WO2008083063A2 - Aqueous fluid and method of making and using the same - Google Patents
Aqueous fluid and method of making and using the same Download PDFInfo
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- WO2008083063A2 WO2008083063A2 PCT/US2007/088511 US2007088511W WO2008083063A2 WO 2008083063 A2 WO2008083063 A2 WO 2008083063A2 US 2007088511 W US2007088511 W US 2007088511W WO 2008083063 A2 WO2008083063 A2 WO 2008083063A2
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- aqueous fluid
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- 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
- C09K8/02—Well-drilling compositions
- C09K8/04—Aqueous well-drilling compositions
- C09K8/06—Clay-free compositions
- C09K8/08—Clay-free compositions containing natural organic compounds, e.g. polysaccharides, or derivatives thereof
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- 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
- C09K8/02—Well-drilling compositions
- C09K8/38—Gaseous or foamed well-drilling compositions
Definitions
- a drilling fluid is typically circulated downwardly through a drill string to cool and lubricate the drill string, suspend the cuttings removed from the well bore, and to keep out formation fluids.
- Both aqueous and oil-based drilling fluid systems are known.
- the more economical aqueous systems are used when practicable with oil-based systems being used where increased lubricity at the drilling head is desirable or when traversing formations which would be adversely affected by a water-based system, such as water soluble shale formations.
- Aqueous drilling fluids typically comprise a viscosifying agent, generally a clay (e.g., a solid phase bentonite, attapulgite, or sepiolite), and a water fluid vehicle.
- a viscosifying agent generally a clay (e.g., a solid phase bentonite, attapulgite, or sepiolite)
- salt or salt water can be added to the components of the drilling fluid to prepare a salt water drilling fluid.
- additives are also commonly employed to control viscosity, yield point, gel strength (thixotropic properties), pH, fluid loss, tolerance to contaminants (e.g., salt and calcium carbonate), lubricating properties, filter caking properties, cooling and heat transfer properties, and tolerance to inactive solids such as sand and silt or active native mud making clays (e.g., smectites, illites, kaolinites, chlorites, etc.).
- Clays are not usually used as the sole viscosifying agent, and typically organic water-soluble polymers (e.g., starch, carboxymethylcellulose, natural gums, or synthetic resins) are used in conjunction with clays.
- aqueous drilling fluids e.g., those comprising polysaccharides and dissolved salt (e.g., dissolved NaCl and CaCl 2 )
- certain glass bubbles e.g., soda-lime-borosilicate glasses such as those marketed by 3M Company, St. Paul, MN, under the trade designation "HGS 18000"
- HGS 18000 soda-lime-borosilicate glasses
- aqueous drilling fluids e.g., those comprising polysaccharide and dissolved salt (e.g., dissolved NaCl and CaCl 2 )
- glass bubbles e.g., those marketed by 3M Company under the trade designation "HGS 18000”
- the borate anion, or at least a source thereof is present, for example, on the outer surface and/or in the ceramic of some ceramic bubbles (e.g., those marketed by 3M Company under the trade designation "HGS 18000").
- Fluids described herein are useful as drilling fluids.
- the method comprises circulating an aqueous drilling fluid according to the present invention in a wellbore penetrating a subterranean zone.
- the present invention provides a method of making a low density fluid.
- the method comprises combining (a) an aqueous fluid comprising polysaccharide and dissolved salt, (b) borate anions comprising at least one boron atom and at least two oxygen atoms, (c) ceramic (i.e., any of glass, crystalline ceramics, glass- ceramics, and combinations thereof) bubbles (also referred to as "hollow ceramic microspheres"), and (d) organic material that preferentially reacts with the borate anions as compared to the polysaccharide, to provide the low density fluid, wherein in the absence of the organic material, the low density fluid gels within 16 hours, at 20 0 C (i.e., in the absence of the organic material the modified fluid gels, and the amount of organic material is sufficient to prevent the modified fluid from gelling within 16 hours, at 20 0 C).
- the low density fluid remains a fluid for at least 2, 3, 4, 5, 6, 7, 8, 9, or even 10 days.
- the present invention provides a method of making a modified aqueous fluid (e.g., a drilling fluid).
- the method comprises combining an aqueous fluid comprising (a) polysaccharide and dissolved salt (e.g., dissolved NaCl and CaCl 2 ), (c) borate anions comprising at least one boron atom and at least two oxygen atoms, and (d) organic material that preferentially reacts with the borate anions as compared to the polysaccharide, to provide a modified aqueous fluid (e.g., a modified drilling fluid), wherein in the absence of the organic material the modified aqueous fluid gels within 16 hours, at 20 0 C.
- the aqueous fluid remains a fluid for at least 2, 3, 4, 5, 6, 7, 8, 9, or even 10 days.
- the aqueous fluid further comprises ceramic bubbles.
- the aqueous fluid further comprises gas bubbles (i.e., the aqueous fluid is foamed).
- the present invention provides an aqueous fluid (e.g., a drilling fluid) comprising the reaction product of at least borate anions comprising at least one boron atom and at least two oxygen atoms and organic material that preferentially reacts with the borate anions as compared to polysaccharide present in the fluid.
- aqueous fluid e.g., a drilling fluid
- the aqueous composition in the absence of the organic material that formed the reaction product, the aqueous composition would gel within 16 hours, at 20 0 C, and wherein the amount of organic material forming the reaction product was sufficient to prevent the aqueous composition from gelling.
- the aqueous fluid remains a fluid for at least 2, 3, 4,
- the aqueous fluid further comprises dissolved salt.
- the aqueous fluid further comprises ceramic bubbles.
- the aqueous fluid further comprises gas bubbles (i.e., the aqueous fluid is foamed).
- the method comprises circulating an aqueous drilling fluid comprising the reaction product of at least borate anions comprising at least one boron atom and at least two oxygen atoms and organic material that preferentially reacts with the borate anions as compared to polysaccharide present in the fluid, in a wellbore penetrating a subterranean zone.
- the aqueous drilling fluid further comprises ceramic bubbles.
- the aqueous fluid further comprises gas bubbles (i.e., the aqueous fluid is foamed).
- Examples of the organic material referred to above with respect to the invention which may prevent, or at least inhibit, gelling in certain concentrations, include monosaccharides (including aldoses (e.g., glucose, mannose, or xylose) and ketoses (e.g., fructose)); sugar alcohols (e.g., sorbitol or maltitol); disaccharides (e.g., maltose); amino sugars (e.g., glucosamine); sugar acids (i.e., aldonic acids (e.g., gluconic acid)); compounds (including linear and branched) containing at least three functional groups selected from the group consisting of hydroxyl functional groups, carboxylic acid functional groups, and combinations thereof (e.g., erythorbic acid, phloroglucinol, glycerol, meso-erythritol, pentaerythritol, citric acid, l,l,l-tris
- organic material includes these compounds in any of their stereoisomeric (e.g., enantiomeric or diasteromeric), solvated (e.g., hydrated), and/or salt (e.g., in the case of amino sugars, sugar acids, or other carboxylic acids) forms.
- stereoisomeric e.g., enantiomeric or diasteromeric
- solvated e.g., hydrated
- salt e.g., in the case of amino sugars, sugar acids, or other carboxylic acids
- the present invention provides a method of making a low density fluid.
- the method comprises combining (a) an aqueous fluid comprising polysaccharide and dissolved salt, (b) soda-lime-borosilicate glass bubbles, and (c) at least one of monosaccharides; sugar alcohols; disaccharides; amino sugars; sugar acids; compounds containing at least three functional groups selected from the group consisting of hydroxyl functional groups, carboxylic acid functional groups, and combinations thereof; 1 ,6-hexanediol; phthalic acid; or hydantoin, to provide a low density aqueous fluid, wherein in the absence of the at least one of monosaccharides; sugar alcohols; disaccharides; amino sugars; sugar acids; compounds containing at least three functional groups selected from the group consisting of hydroxyl functional groups, carboxylic acid functional groups, and combinations thereof; 1,6-hexanediol; phthalic acid; or hydan
- Aqueous fluids comprising polysaccharide useful for the present invention are known in the art, and are available commercially, for example, from Baker Hughes, Houston, TX; M-I LLC, Houston, TX; and Haliburton, Houston, TX.
- Exemplary polysaccharides present in the aqueous fluids include at least one of xanthan gum, guar gum, starch, or cellulose (e.g., polyanioninc cellulose).
- Exemplary dissolved salts which may be present in the fluids include NaCl and CaCl 2 .
- the aqueous fluids include a viscosifying component in an amount sufficient to increase the viscosity of the composition.
- exemplary viscosifying components include bentonite, asbestos, sepiolite, attapulgite, cellulose derivatives, and combinations thereof.
- the borate anions include monoborate and polyborate anions and anions comprising at least 2, 3, 4, 5, or even at least 6 boron atoms, which may be trivalent or tetravalent, and at least 3, 4, 5, 6, 7, 8, 9 or even at least 10 oxygen atoms.
- Exemplary sources of borate anions comprising at least one boron atom and at least two oxygen atoms include boric acid, borax (i.e., sodium tetraborate decahydrate), other boric acid salts (including solvated or hydrated forms), and soda-lime -borosilicate glass bubbles.
- Exemplary borate counter-ions include alkali metal cations, alkaline earth metal cations, and combinations thereof.
- Exemplary organic materials that preferentially react with the borate anions as compared to the polysaccharide include at least one of sorbitol (e.g., D-sorbitol), D- (+)glucosamine hydrochloride, hydantoin, erythorbic acid, phloroglucinol dihydrate, meso-erythritol, pentaerythritol, D-gluconic acid, phthalic acid, citric acid monohydrate, l,l,l-tris(hydroxymethyl)ethane, D-fructose, D-glucose anhydrous, xylose, maltitol (e.g., D-sorbitol), D- (+)glucosamine hydrochloride, hydantoin, erythorbic acid, phloroglucinol dihydrate, meso-erythritol, pentaerythritol, D-gluconic acid, phthalic acid,
- Ceramic bubbles useful in practicing the present invention are typically generally round.
- the bubbles need not be perfectly spherical, and may, for example, be cratered or ellipsoidal.
- Suitable ceramic bubbles can be made by techniques known in the art and/or are commercially available. For example, techniques for making glass bubbles are reported, for example, in U.S. Pat. Nos.
- one exemplary soda-lime-borosilicate glass bubble formulation comprises, by weight, at least 90%, 94%, or even 97% of glass that in turn comprises at least 67% SiO 2 , (e.g., a range of 70% to 80% SiO 2 ), a range of 8% to 15% CaO, a range of 3% to 8% Na 2 O, a range of 2% to 6% B 2 O 3 , and a range of 0.125% to 1.5% SO 3 .
- Glass bubbles are commercially available, for example, from 3M Company, St. Paul, MN under the trade designations "3M HOLLOW GLASS MICROSPHERES, HGS
- SERIES e.g., “HGS 18000”
- 3M GLASS BUBBLES e.g., grades S60, S60HS, iM30K, Kl, K15, S15, S22, K20, K25, S32, K37, S38, S38HS, S38XHS, K46, (A16/500, A20/1000, D32/4500, and H50/10000); and from Potters Industries, Valley forge.
- PA (an affiliate of PQ Corporation) under the trade designation ''SPMERICEl MOLLOW GLASS SPHERES” ⁇ e.g., grades 110P8 and 60P18 ) and ''Q-CEL HOLLOW SPHERES” (e.g., grades 30, 6014, 6019, 6028, 6036, 6042, 6048, 5019, 5023, and 5028); and from Silbrico Corp., Hodgkins, IL under the trade designation "SIL-CELL” (e.g., grades SIL 35/34, SIL- 32, SIL-42, and SIL-43).
- SIL-CELL e.g., grades SIL 35/34, SIL- 32, SIL-42, and SIL-43.
- the ceramic bubbles are aluminosilicate bubbles extracted from pulverized fuel ash collected from coal-fired power stations (i.e., cenospheres).
- Useful cenospheres include those marketed by Sphere One, Inc., Chattanooga, TN, under the trade designation ⁇ EXTENDOSPKERES HOLLOW SPHERES” (e.g., grades SG, MG, CG, TG, HA, SLG, SL-150, 300/600, 350, XOL -200, XOL-150, FM-I); and those marketed by 3M Company under the trade designation "3M HOLLOW CERAMIC MICROSPHERES” (e.g., grades G-3125, G-3150, and G-3500). Cenospheres typically have average true densities in a range from 0.7 g/cm 3 to 0.8 g/cm 3 .
- the ceramic bubbles have average true densities in a range from about 0.1 g/cm 3 to about 0.9 g/cm 3 (in some embodiments, in a range from about 0.2 g/cm 3 to about 0.7 g/cm ), although densities outside of these ranges may also be useful.
- the glass bubbles have diameters in a range from about 5 micrometers to about 250 micrometers (in some embodiments, in a range from about 10 micrometers to about 110 micrometers, or even about 10 micrometers to about 70 micrometers), although sizes outside of these ranges may also be useful.
- the glass bubbles have median diameters in a range from 20 micrometers to about 40 micrometers.
- the ceramic bubbles such as cenospheres have diameters in a range from about 5 micrometers to about 500 micrometers (in some embodiments, in a range from about 50 micrometers to about 300 micrometers, or even about 75 micrometers to about 200 micrometers), although sizes outside of these ranges may also be useful.
- the amount of bubbles present are sufficient to reduce the density of the fluid at least 5% (in some embodiments, at least 10%, 15%, 20%, 25%, or even at least 30%).
- the ceramic bubbles comprise in a range from about 25 to about 50 percent by volume of the drilling fluid. Reducing the density of the drilling fluid is advantageous, for example, by significantly reducing the pressures required to raise the drilling fluid to the surface, as well as in reducing the associated pumping costs.
- the compressive strength required of the ceramic bubbles is dependent on the particular intended use of the fluid. For example in drilling applications, the compressive strength required of the ceramic bubbles is typically dictated by the bottom hole pressure in which it will be employed.
- the compressive strength of the ceramic bubbles does not have to be high, but in very deep wellbores, and/or at very great depths under the sea, the hydrostatic pressure exerted on the ceramic bubbles becomes enormous, and the ceramic bubbles should have very high resistance to collapse (high compressive strengths).
- Bubbles because of their generally spherical form, provide resistance to compression equally from all directions (isotropic compressive strength), and are ideally suited for this application.
- the ceramic bubble component has a collapse strength of at least 2000 psi (13.8 MPa) (in some embodiments at least 3000 psi (20.7
- MPa 4000 psi (27.6 MPa), 5500 psi (37.9 MPa), 6000 psi (41.1 MPa), 10,000 psi (68.9 MPa), or at least even 18,000 psi (124.1 MPa)).
- Embodiments of low density aqueous fluids according to the present invention are also useful, for example in dual gradient drilling.
- the low density aqueous fluid is introduced at the base of a riser at or near the seafloor, to facilitate pressure control in the drilling operations.
- additives that may be included in fluids described herein include alkalinity and pH control additives, bactericides, calcium reducers, corrosion inhibitors, defoamers, emulsif ⁇ ers, filtrate reducers, flocculants, foaming agents, hydrate suppressants, lost circulation materials, lubricants/pipe-freeing agents, shale control inhibitors, surface active agents, temperature stability agents, thinners, dispersants, viscosifiers, and weighting materials.
- alkalinity and pH control additives include alkalinity and pH control additives, bactericides, calcium reducers, corrosion inhibitors, defoamers, emulsif ⁇ ers, filtrate reducers, flocculants, foaming agents, hydrate suppressants, lost circulation materials, lubricants/pipe-freeing agents, shale control inhibitors, surface active agents, temperature stability agents, thinners, dispersants, viscosifiers, and weighting materials.
- mixing gas e.g., nitrogen, carbon dioxide, or air
- mixing gas e.g., nitrogen, carbon dioxide, or air
- Such methods include those described, for example, in U. S. Pat. Nos. 3,463,231 (Hutchison et al.) and 3,819,519 (Sharman et al).
- the present invention also provides a method of drilling, the method comprising circulating a drilling fluid described herein down a drill string and up an annulus between the drill string and borehole.
- the present invention also provides a method of drilling wherein the pressure of the drilling fluid may be controlled to prevent blowouts, kicks or other uncontrolled pressure conditions.
- the drilling fluid pressure should be kept between the pore pressure of the well and the fracturing pressure of the surrounding well formation. If the fluid pressure is too low, the formation fluid can force the fluid from the wellbore or annulus resulting in a kick or blowout. If the fluid pressure is too high the formation adjacent the well bore may fracture resulting in loss of fluid circulation and loss of fluid and cuttings to the fracture. Glass bubbles can be used to control the density of aqueous drilling fluids, and therefore to control the pressure the fluid exerts on the formation.
- Fluid-Gel Test [031] Whether a material was fluid can be verified using the following "Fluid-Gel Test”.
- the mixture (after at least 18 days) was tested according to the Fluid-Gel Test described above, and designated a fluid.
- Example 2 was prepared and tested as described in Example 1, except 3 grams of D-(+)-glucosamine hydrochloride (CAS # 66-84-2; obtained from Calbiochem, La Jolla, CA) was used in place of the D-sorbitol. After at least about 16 hours, the fluid was observed to remain as a fluid, with a small but perceptible increase in viscosity. The mixture was still free flowing after at least 7 days. [035] Further, the mixture (after at least 10 days) was designated a fluid when tested according to the Fluid-Gel Test described above.
- D-(+)-glucosamine hydrochloride CAS # 66-84-2; obtained from Calbiochem, La Jolla, CA
- Example 3 was prepared and tested as described in Example 1, except 3 grams of hydantoin (CAS # 461-72-3; 99%; obtained from Aldrich Chemical Company, Milwaukee, WI) was used in place of the D-sorbitol. After at least about 16 hours, the fluid was observed to remain as a fluid, with a small but perceptible increase in viscosity. The mixture was still free flowing after at least 7 days. [037] Further, the mixture (after at least 10 days) was designated a fluid when tested according to the Fluid-Gel Test described above.
- Example 4 was prepared and tested as described in Example 1, except 3 grams of erythorbic acid (obtained from Pfizer Chemical Division, New York, NY) was used in place of the D-sorbitol. After at least about 16 hours, the fluid was observed to remain as a fluid, with a small but perceptible increase in viscosity. The mixture was still free flowing after at least 7 days.
- erythorbic acid obtained from Pfizer Chemical Division, New York, NY
- the mixture (after at least 10 days) was designated a fluid when tested according to the Fluid-Gel Test described above.
- Example 5 was prepared and tested as described in Example 1, except 3 grams of phloroglucinol dihydrate (CAS # 6099-90-7; 97%; obtained from Aldrich Chemical Company) was used in place of the D-sorbitol. After about at least 16 hours, the fluid was observed to remain as a fluid, with a small but perceptible increase in viscosity. The mixture was still free flowing after at least 7 days.
- phloroglucinol dihydrate CAS # 6099-90-7; 97%; obtained from Aldrich Chemical Company
- Example 6 was prepared and tested as described in Example 1, except 3 grams of meso-erythritol (obtained from Aldrich Chemical Company) was used in place of the D- sorbitol. After at least about 16 hours, the fluid was observed to remain as a fluid, with a small but perceptible increase in viscosity. The mixture was still free flowing after at least
- the mixture (after at least 10 days) was designated a fluid when tested according to the Fluid-Gel Test described above.
- Example 7 was prepared and tested as described in Example 1, except 3 grams of pentaerythritol (Purified Grade; obtained from Fisher Scientific Co, Fair Lawn, NJ) was used in place of the D-sorbitol. After at least about 16 hours, the fluid was observed to remain as a fluid, with a small but perceptible increase in viscosity. The mixture was still free flowing after at least 7 days.
- pentaerythritol Purified Grade; obtained from Fisher Scientific Co, Fair Lawn, NJ
- the mixture (after at least 10 days) was designated a fluid when tested according to the Fluid-Gel Test described above.
- Example 8 was prepared and tested as described in Example 1, except 3 grams of
- D-gluconic acid, potassium salt (CAS # 299-27-4; 99%; obtained from Aldrich Chemical Company) was used in place of the D-sorbitol. After at least about 16 hours, the fluid was observed to remain as a fluid, with a small but perceptible increase in viscosity. The mixture was still free flowing after at least 7 days. [047] Further, the mixture (after at least 10 days) was designated a fluid when tested according to the Fluid-Gel Test described above.
- Example 9 was prepared and tested as described in Example 1, except 3 grams of phthalic acid (CAS # 88-99-3; 98%; obtained from Aldrich Chemical Company) was used in place of the D-sorbitol. After at least about 16 hours, the fluid was observed to remain as a fluid, with a small but perceptible increase in viscosity. The mixture was still free flowing after at least 7 days.
- phthalic acid CAS # 88-99-3; 98%; obtained from Aldrich Chemical Company
- the mixture (after at least 10 days) was designated a fluid when tested according to the Fluid-Gel Test described above.
- Example 10 was prepared and tested as described in Example 1, except 3 grams of citric acid monohydrate (ACS, 99.0-102.0%; obtained from Alfa Aesar) was used in place of the D-sorbitol. After at least about 16 hours, the fluid was observed to remain as a fluid, with a small but perceptible increase in viscosity. The mixture was still free flowing after at least 7 days.
- ACS citric acid monohydrate
- the mixture (after at least 10 days) was designated a fluid when tested according to the Fluid-Gel Test described above.
- Example 11 was prepared and tested as described in Example 1, except 3 grams of l,l,l-tris(hydroxymethyl)ethane (CAS # 77-85-0; 99%; obtained from Aldrich Chemical Company) was used in place of the D-sorbitol. After at least about 16 hours, the fluid was observed to remain as a fluid, with a small but perceptible increase in viscosity. The mixture was still free flowing after at least 7 days.
- the mixture (after at least 10 days) was designated a fluid when tested according to the Fluid-Gel Test described above.
- Example 12 was prepared and tested as described in Example 1, except 3 grams of
- D-fructose (98%; obtained from Aldrich Chemical Company) was used in place of the D- sorbitol. After at least about 16 hours, the fluid was observed to remain as a fluid, with a small but perceptible increase in viscosity. The mixture was still free flowing after at least 7 days. [055] Further, the mixture (after at least 10 days) was designated a fluid when tested according to the Fluid-Gel Test described above.
- Example 13 was prepared and tested as described in Example 1, except 3 grams of D-glucose anhydrous (obtained from Merck Co., Inc, Rahway, NJ) was used in place of the D-sorbitol. After at least about 16 hours, the fluid was observed to remain as a fluid, with a small but perceptible increase in viscosity. The mixture was still free flowing after at least 7 days.
- D-glucose anhydrous obtained from Merck Co., Inc, Rahway, NJ
- the mixture (after at least 10 days) was designated a fluid when tested according to the Fluid-Gel Test described above.
- Example 14 was prepared and tested as described in Example 1, except 3 grams of D-xylose (CAS # 58-86-6; obtained from Avocado Research Chemicals, Ltd., Heysham, Lancaster, UK) was used in place of the D-sorbitol. After at least about 16 hours, the fluid was observed to remain as a fluid, with a small but perceptible increase in viscosity. The mixture was still free flowing after at least 7 days.
- D-xylose CAS # 58-86-6; obtained from Avocado Research Chemicals, Ltd., Heysham, Lancaster, UK
- the mixture (after at least 10 days) was designated a fluid when tested according to the Fluid-Gel Test described above.
- Example 15 was prepared and tested as described in Example 1, except 3 grams of
- Example 16 was prepared and tested as described in Example 1, except 3 grams of D-(+)-mannose (obtained from The Matheson Co. Inc., East Rutherford, NJ) was used in place of the D-sorbitol. After at least about 16 hours, the fluid was observed to remain as a fluid, with a small but perceptible increase in viscosity. The mixture was still free flowing after at least 7 days.
- D-(+)-mannose obtained from The Matheson Co. Inc., East Rutherford, NJ
- the mixture (after at least 10 days) was designated a fluid when tested according to the Fluid-Gel Test described above.
- Example 17 was prepared and tested as described in Example 1, except 3 grams of high fructose corn syrup (026550; obtained under the trade designation "INVERTOSE” from Corn Products, Bedford Park, IL) was used in place of the D-sorbitol. After at least about 16 hours, the fluid was observed to remain as a fluid, with a small but perceptible increase in viscosity. The mixture was still free flowing after at least 7 days. [065] Further, the mixture (after at least 10 days) was designated a fluid when tested according to the Fluid-Gel Test described above.
- Example 18 was prepared and tested as described in Example 1, except 10 grams of the aqueous drilling fluid was mixed by hand in a 6 dram vial with 1 gram of D-(+)- maltose monohydrate (obtained from Aldrich Chemical Company) and 1 gram of ceramic microspheres ("3M HOLLOW GLASS MICROSPHERES HGS 18000"). After at least about 20 hours, the mixture was found to be a fluid when tested according to the Fluid-Gel test described above.
- Example 19 was prepared and tested as described in Example 18, except 10 grams of the aqueous drilling fluid was mixed by hand in a 6 dram vial with 1 gram of glycerol
- Example 20 was prepared and tested as described in Example 18, except 10 grams of the aqueous drilling fluid was mixed by hand in a 6 dram vial with 0.1 gram of D- sorbitol and 1 gram of ceramic microspheres ("3M HOLLOW GLASS MICROSPHERES HGS 18000"). After at least about 10 days, the mixture was found to be a fluid when tested according to the Fluid-Gel Test described above.
- Example 21 was prepared and tested as described in Example 18, except 10 grams of the aqueous drilling fluid was mixed by hand in a 6 dram vial with 0.3 gram of D- sorbitol and 0.1 gram of borax (obtained as borax under the trade designation "20 MULE TEAM" from Dial Corp. Scottsdale, AZ) was used in place of the Glass Bubbles. After at least about 10 days, the mixture was found to be a fluid when tested according to the Fluid-Gel Test described above.
- Example 22 was prepared and tested as described in Example 18, except 5 grams of 1,6-hexanediol was used in place of the D-sorbitol. After at least about 20 hours, the mixture was found to be a fluid when tested according to the Fluid-Gel Test described above, with the further observation that there was a significant amount of precipitated solids present in the mixture.
- Example B Illustrative Example B was prepared and tested as described in Example 1, except 3 grams of dipentaerythritol (CAS # 126-58-9; tech.; obtained from Aldrich Chemical Company) was used in place of the D-sorbitol. After about 16 hours, the fluid was observed to be a gelled mass, no longer fluid, which could be easily cut with a wooden stick. This gel is similar to a soft gelatin which will not flow under its own weight, and hence clearly would not flow through the funnel in 1 minute if tested using the Fluid-Gel Test described above.
- dipentaerythritol CAS # 126-58-9; tech.; obtained from Aldrich Chemical Company
- Example C Illustrative Example C was prepared and tested as described in Example 1, except 3 grams of 1,6-hexanediol (99+%; obtained from Aldrich Chemical Company) was used in place of the D-sorbitol. After about 16 hours, the fluid was observed to be a gelled mass, no longer fluid, which could be easily cut with a wooden stick. This gel is similar to a soft gelatin which will not flow under its own weight, and hence clearly would not flow through the funnel in 1 minute if tested using the Fluid-Gel Test described above.
- Example D Illustrative Example D was prepared and tested as described in Example 1 , except 3 grams of D-(+)-maltose monohydrate (obtained from Aldrich Chemical Company) was used in place of the D-sorbitol. After about 16 hours, the fluid was observed to be a gelled mass, no longer fluid, which could be easily cut with a wooden stick. This gel is similar to a soft gelatin which will not flow under its own weight, and hence clearly would not flow through the funnel in 1 minute if tested using the Fluid-Gel Test described above.
- Example E was prepared and tested as described in Example 1, except 3 grams of sucrose (sugar; obtained from Super Value Inc., Eden Prairie, MN) was used in place of the D-sorbitol. After about 16 hours, the fluid was observed to be a gelled mass, no longer fluid, which could be easily cut with a wooden stick. This gel is similar to a soft gelatin which will not flow under its own weight, and hence clearly would not flow through the funnel in 1 minute if tested using the Fluid-Gel Test described above.
- sucrose sucrose
- Example F Illustrative Example F was prepared and tested as described in Example 1 , except 3 grams of glycerol (obtained from Alfa Aesar) was used in place of the D-sorbitol. After about 16 hours, the fluid was observed to be a gelled mass, no longer fluid, which could be easily cut with a wooden stick. This gel is similar to a soft gelatin which will not flow under its own weight, and hence clearly would not flow through the funnel in 1 minute if tested using the Fluid-Gel Test described above.
- glycerol obtained from Alfa Aesar
- Illustrative Example G was prepared and tested as described in Example 1, except
- Example H Illustrative Example H was prepared and tested as described in Example 1, except 3 grams of acetic acid (obtained from J T Baker, Phillipsburg, NJ) was used in place of the D-sorbitol. After about 16 hours, the fluid was observed to be a gelled mass, no longer fluid, which could be easily cut with a wooden stick. This gel is similar to a soft gelatin which will not flow under its own weight, and hence clearly would not flow through the funnel in 1 minute if tested using the Fluid-Gel Test described above.
- acetic acid obtained from J T Baker, Phillipsburg, NJ
- Example I was prepared and tested as described in Example 1 , except 3 grams of glycolic acid (obtained from Aldrich Chemical Company) was used in place of the D-sorbitol. After about 16 hours, the fluid was observed to be a gelled mass, no longer fluid, which could be easily cut with a wooden stick. This gel is similar to a soft gelatin which will not flow under its own weight, and hence clearly would not flow through the funnel in 1 minute if tested using the Fluid-Gel Test described above.
- Illustrative Example J is similar to a soft gelatin which will not flow under its own weight, and hence clearly would not flow through the funnel in 1 minute if tested using the Fluid-Gel Test described above.
- Example J Illustrative Example J was prepared and tested as described in Example 1, except 3 grams of polysorbate (obtained from Uniqema, New Castle, DE under the trade designation "TWEEN 60" (NF)) was used in place of the D-sorbitol. After about 16 hours, the fluid was observed to be a gelled mass, no longer fluid, which could be easily cut with a wooden stick. This gel is similar to a soft gelatin which will not flow under its own weight, and hence clearly would not flow through the funnel in 1 minute if tested using the Fluid-Gel Test described above.
- polysorbate obtained from Uniqema, New Castle, DE under the trade designation "TWEEN 60" (NF)
- Example K Illustrative Example K was prepared and tested as described in Example 1, except 3 grams of cetyl alcohol (obtained from The Chemistry Store Dot Com, Cayce, SC) was used in place of the D-sorbitol. After about 16 hours, the fluid was observed to be a gelled mass, no longer fluid, which could be easily cut with a wooden stick. This gel is similar to a soft gelatin which will not flow under its own weight, and hence clearly would not flow through the funnel in 1 minute if tested using the Fluid-Gel Test described above.
- cetyl alcohol obtained from The Chemistry Store Dot Com, Cayce, SC
- Example L Illustrative Example L was prepared and tested as described in Example 1, except 3 grams of sorbitan monostearate (obtained from Uniqema under the trade designation "ARLACEL 60") was used in place of the D-sorbitol. After about 16 hours, the fluid was observed to be a gelled mass, no longer fluid, which could be easily cut with a wooden stick. This gel is similar to a soft gelatin which will not flow under its own weight, and hence clearly would not flow through the funnel in 1 minute if tested using the Fluid-Gel Test described above.
- Illustrative Example M was prepared and tested as described in Illustrative Example A, except 10 grams of the aqueous drilling fluid was mixed in a 6 dram glass vial with 2.5 grams of an aqueous solution, prepared by mixing 20 grams of deionized water with 10 grams of ceramic microspheres ("3M HOLLOW GLASS MICROSPHERES HGS 18000") and filtering the mixture through Whatman # 5 filter paper (Whatman International Ltd., Maidstone, Kent, UK). After about 20 hours, the fluid was found to be a fluid when tested according to the Fluid-Gel Test described above.
- Illustrative Example N was prepared as described in Example M, except 0.3 gram of D-sorbitol was added to the aqueous drilling fluid prior to the addition of the aqueous solution. After about 20 hours, the fluid was found to be a fluid when tested according to the Fluid-Gel Test described above.
- Illustrative Example O was prepared by diluting 10 grams of the aqueous drilling fluid with 10 grams of deionized water in a 6 dram vial, and mixing by hand 2 grams of ceramic microspheres ("3M HOLLOW GLASS MICROSPHERES HGS 18000"). After about 20 hours, the fluid was found to be a fluid when tested according to the Fluid-Gel Test described above.
- Example P Illustrative Example P was prepared and tested as described in Example O, except 0.1 gram of borax (Dial Corp.) was used in place of the glass bubbles. After about 16 hours, the fluid was observed to be a gelled mass, no longer fluid, which could be easily cut with a wooden stick. This gel is similar to a soft gelatin which will not flow under its own weight, and did not pass the Fluid-Gel Test described above.
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- Engineering & Computer Science (AREA)
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- Cosmetics (AREA)
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Abstract
Description
Claims
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US12/521,096 US8324135B2 (en) | 2006-12-28 | 2007-12-21 | Aqueous fluid and method of making and using the same |
EP07869728A EP2118232A2 (en) | 2006-12-28 | 2007-12-21 | Aqueous fluid and method of making and using the same |
BRPI0722066-9A2A BRPI0722066A2 (en) | 2006-12-28 | 2007-12-21 | WATER FLUID AND METHOD OF MANUFACTURING AND USE THEREOF |
NO20092703A NO20092703L (en) | 2006-12-28 | 2009-07-16 | Aqueous fluid and process for making and using the same |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US88234206P | 2006-12-28 | 2006-12-28 | |
US60/882,342 | 2006-12-28 |
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WO2008083063A2 true WO2008083063A2 (en) | 2008-07-10 |
WO2008083063A3 WO2008083063A3 (en) | 2008-09-12 |
Family
ID=39589182
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US2007/088511 WO2008083063A2 (en) | 2006-12-28 | 2007-12-21 | Aqueous fluid and method of making and using the same |
Country Status (6)
Country | Link |
---|---|
US (1) | US8324135B2 (en) |
EP (1) | EP2118232A2 (en) |
CN (1) | CN101578347A (en) |
BR (1) | BRPI0722066A2 (en) |
NO (1) | NO20092703L (en) |
WO (1) | WO2008083063A2 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2012061241A2 (en) | 2010-11-03 | 2012-05-10 | 3M Innovative Properties Company | Fluid composition comprising glass microspheres and method of making and using the same |
WO2021003145A1 (en) * | 2019-07-01 | 2021-01-07 | Highland Fluid Technology, Inc. | Managed pressure drilling with novel noncompressible light weight fluid |
WO2022165581A1 (en) * | 2021-02-08 | 2022-08-11 | Uniquem Inc. | Water-based drilling fluids comprising salts and non-reducing sugar alcohols |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102477289A (en) * | 2010-11-26 | 2012-05-30 | 中联煤层气有限责任公司 | Drilling fluid |
CN102888213B (en) * | 2011-07-21 | 2015-01-07 | 北京博德世达石油技术有限公司 | Clay-content-free drilling fluid |
CN105154040A (en) * | 2015-10-01 | 2015-12-16 | 中国石油集团西部钻探工程有限公司 | Ultra-low-density water-based drilling fluid and preparation method thereof |
CN111117583B (en) * | 2018-10-31 | 2022-02-01 | 中国石油天然气股份有限公司 | Fracturing diverting agent and preparation method thereof |
Citations (4)
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US5658861A (en) * | 1994-03-15 | 1997-08-19 | Dowell Schlumberger Incorporated | Delayed borate crosslinked fracturing fluid having increased temperature range |
US6214773B1 (en) * | 1999-09-29 | 2001-04-10 | Halliburton Energy Services, Inc. | High temperature, low residue well treating fluids and methods |
US6906009B2 (en) * | 2002-08-14 | 2005-06-14 | 3M Innovative Properties Company | Drilling fluid containing microspheres and use thereof |
US20060205605A1 (en) * | 2005-03-08 | 2006-09-14 | Dessinges Marie N | Well treatment composition crosslinkers and uses thereof |
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NL232500A (en) | 1957-10-22 | |||
US3030216A (en) * | 1958-11-04 | 1962-04-17 | Martin Marietta Corp | Refractory composition |
US3230064A (en) * | 1960-10-21 | 1966-01-18 | Standard Oil Co | Apparatus for spherulization of fusible particles |
US3365315A (en) * | 1963-08-23 | 1968-01-23 | Minnesota Mining & Mfg | Glass bubbles prepared by reheating solid glass partiles |
US3463231A (en) * | 1968-02-12 | 1969-08-26 | Chevron Res | Generation and use of foamed well circulation fluids |
US3819519A (en) * | 1968-11-27 | 1974-06-25 | Chevron Res | Foam circulation fluids |
US4279632A (en) * | 1979-05-08 | 1981-07-21 | Nasa | Method and apparatus for producing concentric hollow spheres |
US4391646A (en) * | 1982-02-25 | 1983-07-05 | Minnesota Mining And Manufacturing Company | Glass bubbles of increased collapse strength |
ZA831343B (en) | 1982-04-08 | 1983-11-30 | Pq Corp | Hollow microspheres with organosilicon-silicate surfaces |
US4767726A (en) * | 1987-01-12 | 1988-08-30 | Minnesota Mining And Manufacturing Company | Glass microbubbles |
US6617285B2 (en) * | 2001-07-03 | 2003-09-09 | Baker Hughes Incorporated | Polyols for breaking of borate crosslinked fracturing fluid |
US6794340B2 (en) * | 2002-06-25 | 2004-09-21 | Halliburton Energy Services, Inc. | Method for removing drill cuttings from wellbores and drilling fluids |
-
2007
- 2007-12-21 US US12/521,096 patent/US8324135B2/en not_active Expired - Fee Related
- 2007-12-21 WO PCT/US2007/088511 patent/WO2008083063A2/en active Application Filing
- 2007-12-21 BR BRPI0722066-9A2A patent/BRPI0722066A2/en not_active IP Right Cessation
- 2007-12-21 EP EP07869728A patent/EP2118232A2/en not_active Withdrawn
- 2007-12-21 CN CNA2007800485871A patent/CN101578347A/en active Pending
-
2009
- 2009-07-16 NO NO20092703A patent/NO20092703L/en not_active Application Discontinuation
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5658861A (en) * | 1994-03-15 | 1997-08-19 | Dowell Schlumberger Incorporated | Delayed borate crosslinked fracturing fluid having increased temperature range |
US6214773B1 (en) * | 1999-09-29 | 2001-04-10 | Halliburton Energy Services, Inc. | High temperature, low residue well treating fluids and methods |
US6906009B2 (en) * | 2002-08-14 | 2005-06-14 | 3M Innovative Properties Company | Drilling fluid containing microspheres and use thereof |
US20060205605A1 (en) * | 2005-03-08 | 2006-09-14 | Dessinges Marie N | Well treatment composition crosslinkers and uses thereof |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2012061241A2 (en) | 2010-11-03 | 2012-05-10 | 3M Innovative Properties Company | Fluid composition comprising glass microspheres and method of making and using the same |
EP2635650A2 (en) * | 2010-11-03 | 2013-09-11 | 3M Innovative Properties Company | Fluid composition comprising glass microspheres and method of making and using the same |
EP2635650A4 (en) * | 2010-11-03 | 2014-04-02 | 3M Innovative Properties Co | Fluid composition comprising glass microspheres and method of making and using the same |
WO2021003145A1 (en) * | 2019-07-01 | 2021-01-07 | Highland Fluid Technology, Inc. | Managed pressure drilling with novel noncompressible light weight fluid |
US11549045B2 (en) | 2019-07-01 | 2023-01-10 | Highland Fluid Technology, Inc. | Managed pressure drilling with novel noncompressible light weight fluid |
WO2022165581A1 (en) * | 2021-02-08 | 2022-08-11 | Uniquem Inc. | Water-based drilling fluids comprising salts and non-reducing sugar alcohols |
Also Published As
Publication number | Publication date |
---|---|
WO2008083063A3 (en) | 2008-09-12 |
EP2118232A2 (en) | 2009-11-18 |
NO20092703L (en) | 2009-09-04 |
CN101578347A (en) | 2009-11-11 |
BRPI0722066A2 (en) | 2014-04-01 |
US20100093564A1 (en) | 2010-04-15 |
US8324135B2 (en) | 2012-12-04 |
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