC1=NC=CC=C1C(=O)NC1=CC=CC=C1 MPNXSZJPSVBLHP-UHFFFAOYSA-N 0.000 description 1
- 244000215068 Acacia senegal Species 0.000 description 1
- 244000106483 Anogeissus latifolia Species 0.000 description 1
- 235000011514 Anogeissus latifolia Nutrition 0.000 description 1
- 244000303965 Cyamopsis psoralioides Species 0.000 description 1
- 229920002907 Guar gum Polymers 0.000 description 1
- 229920000084 Gum arabic Polymers 0.000 description 1
- 239000001922 Gum ghatti Substances 0.000 description 1
- 229920000569 Gum karaya Polymers 0.000 description 1
- 235000004298 Tamarindus indica Nutrition 0.000 description 1
- 240000004584 Tamarindus indica Species 0.000 description 1
- 229920001615 Tragacanth Polymers 0.000 description 1
- 235000010489 acacia gum Nutrition 0.000 description 1
- 239000000205 acacia gum Substances 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 150000003973 alkyl amines Chemical group 0.000 description 1
- 235000019270 ammonium chloride Nutrition 0.000 description 1
- 230000000844 anti-bacterial effect Effects 0.000 description 1
- 239000000305 astragalus gummifer gum Substances 0.000 description 1
- 239000003899 bactericide agent Substances 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 229910001570 bauxite Inorganic materials 0.000 description 1
- 239000011324 bead Substances 0.000 description 1
- 125000004181 carboxyalkyl group Chemical group 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
- 229910010293 ceramic material Inorganic materials 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 230000000593 degrading effect Effects 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 238000005553 drilling Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000001747 exhibiting effect Effects 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000000665 guar gum Substances 0.000 description 1
- 235000010417 guar gum Nutrition 0.000 description 1
- 229960002154 guar gum Drugs 0.000 description 1
- 235000019314 gum ghatti Nutrition 0.000 description 1
- 230000036571 hydration Effects 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- 230000002209 hydrophobic effect Effects 0.000 description 1
- 125000002768 hydroxyalkyl group Chemical group 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 229910017053 inorganic salt Inorganic materials 0.000 description 1
- 235000010494 karaya gum Nutrition 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 235000010755 mineral Nutrition 0.000 description 1
- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 238000010979 pH adjustment Methods 0.000 description 1
- 239000012188 paraffin wax Substances 0.000 description 1
- 230000037361 pathway Effects 0.000 description 1
- 239000001103 potassium chloride Substances 0.000 description 1
- 235000011164 potassium chloride Nutrition 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 150000003871 sulfonates Chemical class 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- 239000003180 well treatment fluid Substances 0.000 description 1
- 238000009736 wetting Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/60—Compositions for stimulating production by acting on the underground formation
- C09K8/62—Compositions for forming crevices or fractures
- C09K8/70—Compositions for forming crevices or fractures characterised by their form or by the form of their components, e.g. foams
- C09K8/703—Foams
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/60—Compositions for stimulating production by acting on the underground formation
- C09K8/602—Compositions for stimulating production by acting on the underground formation containing surfactants
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/60—Compositions for stimulating production by acting on the underground formation
- C09K8/84—Compositions based on water or polar solvents
- C09K8/86—Compositions based on water or polar solvents containing organic compounds
- C09K8/88—Compositions based on water or polar solvents containing organic compounds macromolecular compounds
- C09K8/90—Compositions based on water or polar solvents containing organic compounds macromolecular compounds of natural origin, e.g. polysaccharides, cellulose
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/60—Compositions for stimulating production by acting on the underground formation
- C09K8/92—Compositions for stimulating production by acting on the underground formation characterised by their form or by the form of their components, e.g. encapsulated material
- C09K8/94—Foams
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH DRILLING; MINING
- E21B—EARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
- E21B43/25—Methods for stimulating production
- E21B43/26—Methods for stimulating production by forming crevices or fractures
Definitions
- This invention generally relates to method of recycling foamed fracturing fluids used in fracturing subterranean formations in oil and gas wells. More specifically, the invention relates to a self-degrading foaming composition that enhances the recycling of foamed fracturing fluids due to its defoaming character during reclaim of the fluid.
- Natural resources such as gas, oil, minerals, and water residing in a subterranean formation can be recovered by drilling wells into the formation.
- the fluids in the subterranean formation are driven into the wells by, for example, pressure gradients that exist between the formation and the wells, the force of gravity, displacement of the fluids using pumps or the force of another fluid injected into the wells.
- the production of such fluids is commonly increased by hydraulically fracturing the subterranean formations. That is, a viscous fracturing fluid is pumped into a well to a subterranean formation at a rate and a pressure sufficient to form fractures that extend into the formation, providing additional pathways through which the fluids can flow to the wells.
- the fracturing fluid is usually a water-based fluid containing a gelling additive to increase the viscosity of the fluid.
- the gelling additive thus reduces leakage of liquid from the fractures into the subterranean formation and improves proppant suspension capability.
- the gelling additive is commonly a polymeric material that absorbs water and forms a gel as it undergoes hydration.
- one or more foaming surfactants are added to the fracturing fluid.
- a gas is mixed with the fracturing fluid to produce a foamed fracturing fluid, thus ensuring that the pressure exerted by the fracturing fluid on the subterranean formation exceeds the fracture gradient (psi/ft.) to create the fracture.
- the foamed fracturing fluid is injected by foaming the fracturing fluid with nitrogen or carbon dioxide.
- the foaming composition containing one or more surfactants facilitates the foaming and stabilization of the foam produced when the gas is mixed with the fracturing fluid.
- fracturing fluid After a fracturing fluid has been used to form fractures in a subterranean formation, it is usually returned to the surface for disposal or recycle. When fluid is returned, it is desirable to have a fluid that does not foam. Also, it would be desirable to have the ability to recycle the fracturing fluid to form additional fractures in the same subterranean formation or to form fractures in one or more different subterranean formations. Frequently, foamed fracturing fluids are not suitable for recycling. In the recycling operations it is desirable to have a fracturing fluid to be without foam for ease of operation. These recycling operations require addition of defoamer to the fracturing fluids to decrease the foaming and ease of operation.
- the pH of the fracturing fluid may be changed to obtain defoaming during recycling conditions.
- this approach is susceptible to pH fluctuations and if the pH is changed back to the high foaming state, the fracturing fluid will foam again and severely hinder the ease of recycling operation.
- U.S. Patent Application No: 2004/02006616 to Chatterji et al., Oct. 14, 2004, describes cationic tertiary alkyl amine ethoxylates and its mixtures with anionic and amphoteric compounds which can be foamed at pH greater than 9 and defoamed at pH less than 6 or foamed at pH less than 6 and defoamed at pH greater than 9.
- U.S. Patent Application 2003/0207768 to England et. al., Nov. 6, 2003 describes a foaming well treatment fluid comprising an amphoteric surfactant.
- the objective of this patent is to use surfactants that have good wetting characteristics in the presence of coal and be effective foaming agents.
- the recycling of the foamed fracturing fluid is obtained by lowering the pH of the fluid.
- pH variations In addition, adjustment of pH involves additional steps in the recycling operations and usually pH adjustment involves addition of acids that are not desired in terms of environmental acceptability.
- the fracturing fluid does not foam in the fracturing blender or at any stage before it without the change of pH and/or addition of defoamer.
- a foaming composition that foams initially but will be substantially less in foam stability after time is highly desirable for recycling operations.
- a foaming composition that will foam initially and after about 24 hours to have low foam stability is suitable to facilitate processing.
- a foamed fracturing fluid comprised of water, a self-degrading foaming composition comprising one or more surfactant.
- the foamed composition will foam initially but will have reduced foam stability when the fracturing fluid is recovered during flowback.
- foaming composition comprising an anionic surfactant and a nonionic surfactant will foam initially but will not foam after aging compared to the conventional foaming agents used in the recycle operations.
- the foamed fracturing fluid contains a gelling agent. This foamed fracturing fluid does not depend on the change of pH for defoaming during recycling of the fracturing fluid.
- Another object of this invention to introduce a foaming composition in the fracturing fluid, which does not foam in the fracturing blender or any stage before it.
- a further object of the invention to obtain a foaming composition and a foamed fracturing fluid independent on significantly induced pH changes by addition of acids, or buffers for defoaming during reclaim in the recycling step.
- Surfactants in the self-degrading foaming composition in foamed fracturing fluids promote and stabilize the gas-liquid dispersions are soap-like molecules containing a long hydrophobic paraffin chain with a hydrophilic end group.
- Such surfactants include anionic and nonionic compounds.
- Anionic and nonionic surfactants are added in concentrations that range preferably from about 0.05 to about 2 percent of the liquid component volume (from about 0.5 to about 20 gallons per 1000 gallons of liquid); more preferably from about 0.05 to about 1 percent of the liquid component volume.
- Selected anionic surfactants useful in the self-degrading foaming composition of the present invention include dodecylbenzenesulfonates, alpha olefin sulfonates, diphenyloxide disulfonates, alkyl naphthalene sulfonates, sulfosuccinates, sulfosuccinamates, naphthalene-formaldehyde condensates, alkyl sulfoesters and alkyl sulfoamides and mixtures thereof.
- Preferred anionic surfactants are sulfosuccinates and sulfosuccinamates. Most preferred anionic surfactants are sulfosuccinamates such as disodium lauramide monoethanolamine sulfosuccinamate.
- anionic surfactants include those of the following structural formulas:
- R 1 is selected from a group consisting of alkyl, aryl, alkaryl, alkylarylalkyl, arylalkyl, alkylamidoalkyl and alkylaminoalkyl; wherein the alkyl group has about 10 to about 18 carbon atoms; wherein the aryl group represents a phenyl, diphenyl, diphenylether, or naphthalene moiety.
- R 2 is selected from a group consisting of hydrogen, —CH 2 CH 2 OH, alkyl, aryl, alkaryl, alkylarylalkyl, arylalkyl, alkylamidoalkyl and alkylaminoalkyl; wherein the alkyl group has about 10 to about 18 carbon atoms; wherein the aryl group represents a phenyl, diphenyl, diphenylether, or naphthalene moiety.
- p is 0 to about 10, preferably 0 to about 5.
- M is hydrogen, an alkali metal such as sodium or potassium, or an ammonium salt. M is preferably an alkali metal such as sodium or potassium, more preferably sodium.
- Nonionic surfactants include but not limited to fatty acid esters, glycerol esters, ethoxylated fatty acids esters of glycol, ethoxylated fatty acid esters of polyethylene glycol and sorbitan esters.
- Preferred nonionic surfactants are glycerol esters, ethoxylated fatty acids esters of glycol and ethoxylated fatty acid esters of polyethylene glycol. Most preferred are ethoxylated fatty acid esters of polyethylene glycol.
- Selected nonionic surfactants have the structures:
- R 3 is hydrocarbon chain containing about 10 to about 22 carbon atoms and may be branched or straight chained and saturated or unsaturated;
- R 4 hydrogen or a hydrocarbon chain containing about 1 to about 20 carbon atoms and may be branched or straight chained and saturated or unsaturated;
- “p” is from about 1 to about 20, preferably from about 5 to about 20, more preferably from about 5 to about 12.
- the water utilized for forming the foamed fracturing fluid of this invention can be fresh water or salt water.
- salt water is used herein to mean unsaturated salt solutions and saturated salt solutions including brines and seawater.
- water may contain at least one of dissolved organic salts, organic acids, organic acid salts and inorganic salts.
- the gelling agent is added to the water for forming the water into gelled water and increasing the viscosity thereof.
- gelling agents can be used including natural or derivatized polysaccharides which are soluble, dispersible or swellable in an aqueous liquid to yield viscosity to the aqueous liquid.
- polysaccharides which are suitable for use in accordance with the present invention includes galactomannan gums such as gum arabic, gum ghatti, gum karaya, tamarind gum, tragacanth gum, guar gum, locust beam gum and the like.
- Modified gums such as carboxyalkyl derivatives, like carboxymethylguar and hydroxyalkyl derivatives, like hydroxypropylguar can also be employed. Doubly derivatized gums such as carboxymethylhydroxypropylguar can also be used. Mixtures of the galactomannan gums and modified gums can also be used.
- a variety of conventional additives can be included such as gel stabilizers, gel breakers, clay stabilizers, bactericides, fluid loss additives and the like which do not adversely affect the self degrading foaming tendencies of the fracturing fluid.
- Foamed fracturing fluids are superior to conventional liquid fracturing fluids for problematic and water sensitive formations because foams contain less liquid than liquid fracturing fluids and have less tendency to leak. Also, foams have less liquid to retrieve after the fracturing operation is complete. Moreover, the sudden expansion of the gas in the foams when pressure in the well is relieved after the fracturing operation is complete promotes flow of residual fracture fluid liquid back into the well.
- the foamed fracturing fluid can also include a proppant material for preventing formed fractures from closing.
- proppant materials can be utilized including, but not limited to, resin coated or un-coated sand, sintered bauxite, ceramic materials and glass beads. When included, the proppant material is preferably present in the foamed fracturing fluid in an amount in the range of from about 1 to about 10 pounds of proppant material per gallon of the foamed fracturing fluid.
- gases suitable for foaming the fracturing fluid of this invention are air, nitrogen, carbon dioxide and mixtures thereof.
- the gas may be present in the fracturing fluid preferably in an amount in the range of from about 10% to about 95% by volume of liquid, more preferably from about 20% to about 90%, and most preferably from about 20% to about 80% by volume.
- the gas volumetric fraction or “foam quality” of useful foamed fracture fluids is preferably in the range of from about 50 volume percent to about 80 volume percent gas. However, stable foams with foam qualities of up to about 95% can be produced. In general, the viscosity of the foamed fluid increases with increasing quality.
- the foam quality is expressed as a percentage as shown in the equation below:
- U.S. Pat. No. 3,664,422 to Bullen et al. describe fracturing techniques using carbon dioxide as the gas phase.
- an emulsion of liquefied carbon dioxide and water is formed using a surfactant to promote dispersion.
- Proppant is added to the emulsion and the emulsion-proppant slurry is pumped down the wellbore into the formation at a pressure sufficient to fracture the subterranean formation.
- Downhole temperatures are above the critical temperature of carbon dioxide so the liquid carbon dioxide becomes a supercritical fluid as the emulsion approaches the subterranean formation forming a stable foam.
- the foamed fracturing fluid in accordance with the present invention may optionally contain water-soluble inorganic salt, e.g. potassium chloride or ammonium chloride and/or at least one organic acid, water-soluble organic acid salt or organic salt, e.g. trimethyl ammonium chloride. These salts are dissolved in water.
- water-soluble inorganic salt e.g. potassium chloride or ammonium chloride
- organic acid e.g. trimethyl ammonium chloride
- a self-degrading foaming composition is prepared by mixing water with surfactant comprising anionic surfactant, nonionic surfactant, and combinations thereof.
- the foaming composition may contain an organic solvent.
- Preferred organic solvent is isopropyl alcohol. Standard mixing procedures known in the art can be employed since heating of the solution and special agitation conditions are normally not necessary. Of course, if used under conditions of extreme cold such as found in Alaska, normal heating procedures should be employed.
- the initial pH of foamed fracturing composition comprising the self-degrading foaming composition may be lowered or raised to decrease the initial foam quality initially and subsequent aging to reduce foam stability.
- the aging is done up to about 24 hours or longer at room temperature. Further, the aging is done at elevated temperatures preferably from about 80° F. to about 180° F. up to about 24 hours or longer.
- the aging at 140° F. up to 24 hours or longer is most preferred.
- the initial decrease of pH may be by brought about by adding acid and/or buffers. It may be possible to add a base and/or buffers to increase the pH of self-degrading foaming composition.
- Foamed fracturing fluids containing self-degrading foaming compositions were prepared and were found to have reduced foam stability after 24 hours of aging. These foams had good quality initially and half-life was substantially reduced after aging at 140° F. for 24 hours.
- Alkamuls 600 DO is a nonionic surfactant, PEG-12 dioleate supplied by Rhodia, Inc.
- a foamed fracturing fluid with a viscosity of 9-10 cP is prepared by diluting a concentrated hydroxypropyl guar solution in tap water. About 100 ml of the fracturing fluid was added to a Waring blender. The surfactant or surfactant blend was then added and the contents of the blender were mixed slowly. As the mixing speed was slowly increased height of the foam increased due to more air being trapped in the foam. The speed was gradually increased until the foam height remains stable and no further increase in the foam height was observed. The blender was shut off, and its contents were immediately poured into a graduated cylinder and a timer was started. The measured volume of the foam in the graduated cylinder was the foam volume and foam quality was determined by the following equation:
- Foam quality 100 ⁇ (foam volume ⁇ liquid volume)/foam volume
- the foam separated and a clear liquid was collected at the bottom of the cylinder.
- 50% of the original liquid was collected in the bottom of the cylinder (i.e. 50 ml) the time was measured. This time was defined as the half-life.
- the liquid was collected in a bottle and aged in an oven at a set temperature. After a given aging time at the set temperature the bottle was cooled to room temperature and quality and half-life was measured.
- a foamed fracturing fluid of 9-10 cP was prepared as shown in Example 1.
- the foamed fracturing fluid containing the mixture of surfactants compared with the control Gereopon SBL were studied at various pH values.
- the foam height, foam quality and half-life were measured at different pH as well as a function of time and are shown in Table 2.
- the foam quality degraded quickly at higher pH.
Abstract
A method of fracturing a subterranean zone penetrated by a well bore preparing a foamed fracturing fluid containing a self-degrading foaming composition with a mixture of anionic surfactant and nonionic surfactant, and a composition thereof. The fracturing fluid containing self-degrading foaming composition forms a substantially less stable foam when the foamed fracturing fluid is recovered during reclaim.
Description
- This application is a divisional application of U.S. application Ser. No. 11/399,223 filed Apr. 06, 2006.
- 1. Field of the Invention
- This invention generally relates to method of recycling foamed fracturing fluids used in fracturing subterranean formations in oil and gas wells. More specifically, the invention relates to a self-degrading foaming composition that enhances the recycling of foamed fracturing fluids due to its defoaming character during reclaim of the fluid.
- 2. Description of the Related Art
- Natural resources such as gas, oil, minerals, and water residing in a subterranean formation can be recovered by drilling wells into the formation. The fluids in the subterranean formation are driven into the wells by, for example, pressure gradients that exist between the formation and the wells, the force of gravity, displacement of the fluids using pumps or the force of another fluid injected into the wells. The production of such fluids is commonly increased by hydraulically fracturing the subterranean formations. That is, a viscous fracturing fluid is pumped into a well to a subterranean formation at a rate and a pressure sufficient to form fractures that extend into the formation, providing additional pathways through which the fluids can flow to the wells.
- The fracturing fluid is usually a water-based fluid containing a gelling additive to increase the viscosity of the fluid. The gelling additive thus reduces leakage of liquid from the fractures into the subterranean formation and improves proppant suspension capability. The gelling additive is commonly a polymeric material that absorbs water and forms a gel as it undergoes hydration.
- In certain applications one or more foaming surfactants are added to the fracturing fluid. A gas is mixed with the fracturing fluid to produce a foamed fracturing fluid, thus ensuring that the pressure exerted by the fracturing fluid on the subterranean formation exceeds the fracture gradient (psi/ft.) to create the fracture. The foamed fracturing fluid is injected by foaming the fracturing fluid with nitrogen or carbon dioxide. The foaming composition containing one or more surfactants facilitates the foaming and stabilization of the foam produced when the gas is mixed with the fracturing fluid.
- After a fracturing fluid has been used to form fractures in a subterranean formation, it is usually returned to the surface for disposal or recycle. When fluid is returned, it is desirable to have a fluid that does not foam. Also, it would be desirable to have the ability to recycle the fracturing fluid to form additional fractures in the same subterranean formation or to form fractures in one or more different subterranean formations. Frequently, foamed fracturing fluids are not suitable for recycling. In the recycling operations it is desirable to have a fracturing fluid to be without foam for ease of operation. These recycling operations require addition of defoamer to the fracturing fluids to decrease the foaming and ease of operation.
- Alternatively, the pH of the fracturing fluid may be changed to obtain defoaming during recycling conditions. However, this approach is susceptible to pH fluctuations and if the pH is changed back to the high foaming state, the fracturing fluid will foam again and severely hinder the ease of recycling operation. U.S. Patent Application No: 2004/02006616 to Chatterji et al., Oct. 14, 2004, describes cationic tertiary alkyl amine ethoxylates and its mixtures with anionic and amphoteric compounds which can be foamed at pH greater than 9 and defoamed at pH less than 6 or foamed at pH less than 6 and defoamed at pH greater than 9.
- U.S. Patent Application 2003/0207768 to England et. al., Nov. 6, 2003, describes a foaming well treatment fluid comprising an amphoteric surfactant. The objective of this patent is to use surfactants that have good wetting characteristics in the presence of coal and be effective foaming agents. Also the recycling of the foamed fracturing fluid is obtained by lowering the pH of the fluid. However such systems are susceptible to pH variations. In addition, adjustment of pH involves additional steps in the recycling operations and usually pH adjustment involves addition of acids that are not desired in terms of environmental acceptability.
- It is desirable that the fracturing fluid does not foam in the fracturing blender or at any stage before it without the change of pH and/or addition of defoamer. Further, a foaming composition that foams initially but will be substantially less in foam stability after time is highly desirable for recycling operations. Typically a foaming composition that will foam initially and after about 24 hours to have low foam stability is suitable to facilitate processing.
- Accordingly, there is provided a foamed fracturing fluid comprised of water, a self-degrading foaming composition comprising one or more surfactant. The foamed composition will foam initially but will have reduced foam stability when the fracturing fluid is recovered during flowback.
- It is an object of the present invention to provide a method of fracturing a subterranean zone penetrated by a well bore comprising:
- (a) preparing a foamed fracturing fluid comprised of water, a self-degrading foaming composition comprising a mixture of anionic surfactant and nonionic surfactant, and sufficient gas to form a foam when fracturing fluid is injected; and
- (b) contacting said subterranean zone with said foamed fracturing fluid under conditions effective to create at least one fracture therein,
- wherein the self-degrading foaming composition forms a substantially less stable foam when the fracturing fluid is recovered during recycling.
- It has been unexpectedly found that the use of foaming composition comprising an anionic surfactant and a nonionic surfactant will foam initially but will not foam after aging compared to the conventional foaming agents used in the recycle operations. The foamed fracturing fluid contains a gelling agent. This foamed fracturing fluid does not depend on the change of pH for defoaming during recycling of the fracturing fluid.
- Another object of this invention to introduce a foaming composition in the fracturing fluid, which does not foam in the fracturing blender or any stage before it.
- It is still another object of the invention to have a foamed fracturing fluid where the addition of a defoamer is not required to decrease the foam during the recycle operations.
- A further object of the invention to obtain a foaming composition and a foamed fracturing fluid independent on significantly induced pH changes by addition of acids, or buffers for defoaming during reclaim in the recycling step.
- It is still another object of the present invention to have a fracturing fluid to be formulated with a relatively low level of surfactant for cost-effective performance.
- Surfactants in the self-degrading foaming composition in foamed fracturing fluids promote and stabilize the gas-liquid dispersions are soap-like molecules containing a long hydrophobic paraffin chain with a hydrophilic end group. Such surfactants include anionic and nonionic compounds. Anionic and nonionic surfactants are added in concentrations that range preferably from about 0.05 to about 2 percent of the liquid component volume (from about 0.5 to about 20 gallons per 1000 gallons of liquid); more preferably from about 0.05 to about 1 percent of the liquid component volume.
- Selected anionic surfactants useful in the self-degrading foaming composition of the present invention include dodecylbenzenesulfonates, alpha olefin sulfonates, diphenyloxide disulfonates, alkyl naphthalene sulfonates, sulfosuccinates, sulfosuccinamates, naphthalene-formaldehyde condensates, alkyl sulfoesters and alkyl sulfoamides and mixtures thereof. Preferred anionic surfactants are sulfosuccinates and sulfosuccinamates. Most preferred anionic surfactants are sulfosuccinamates such as disodium lauramide monoethanolamine sulfosuccinamate.
- Representative anionic surfactants include those of the following structural formulas:
- and combinations thereof.
- R1 is selected from a group consisting of alkyl, aryl, alkaryl, alkylarylalkyl, arylalkyl, alkylamidoalkyl and alkylaminoalkyl; wherein the alkyl group has about 10 to about 18 carbon atoms; wherein the aryl group represents a phenyl, diphenyl, diphenylether, or naphthalene moiety.
- R2 is selected from a group consisting of hydrogen, —CH2CH2OH, alkyl, aryl, alkaryl, alkylarylalkyl, arylalkyl, alkylamidoalkyl and alkylaminoalkyl; wherein the alkyl group has about 10 to about 18 carbon atoms; wherein the aryl group represents a phenyl, diphenyl, diphenylether, or naphthalene moiety.
- “p” is 0 to about 10, preferably 0 to about 5.
- M is hydrogen, an alkali metal such as sodium or potassium, or an ammonium salt. M is preferably an alkali metal such as sodium or potassium, more preferably sodium.
- Nonionic surfactants include but not limited to fatty acid esters, glycerol esters, ethoxylated fatty acids esters of glycol, ethoxylated fatty acid esters of polyethylene glycol and sorbitan esters. Preferred nonionic surfactants are glycerol esters, ethoxylated fatty acids esters of glycol and ethoxylated fatty acid esters of polyethylene glycol. Most preferred are ethoxylated fatty acid esters of polyethylene glycol.
- Selected nonionic surfactants have the structures:
-
R3C(O)O—(CH2CH2O)p—R4 -
R3C(O)OCH2CH(OH)CH2O—R4 - and combinations thereof.
- R3 is hydrocarbon chain containing about 10 to about 22 carbon atoms and may be branched or straight chained and saturated or unsaturated; R4 hydrogen or a hydrocarbon chain containing about 1 to about 20 carbon atoms and may be branched or straight chained and saturated or unsaturated; “p” is from about 1 to about 20, preferably from about 5 to about 20, more preferably from about 5 to about 12.
- The water utilized for forming the foamed fracturing fluid of this invention can be fresh water or salt water. The term “salt water” is used herein to mean unsaturated salt solutions and saturated salt solutions including brines and seawater. In addition water may contain at least one of dissolved organic salts, organic acids, organic acid salts and inorganic salts.
- The gelling agent is added to the water for forming the water into gelled water and increasing the viscosity thereof. A variety of gelling agents can be used including natural or derivatized polysaccharides which are soluble, dispersible or swellable in an aqueous liquid to yield viscosity to the aqueous liquid. One group, for example, of polysaccharides which are suitable for use in accordance with the present invention includes galactomannan gums such as gum arabic, gum ghatti, gum karaya, tamarind gum, tragacanth gum, guar gum, locust beam gum and the like. Modified gums such as carboxyalkyl derivatives, like carboxymethylguar and hydroxyalkyl derivatives, like hydroxypropylguar can also be employed. Doubly derivatized gums such as carboxymethylhydroxypropylguar can also be used. Mixtures of the galactomannan gums and modified gums can also be used. Optionally a variety of conventional additives can be included such as gel stabilizers, gel breakers, clay stabilizers, bactericides, fluid loss additives and the like which do not adversely affect the self degrading foaming tendencies of the fracturing fluid.
- Foamed fracturing fluids are superior to conventional liquid fracturing fluids for problematic and water sensitive formations because foams contain less liquid than liquid fracturing fluids and have less tendency to leak. Also, foams have less liquid to retrieve after the fracturing operation is complete. Moreover, the sudden expansion of the gas in the foams when pressure in the well is relieved after the fracturing operation is complete promotes flow of residual fracture fluid liquid back into the well. The foamed fracturing fluid can also include a proppant material for preventing formed fractures from closing. A variety of proppant materials can be utilized including, but not limited to, resin coated or un-coated sand, sintered bauxite, ceramic materials and glass beads. When included, the proppant material is preferably present in the foamed fracturing fluid in an amount in the range of from about 1 to about 10 pounds of proppant material per gallon of the foamed fracturing fluid.
- Examples of gases suitable for foaming the fracturing fluid of this invention are air, nitrogen, carbon dioxide and mixtures thereof. The gas may be present in the fracturing fluid preferably in an amount in the range of from about 10% to about 95% by volume of liquid, more preferably from about 20% to about 90%, and most preferably from about 20% to about 80% by volume.
- The gas volumetric fraction or “foam quality” of useful foamed fracture fluids is preferably in the range of from about 50 volume percent to about 80 volume percent gas. However, stable foams with foam qualities of up to about 95% can be produced. In general, the viscosity of the foamed fluid increases with increasing quality.
- The foam quality is expressed as a percentage as shown in the equation below:
-
[foam volume (ml)−liquid volume (ml)]×[100]/foam volume (ml) - Procedures for making and using foamed fracturing fluids are described in U.S. Pat. No. 3,937,283 to Blauer et al and U.S. Pat. No. 3,980,136 to Plummer et al. Briefly, these patents teach how to produce stable foam fracturing fluids using nitrogen, water, a surfactant and a sand proppant. The foam quality ranges between 53% to 99%. The foam is pumped down the well and into the formation at a pressure sufficient to fracture the formation. When the fracturing operation is complete, the pressure on the well is relieved at the wellhead. The foam is carried back into the well by the rush of expanding gas when pressure on the foam is reduced.
- U.S. Pat. No. 3,664,422 to Bullen et al., describe fracturing techniques using carbon dioxide as the gas phase. First, an emulsion of liquefied carbon dioxide and water is formed using a surfactant to promote dispersion. Proppant is added to the emulsion and the emulsion-proppant slurry is pumped down the wellbore into the formation at a pressure sufficient to fracture the subterranean formation. Downhole temperatures are above the critical temperature of carbon dioxide so the liquid carbon dioxide becomes a supercritical fluid as the emulsion approaches the subterranean formation forming a stable foam.
- The foamed fracturing fluid in accordance with the present invention may optionally contain water-soluble inorganic salt, e.g. potassium chloride or ammonium chloride and/or at least one organic acid, water-soluble organic acid salt or organic salt, e.g. trimethyl ammonium chloride. These salts are dissolved in water.
- In an embodiment of the invention a self-degrading foaming composition is prepared by mixing water with surfactant comprising anionic surfactant, nonionic surfactant, and combinations thereof. The foaming composition may contain an organic solvent. Preferred organic solvent is isopropyl alcohol. Standard mixing procedures known in the art can be employed since heating of the solution and special agitation conditions are normally not necessary. Of course, if used under conditions of extreme cold such as found in Alaska, normal heating procedures should be employed.
- In another embodiment of the invention the initial pH of foamed fracturing composition comprising the self-degrading foaming composition may be lowered or raised to decrease the initial foam quality initially and subsequent aging to reduce foam stability. Alternatively it may be possible to raise the pH. The aging is done up to about 24 hours or longer at room temperature. Further, the aging is done at elevated temperatures preferably from about 80° F. to about 180° F. up to about 24 hours or longer.
- The aging at 140° F. up to 24 hours or longer is most preferred. The initial decrease of pH may be by brought about by adding acid and/or buffers. It may be possible to add a base and/or buffers to increase the pH of self-degrading foaming composition.
- The following examples are presented to illustrate the preparation and properties of foamed fracturing fluids containing self-degrading foaming compositions and should not be construed to limit the scope of the invention, unless otherwise expressly indicated in the appended claims.
- Foamed fracturing fluids containing self-degrading foaming compositions were prepared and were found to have reduced foam stability after 24 hours of aging. These foams had good quality initially and half-life was substantially reduced after aging at 140° F. for 24 hours.
-
-
- Gerepon SBL-203 is an anionic surfactant, disodium lauramide monoethanolamine sulfosuccinamate, supplied by Rhodia, Inc.
- Alkamuls 600 DO is a nonionic surfactant, PEG-12 dioleate supplied by Rhodia, Inc.
- A foamed fracturing fluid with a viscosity of 9-10 cP is prepared by diluting a concentrated hydroxypropyl guar solution in tap water. About 100 ml of the fracturing fluid was added to a Waring blender. The surfactant or surfactant blend was then added and the contents of the blender were mixed slowly. As the mixing speed was slowly increased height of the foam increased due to more air being trapped in the foam. The speed was gradually increased until the foam height remains stable and no further increase in the foam height was observed. The blender was shut off, and its contents were immediately poured into a graduated cylinder and a timer was started. The measured volume of the foam in the graduated cylinder was the foam volume and foam quality was determined by the following equation:
-
Foam quality=100×(foam volume−liquid volume)/foam volume - As time progressed, the foam separated and a clear liquid was collected at the bottom of the cylinder. After 50% of the original liquid was collected in the bottom of the cylinder (i.e. 50 ml) the time was measured. This time was defined as the half-life. After measuring the half-life, the liquid was collected in a bottle and aged in an oven at a set temperature. After a given aging time at the set temperature the bottle was cooled to room temperature and quality and half-life was measured.
- The foam volume and time required to reach the half-life (50ml) was measured, exhibiting the recyclable nature of the foamed fracturing. The foam testing results are shown in Table 1.
-
TABLE 1 Foam Testing Results Foam Volume Foam (ml) @ Half Life Quality Sample ID Description Testing Conditions 75 F. (min:sec) (%) Geropon SBL-203 only R0476-70-5 0.5 ml Geropon initial 340 31:00 70.6 SBL-203 24 hrs @ 140 F. 180 9:45 44.4 R0476-70-18 0.2 ml Geropon initial 305 29:45 67.2 SBL-203 24 hrs @ 140 F. 185 5:45 48.6 Geropon SBL- 203 with Alkamuls 600DO R0476-70-9 0.2 ml Geropon initial 275 24:15 63.6 SBL-203 + 0.05 ml Alkamuls 600 DO 24 hrs @ 140 F. 135 1:30 26.0 R0476-70-10 0.2 ml Geropon initial 195 7:05 48.7 SBL-203 + 0.1 ml Alkamuls 600 DO 24 hrs @ 140 F. 125 very 20.0 fast~5 sec - A foamed fracturing fluid of 9-10 cP was prepared as shown in Example 1. The foamed fracturing fluid containing the mixture of surfactants compared with the control Gereopon SBL were studied at various pH values. The foam height, foam quality and half-life were measured at different pH as well as a function of time and are shown in Table 2. The foam quality degraded quickly at higher pH.
-
TABLE 2 Effect of Initial pH on the Foam Quality and Aging Foam Final T Volume ½ pH Solution Weight Time (deg (ml) Life Quality after Designation Surfactant pH (g) (hr) F.) @ 75 F. (min) (%) 24 hr's R0476-175-6 Geropon 11.8 100 0 RT 290 34.0 65.5 10.6 SBL-203 89 2 140 145 3.3 38.6 (Control) 82 6 130 2.5 36.9 76 24 120 2.3 36.7 R0476-175-7 R0476-85-11 11.8 100 0 RT 265 19.5 62.3 11.0 93 2 140 120 0.0 22.5 — 6 88 24 125 0.0 29.6 R0476-175-8 R0476-85-11 11.8 100 0 RT 260 16.5 61.5 11.3 98 2 135 0.5 27.4 — 6 91 24 115 0.0 20.9 R0476-175-10 Geropon 10.1 100 0 RT 295 35.0 66.1 9.1 SBL-203 89 2 140 270 32.0 67.0 (Control) 82 6 215 23.0 61.9 75 24 180 17.0 58.3 R0476-175-11 R0476-85-11 10.1 100 0 RT 275 18.0 63.6 9.1 94 2 140 235 14.0 60.0 86 6 175 8.0 50.8 80 24 125 1.5 36.0 R0476-85-11: Formulated by blending 66.67% Geropon SBL-203 + 16.67% Alkamuls 600DO + 8.33% isopropanol + 8.33% Deionized water. - The invention has been described in the more limited aspects of preferred embodiments hereof, including numerous examples. Other embodiments have been suggested and still others may occur to those skilled in the art upon a reading and understanding of the specification. It is intended that all such embodiments be included within the scope of this invention.
Claims (8)
1. A self-degrading foaming composition comprising a mixture of anionic surfactants selected from the group consisting of dodecylbenzenesulfonate, alpha olefin sulfonate, diphenyloxide disulfonate, alkyl naphthalene sulfonate, sulfosuccinate, sulfosuccinamate, naphthalene-formaldehyde condensate, alkyl sulfoester, alkyl sulfoamide, and mixtures thereof; and
a nonionic surfactant selected from the group consisting of fatty acid esters, glycerol esters, ethoxylated fatty acids esters of glycol, ethoxylated fatty acid esters of polyethylene glycol and sorbitan esters;
wherein the self-degrading composition has a substantially reduced foam stability after aging.
2. The composition of claim 1 wherein the anionic surfactant is selected from the group consisting of formula (I), (II), (III), or (IV):
and combinations thereof;
wherein R1 is selected from a group consisting of alkyl, aryl, alkaryl, alkylarylalkyl, arylalkyl, alkylamidoalkyl and alkylaminoalkyl, and
wherein the alkyl group has about 10 to about 18 carbon atoms, the aryl group represents a phenyl, diphenyl, diphenylether, or naphthalene moiety;
R2 is selected from a group consisting of hydrogen, —CH2CH2OH, alkyl, aryl, alkaryl, alkylarylalkyl, arylalkyl, alkylamidoalkyl and alkylaminoalkyl, wherein the alkyl group has about 10 to about 18 carbon atoms, wherein the aryl group represents a phenyl, diphenyl, diphenylether, or naphthalene moiety; and
“p” is 0 to about 10, and M represents hydrogen, an alkali metal such as sodium or potassium, or an ammonium salt.
3. The composition of claim 1 wherein said fracturing fluid comprises a crosslinker.
4. The composition of claim 3 wherein said crosslinker is a boron containing compound.
5. The composition of claim 3 wherein said crosslinker is selected from the group consisting of boric acid, borax, boron containing ores, colemanite, and ulexite.
6. The composition of claim 1 wherein said crosslinker is a zirconium or titanium based metallic crosslinker.
7. The composition of claim 1 further comprising cationic surfactants, zwitterionic surfactants, amphoteric surfactants, or mixtures thereof.
8. A foamed fracturing composition comprising:
(a) a self-degrading foaming composition having substantially reduced foam stability after aging, said self-degrading foaming comprising a mixture of anionic surfactants wherein at least one of said anionic surfactants has the general formula:
wherein R1 is selected from a group consisting of alkyl, aryl, alkaryl, alkylarylalkyl, arylalkyl, alkylamidoalkyl and alkylaminoalkyl, and wherein the alkyl group has about 10 to about 18 carbon atoms, the aryl group represents a phenyl, diphenyl, diphenylether, or naphthalene moiety;
R2 is selected from a group consisting of hydrogen, —CH2CH2OH, alkyl, aryl, alkaryl, alkylarylalkyl, arylalkyl, alkylamidoalkyl and alkylaminoalkyl, wherein the alkyl group has about 10 to about 18 carbon atoms, wherein the aryl group represents a phenyl, diphenyl, diphenylether, or naphthalene moiety; and at least one nonionic surfactant having the general formula:
R3C(O)O—(CH2CH2O)pR4
R3C(O)O—(CH2CH2O)pR4
wherein, R3 is hydrocarbon chain containing about 10 to about 22 carbon atoms, R4 is a hydrogen or a hydrocarbon chain containing about 1 to about 20 carbon atoms; and “p” is from about 1 to about 20
(b) an aqueous solution;
(c) a gelling agent; and
(d) a gas.
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US11/399,223 Expired - Fee Related US7404442B2 (en) | 2005-04-06 | 2006-04-06 | Method of recycling fracturing fluids using a self-degrading foaming composition |
Country Status (5)
Country | Link |
---|---|
US (2) | US7404442B2 (en) |
EP (1) | EP1866519B1 (en) |
CA (2) | CA2826313C (en) |
DK (1) | DK1866519T3 (en) |
WO (1) | WO2006108161A2 (en) |
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Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3937283A (en) * | 1974-10-17 | 1976-02-10 | The Dow Chemical Company | Formation fracturing with stable foam |
US3962150A (en) * | 1974-04-10 | 1976-06-08 | Richardson-Merrell Inc. | Foam producing cleansing compositions |
US3980136A (en) * | 1974-04-05 | 1976-09-14 | Big Three Industries, Inc. | Fracturing well formations using foam |
US5310002A (en) * | 1992-04-17 | 1994-05-10 | Halliburton Company | Gas well treatment compositions and methods |
US5566760A (en) * | 1994-09-02 | 1996-10-22 | Halliburton Company | Method of using a foamed fracturing fluid |
US6148932A (en) * | 1997-04-03 | 2000-11-21 | Institut Francias Du Petrole | Drilling method and system using foam--foaming composition |
US7077219B1 (en) * | 2005-02-18 | 2006-07-18 | Halliburton Energy Services, Inc. | Foamed treatment fluids and associated methods |
Family Cites Families (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3664422A (en) * | 1970-08-17 | 1972-05-23 | Dresser Ind | Well fracturing method employing a liquified gas and propping agents entrained in a fluid |
US4453596A (en) * | 1983-02-14 | 1984-06-12 | Halliburton Company | Method of treating subterranean formations utilizing foamed viscous fluids |
US4627495A (en) * | 1985-04-04 | 1986-12-09 | Halliburton Company | Method for stimulation of wells with carbon dioxide or nitrogen based fluids containing high proppant concentrations |
WO1992014907A1 (en) * | 1991-02-22 | 1992-09-03 | The Western Company Of North America | Slurried polymer foam system and method for the use thereof |
US5480586A (en) * | 1991-04-15 | 1996-01-02 | Colgate-Palmolive Co. | Light duty liquid detergent compostion comprising a sulfosuccinamate-containing surfactant blend |
US5558855A (en) * | 1993-01-25 | 1996-09-24 | Sonus Pharmaceuticals | Phase shift colloids as ultrasound contrast agents |
US6148917A (en) * | 1998-07-24 | 2000-11-21 | Actisystems, Inc. | Method of releasing stuck pipe or tools and spotting fluids therefor |
EP1203068B1 (en) * | 1999-07-17 | 2008-09-03 | Huntsman International Llc | Structured surfactant systems |
CA2401150C (en) | 2000-02-25 | 2009-08-11 | Schlumberger Canada Limited | Foaming agents for use in coal seam reservoirs |
DE10237378A1 (en) * | 2002-08-12 | 2004-03-11 | Basf Ag | Crosslinked cationic copolymers with regulators and their use in hair cosmetic preparations |
US6986392B2 (en) | 2003-03-25 | 2006-01-17 | Halliburton Energy Services, Inc. | Recyclable foamed fracturing fluids and methods of using the same |
-
2006
- 2006-04-06 DK DK06749598.6T patent/DK1866519T3/en active
- 2006-04-06 CA CA2826313A patent/CA2826313C/en not_active Expired - Fee Related
- 2006-04-06 CA CA2603960A patent/CA2603960C/en not_active Expired - Fee Related
- 2006-04-06 EP EP06749598A patent/EP1866519B1/en not_active Not-in-force
- 2006-04-06 US US11/399,223 patent/US7404442B2/en not_active Expired - Fee Related
- 2006-04-06 WO PCT/US2006/013204 patent/WO2006108161A2/en active Application Filing
-
2008
- 2008-04-21 US US12/148,638 patent/US20080200351A1/en not_active Abandoned
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3980136A (en) * | 1974-04-05 | 1976-09-14 | Big Three Industries, Inc. | Fracturing well formations using foam |
US3962150A (en) * | 1974-04-10 | 1976-06-08 | Richardson-Merrell Inc. | Foam producing cleansing compositions |
US3937283A (en) * | 1974-10-17 | 1976-02-10 | The Dow Chemical Company | Formation fracturing with stable foam |
US5310002A (en) * | 1992-04-17 | 1994-05-10 | Halliburton Company | Gas well treatment compositions and methods |
US5566760A (en) * | 1994-09-02 | 1996-10-22 | Halliburton Company | Method of using a foamed fracturing fluid |
US6148932A (en) * | 1997-04-03 | 2000-11-21 | Institut Francias Du Petrole | Drilling method and system using foam--foaming composition |
US7077219B1 (en) * | 2005-02-18 | 2006-07-18 | Halliburton Energy Services, Inc. | Foamed treatment fluids and associated methods |
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AU2010298509B2 (en) * | 2009-09-23 | 2014-06-12 | Nalco Company | Foamers for downhole injection |
US20110071059A1 (en) * | 2009-09-23 | 2011-03-24 | Nguyen Duy T | Foamers for downhole injection |
WO2011037849A3 (en) * | 2009-09-23 | 2011-08-18 | Nalco Company | Foamers for downhole injection |
US20110071060A1 (en) * | 2009-09-23 | 2011-03-24 | Nguyen Duy T | Foamers for downhole injection |
US9631133B2 (en) | 2009-09-23 | 2017-04-25 | Nalco Company | Foamers for downhole injection |
US8399386B2 (en) | 2009-09-23 | 2013-03-19 | Nalco Company | Foamers for downhole injection |
US20120125620A1 (en) * | 2010-11-19 | 2012-05-24 | Nguyen Duy T | Foamers for downhole injection |
US8950494B2 (en) * | 2010-11-19 | 2015-02-10 | Nalco Company | Foamers for downhole injection |
US8746341B2 (en) | 2011-05-06 | 2014-06-10 | Nalco Company | Quaternary foamers for downhole injection |
WO2013028254A1 (en) * | 2011-08-24 | 2013-02-28 | Baker Hughes Incorporated | Method of using fracturing fluids containing carboxyalkyl tamarind |
US10655054B2 (en) | 2015-06-01 | 2020-05-19 | Cytec Industries Inc. | Foam-forming surfactant compositions |
US10245560B2 (en) | 2015-11-06 | 2019-04-02 | Dow Global Technologies Llc | Filtration and reuse of surfactant-containing produced water for oil recovery |
CN112832728A (en) * | 2021-01-08 | 2021-05-25 | 中国矿业大学 | Shale reservoir fracturing method based on methane multistage combustion and explosion |
Also Published As
Publication number | Publication date |
---|---|
DK1866519T3 (en) | 2012-08-27 |
WO2006108161A3 (en) | 2007-11-15 |
CA2603960C (en) | 2013-11-19 |
CA2826313C (en) | 2016-05-17 |
CA2826313A1 (en) | 2006-10-12 |
US7404442B2 (en) | 2008-07-29 |
EP1866519A4 (en) | 2009-11-18 |
EP1866519A2 (en) | 2007-12-19 |
WO2006108161A2 (en) | 2006-10-12 |
CA2603960A1 (en) | 2006-10-12 |
US20060260815A1 (en) | 2006-11-23 |
EP1866519B1 (en) | 2012-08-08 |
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