Borate crosslinked fracturing fluid and method
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- CA2154950C CA2154950C CA 2154950 CA2154950A CA2154950C CA 2154950 C CA2154950 C CA 2154950C CA 2154950 CA2154950 CA 2154950 CA 2154950 A CA2154950 A CA 2154950A CA 2154950 C CA2154950 C CA 2154950C
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; MISCELLANEOUS COMPOSITIONS; MISCELLANEOUS APPLICATIONS OF MATERIALS
- 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
- C09K8/66—Compositions based on water or polar solvents
- C09K8/68—Compositions based on water or polar solvents containing organic compounds
- C09K8/685—Compositions based on water or polar solvents containing organic compounds containing cross-linking agents
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S507/00—Earth boring, well treating, and oil field chemistry
- Y10S507/922—Fracture fluid
w__ ~~~~9~0 Patent 56.347 IMPROVED BORATE CROSSLINKEID FRACTURING FLUID AND METHOD
This invention relates to the recovery of hydrocarbon fluids from subterranean formations. More particularly, i:he invention relates to a novel well treatment fluid, a process for its preparation, and to a rnethod of treating or fracturing a subterranean formation using such fluid.
BACKGROUND OF THE INVENTION
In the process of recovering hydrocarbon values from subterranean formations, it is common practice to treat a hydrocarbon-bearing formation with a pressurized fluid to provide flow channels, i.E:., to fracture the formation, or to use such fluids to control sand to facilitate flow of the hydrocarbons to the wellbore.
Well treatment fluids, particularly those used in fracturing, typically comprise a water or oil based fluid incorporating a thickening agent, normally a polymeric material. The thickening agent helps to control leak-off of the fluid into the formation, and aids in the transfer of hydraulic fracturing pressure to the rock surfaces. Primarily, however, the thickening agent permits the suspension and transfer into the formation of proppant materials which remain in the fracture or sand when the hydraulic pressure is released, thereby holding the fracture open or stabilizing the sand.
Typical polymeric thickening agents for use in such fluids comprise galactomannan gums, such as guar and substituted guars such as hydroxypropyl guar and carboxymethylhydroxypropyl guar. Celluilosic polymers such as hydroxyethyl cellulose may be used, as well as synthetic polymers such as polyacrylamide.
To increase the viscosity, and, therefore, the proppant carrying ability of the fracturing fluid, as well as increase its high temperature stability, crosslinking of the polymeric materials employed is 56.347 also commonly practiced. Typical cross linkiing agents comprise soluble boron, zirconium, and titanium compounds.
By necessity, well treatment fluids are prepared on the surface, and then pumped through tubing in the wellbore to the hydrocarbon-bearing subterranean formation. While high viscosity, thickened fluid is highly desirable within the formation in order to transfer hydraulic pressure efficientl~~ to the rock and to reduce fluid leak-off, large amounts of energy are required to pump such fluids through the tubing into the formation.
To reduce the amount of energy required, various methods of delaying crosslinking have been developed. These techniques allow the pumping of a relatively less viscous fluid having relatively low friction pressures within the well tubing with crosslinking being effected near or in the formation so that the advantageous properties of thickened crosslinked fluid are available at the rock face.
One typical delayed crosslinking well treatment fluid system comprises borate crosslinked galactomannan gums such as guar or hydroxypropyl guar. The galactomannan polymers; which may be provided as a solid or as a suspension in a hydrocarbon, hydrate in neutral or acidic solution to form a gel. Under these conditions, i.e., pH of 7 or lower, no crosslinking of guar or hydroxypropyl guar will occur with borate ion. To effect borate crosslinking of guar and hydroxypropyl guar, the pH must be raised to at least 9Ø The requirement to raise the pH to this level has been exploited to delay the crosslinking of the galactomannan gums by borate ion.
The practice of delaying crosslinking of thickening agents in such fluids, however, presents its own set of difficulties. -thus, sophisticated techniques must be employed to adjust the pH of the fluid at the proper location, i.e., in or near the formation.
U.S. patent 5,259,455, for example, describes the practice of controlled dissolution of Mg0 in a fracturing fluid to provide such pH adjustment. To be able to operate effectively where formation temperatures are above 200oF, the patent discloses additives to prevent the magnesium precipitation which would lo~nrer the pH of the system.
21 ~ 4 9 ~ ~ 56.34 An alternative approach to downhole pH adjustment would be some reduction of the concentration of the thickening agent in the well treatment fluid, with crosslinking being accomplished or being only slightly delayed, the reduced loading thereby reducing the friction penalty. However, reduction of the thickening agent concentration ( i.e., use of a lower concentration) in such fluids has not been practiced to any significant extent because of a long-established belief by those skilled in the art that minimum levels of loading of the thickening agents mentioned are required for effective or sufficient crosslinking. In the case of guar, for example, this concentration has been considered to be about 17 pounds of guar per one thousand gallons of aqueous fracturing fluid. This belief was based on studies of they radius of gyration of the guar molecule and the theory that if the radius of gyration of twc> molecules in solution do not overlap, the molecules cannot be crosslinked to produce the type of gel required for reliable fracturing operations. As a general proposition, most v~rell treatment solutions employed in the field utilizing crosslinking of the thickening agent prior to the invention have utilized concentrations of the delayed crosslinking thickening agents that are well above the level mentioned, and, typically, 30 pounds per 1000 gallons of liquid or greater are used.
Accordingly, a need has existed for a well treatment fluid, especially a fracturing fluid, that exhibits relatively low friction loss in the well tubing, while avoiding the difficulties associated with raising the pH at the proper time or location, and further avoids those difficulties associated with insufficient ~;,rosslinking. Further, there has existed a need for an effective fluid having reduced concentrations of thickening agent or agents, thereby reducing the costs of such solutions and improving the conductivity of the formations. Finally, there has existed a need for a method of treating or fracturing a subterranean formation characterized by use of a low cost fracturing fluid that is not dependent on precision pH adjustment downhole. The invention addresses these needs.
SUMMARY OF THE INVENTION
Surprisingly, it has been found that the hydrated galactomannan gum component of a low or reduced concentration hydrated galactomannan gum cont<~ining fluid may be crosslinked by a suitable metal crosslinking agent if appropriate buffering of the fluid is provided. Moreover, it has been found that buffered, low conceni~ration hydrated metal crosslinked galactomannan gum thickened fluids according to the invention are effective wel:1 treatment fluids that are easily transported down well with significant energy saving.
Accordingly, in one embodiment, the invention relates to a well treating composition comprising an aqueous hydrated metal crosslinked galactomannan gum containing fluid containing a buffering agent comprising a week acid and a salt of said weak acid, in an amount sufficient to provide a pH of from about 9.0 to about 12 in the fluid. (Preferably the pH is from about 9.5 to about 11.75. More particularly, the invention relates to a well treatment fluid of the galactomannan gum type which is buffered by the addition of or which contains a selected buffering agent or agents in a concentration sufficient to provide or maintain a pH in the solution or fluid of from about 9.0 to about 12. In a preferred embodiment, the invention relates to a well tre<~tment or fracturing fluid of the type described wherein the buffering agent comprises a weak acid and an ammonium or all~cali metal salt of a weak acid, the acid and salt being selected to provide a pH of the fluid between 9.0 and 11. In a most preferred embodiment, the invention relates to a fracturing fluid composition comprising A
an aqueous hydrated borate cros:alinked galactomannan gum solution containing a buffering agent, the buffering agent being present in the solution in an amount sufficient to provide the fluid with a pH of i'rom about 9.0 to about 12. As used herein, the term "well treatment" refers generally to operations undertaken with respE~ct to a well and formation, including, but not limited to, i'racturing and sand control, while the term "galactomannan gum" is understood to include mixtures of such gums.
In a further embodiment of the invention, the invent ion relates to a method oi' t neat ing a subterranean formation penetrated by a borehole, comprising injecting into the borehole and into contact w:lth the formation, at a rate and pressure sufficient to t neat: the format ion, a f luid composition comprising an aqueous hydrated metal crosslinked - 4a -A
215 ~ 9 ~ p 56.347 galactomannan gum solution buffered to a pH of from about 9.0 to about 12.
Preferably, the fluid is injected at a pressure sufficient to fracture the formation. More particularly, the invention relates to a method of treating or fracturing characterized by use of a fluid of the galactomannan gum type wherein the buffering agent comprises a weak acid and an ammonium or alkali metal salt of a weak acid, the acid and salt being selected to provide a pH of the fluid of solution between about 9~.0 and about 12. In a preferred embodiment, the galactomannan gum is borate crosslinked, and buffering agent is present in the solution in an amount sufficient to provide or' maintain the fluid with a pH
of from about 9.0 to about 12.
Finally, the invention relates to a process for preparing a fluid of the type described. According to this embodiment of the invention, galactomannan gum is dissolved or suspended in a neutral or acidic aqueous solution to form hydrated galactomannan gum. A crosslinking metal releasing agent and a buffering agent or agents, in a concentration sufficient to provide or maintain a pH in the solution or fluid of from about 9.0 to about 12, are then combined with the hydrated gum, simultaneously, or in any order, to form an aqueous hydrated metal crosslinked galactomannan gum solution buffered to a pH of from about 9.0 to about 12. As used herein, the term "crosslinking metal releasing agent" is taken to designate those metal or metal containing materials which will provide a metal ion or metal containing species in the solution capable of crosslinking the galactomannan gum. TempEsratures employed are ambient or greater.
DETAILED DESCRIPTION OF THE INVENTION
As indicated, the fluid composiitions of the invention comprise an aqueous hydrated metal crosslinked galactomannan chum solution. Preferred solutions are those derived from guar, hydroxypropyl guar, or carboxymethylhydroxypropyl guar, and mixtures thereof. Initially, the hydrated metal gum solutions may be formed by providing the gum compositions in solid powder form, or as a suspension in a hydrocarbon liquid (e.g., diesel or kerosene) and blending with a neutral or acidic aqueous solution, the hydrate _ 21 ~ ~ 9 5 0 56.347 forming a gel. As indicated, it is a surprising advantage of the invention that reduced concentrations of the hydrated crosslinked gum may be employed in the fluid.
Prefer-ably, the concentrations of the hydrated metal crosslinked gum will be below 25 pounds per 1000 gallons, being most preferably from ak>out 10 pounds to 25 pounds per gallons, it being understood that higher amounts may be employed. Superior advantages accrue at levels of from 10 to 22 pounds per' 1000 gallons of fluid.
Any suitable crosslinking metal ion, metal containing species, or mixture of such ions and species may be employed. Accordingly, as used herein, the term "metal crosslinked" is understood to include crosslinking attributable to certain metal containing species, such as borate ion. The crosslinking ions or species may be provided, as indicated, by dissolving into the solution connpounds containing the appropriate metals, or by other means. Exemplary metal ions or metal containing species include those of boron, zirconium, and titanium, supplied from compounds such as boric acid, sodium borates, boron oxide, zirconium oxide, and titanium oxide. The concentration of added crosslinking metal releasing agent is dependent on factors such as the temperature and the amount of thickening agent employed, and will normally range from about 5 ppm to about 100 ppm, preferably from about 10 ppm to about 60 pp~m . It is an important advantage of the invention that higher levels of the crosslinking metal ion or metal containing species may be employed, thereby insuring improved crosslinking. While cross-linking may be virtually immediate, a slight delay thereof, e.g., up to twenty seconds or so, may actually be preferred in the field since it allows mixing and pumping of the precursor solution through surface equipment, formation of the composition being feasible on the fly.
Any buffering agent or combinaition of such that will provide or maintain the solution at the necessary pH required may b~e employed. Thus, the combination of a weak acid and its salts may be employed, so long as the pH of the solution is maintained in the range mentioned. For example, the corresponding acid and ammonium and alkali metal phosphates, carbonates, bicarbonates, sesquicarbonates, acetates, or mixtures thereof may be used. Ammonium, potassium, and sodium carbonates, bicarbonates, 21 ~49~50 56.347 sesquicarbonates and hydrogen phosphate:> are preferred as buffer salt components.
For pH values toward the upper end of the range specified, combinations of alkali metal hydroxide and appropriate weak acid salt m<~y be employed. For example, a buffer comprising a base such as NaOH or IOH and a weak acid salt such as NA 2H2P04 may be used. Proportioning of the buffer components of the combinations to achieve the desired pH is well within the ambit of those skilled in the art. As will be appreciated by those skilled in the art, other additives commonly employed in fracturing solutions, such as breakers, clays, etc., must be selected so that they do not significantly reduce the pH of the solution. As indicated, the pH required in thE> various embodiments of the invention ranges from about 9.0 to 11, preferably from about ~i.5 to about 10. The amount of buffer required is, of course, an effective amount, i.e., an amount sufficient to maintain the desired pH, given the additives and other components of the fluid. Preferably, this amount will not exceed 50 pounds per 1000 gallons of fluid, most preferably , not more than about 20 pounds per 1000 gallons of fluid.
In order to illustrate the invention more fully, the following procedures were performed.
Base fluids comprising fifteen pounds and twenty pounds of guar respectively per 1000 gallons of fresh water, optionally containing KCI or similar salt, were prepared, and the guar in each was allowed to hydrate. The fluids also contained minor amounts of normal, non-active (from the standpoint of crosslink-ing activity) fracturing fluid additives such as a surfactant, a biocide, and a defoamer. These fluids were used in the tests reported hereinafter. Sodium sesquicarbonate and sodium carbonate were added as a buffering agent to each base fluid in the amount of 12 pounds and 5 pounds, respectively, per 1000 gallons. Finally, boric acid, as a 3.5 percent by weight solution in water, based on the weight of the water and acid, was mixed with each of the base fluids containing the buffer to give a concentration- triton of 1.5 pounds of boric acid per 1000 gallons. Borate crosslinking of the guar was effected within 5 to 20 seconds.
0 56.347 To demonstrate the suitability of the fluids for fracturing, viscosity tests were performed. The conditions of and results of lthe tests are given in the tables below. Table I
reports results with the 15 pound solution, while Table II reports results with the 20 pound solution. In both tables, viscosity results are rounded to the nearest 5th unit.
~ 1 ~ ~ ~ 5 p 56.347 TABLE I
Temperature Viscosity, 100 sec-1 c~
Initial Final(3 hours 1 ) 100 of 135 120 2) 125 of 140 110 3) 150 of 140 105 TABLE II
Temperature Viscosity, 100 sec-1 c~
Initial Final(3 hours) 1 ) 100 of 350 275 2) 125 of 370 255 3) 150 of 290 250 4) 175 of 285 180 As those skilled in the art will be aware, upon completion of fracturing, removal or breakdown of the fluid in the fracirure is important, compositions called breakers (e.g., ammonium persulfate or peroxide) being employed to assist in such. The retained conductivity of the formation after such withdrawal and/or breakdown is an important measure of fracturing- fluid efficiency. Accordingly, standardized retained conductivity tests were run on two fluids according to the invention, utilizing a combination breaker system, the fluids containing 15 pomnds (A) and 20 pounds (B), per 1000 gallons, respectively, of hydrated borate crosslinked galactomannan gum thickener. Each fluid was buffered with 12 pounds of sodium sesquicarbonate and 5 pounds of sodium 21~~9~~
56.347 carbonate. Proppant type was 20/40 Badger sand at a concentration of 2 Ibs/sq.ft. A two percent by weight KCI solution was used as a base line solution. Results are shown in Table III.
Final Percent Closure Polymer Conduc-Retained Temp Breaker Pressure Cone tivity Conduc-Fluid of Ibs/1000 si Ibs/1000 Darc tivitv gal. gal 2% KCI 125 0 2000 - 216 -A 125 2.5 (Tot.) 2000 159 130 60 B 125 3.0 (Tot.) 2000 188 106 49 Static fluid coefficients for fluida according to the invention were determined utilizing own in Table IV.
standard fluid loss coefficient procedures.
Results are sh TAE?~LE IV
Fluid Temp. Permeabilii:y Cw Spurt (Ibs/1000 of and ft/mini/2)a1/100 ft2) gal) 15 100 0.76 0.0017 1.82 15 125 0.77 0.0018 0.15 15 150 0.73 0.0023 5.17 20 100 0.77 0.0014 0.0 20 125 0.80 0.0016 0.0 20 150 0.71 0.0013 0.0 20 175 0.80 0.0032 0.0 These results clearly demonstrate the suitability of the low concentration borate crosslinked guar solution, buffered according to the invention, for use as a fracturing fluid.
2I ~~ 950 56.347 In the manner described, supra, a fracturing fluid was prepared containing, per 1000 gallons, 10 pounds of guar, 1.5 pounds of boric acid, and 5 pounds each of sodium bicarbonate and sodium carbonate. Viscosity of solution at 90 of was 170 sec-1 with greater than 100 cp. This further experiment demonstrates the ability of the borate-buffer combination to crosslink very reduced concE;ntrations of galactomannan gum.
(a) an aqueous hydrated, gum;
(b) a buffering agent in an amount sufficient to provide a controlled alkaline pH, of between 9 and 11 the buffering agent being effective at the crosslinking pH of the fluid;
(c) a metal ion source capable of furnishing metal ions in solution for crosslinking said gum;
(d) the well treating fluid having reduced concentration levels of gum of about 10 to about 32 pounds of gum per 1000 gallons of well treating fluid;
(e) wherein the fluid is effective to delay release of metal ions and facilitates a sufficiently elevated concentration o1' metal ions at the crosslinking pH to facilitate effective use of the fluid at subterrane<ur temperatures.
ammonium carbonates, potassium carbonates, sodium carbonates, bicarbonate, sesquicarbonate, and sesquicarbonate.
(a) forming a well treating fluid according to any of claims 1 to 13;
(b) providing a propping agent;.
(c) pumping the well treating fluid and the propping agent downhole in concentrations effective to provide an alkaline pH during pumping; and (d) facilitating the reaction of said metal releasing agent with said gum to provide a crosslinked gum in the formation.
of from about 9.0 to about 12.
(a) an aqueous hydrated galactomannan gum thickening agent;
(b) a buffering agents in an amount sufficient to provide the fluid with a pH of from about. 9.0 to 12; and (c) a metal ion source capable of furnishing metal ions in solution for crosslinking the hydrated galactomannan gum thickening agent, wherein the hydrated metal-crosslinked galactomannan gum thickening agent is present in the fluid at a concentration of from about 10 to about 25 pounds per 1,000 gallons of the fluid.
Priority Applications (2)
|Application Number||Priority Date||Filing Date||Title|
|US08283129 US5681796A (en)||1994-07-29||1994-07-29||Borate crosslinked fracturing fluid and method|
|Publication Number||Publication Date|
|CA2154950A1 true CA2154950A1 (en)||1996-01-30|
|CA2154950C true CA2154950C (en)||2003-04-08|
Family Applications (1)
|Application Number||Title||Priority Date||Filing Date|
|CA 2154950 Expired - Fee Related CA2154950C (en)||1994-07-29||1995-07-28||Borate crosslinked fracturing fluid and method|
Country Status (3)
|US (3)||US5681796A (en)|
|CA (1)||CA2154950C (en)|
|GB (1)||GB2291907B (en)|
Families Citing this family (55)
|Publication number||Priority date||Publication date||Assignee||Title|
|US6649572B2 (en) *||1997-05-27||2003-11-18||B J Services Company||Polymer expansion for oil and gas recovery|
|WO1998054272A1 (en) *||1997-05-27||1998-12-03||Bj Services Company||Improved polymer expansion for oil and gas recovery|
|US6302209B1 (en)||1997-09-10||2001-10-16||Bj Services Company||Surfactant compositions and uses therefor|
|US6024170A (en) *||1998-06-03||2000-02-15||Halliburton Energy Services, Inc.||Methods of treating subterranean formation using borate cross-linking compositions|
|US6230805B1 (en)||1999-01-29||2001-05-15||Schlumberger Technology Corporation||Methods of hydraulic fracturing|
|CA2451334C (en)||2001-06-22||2008-09-09||Jeffrey C. Dawson||Fracturing fluids and methods of making and using same|
|US6617285B2 (en)||2001-07-03||2003-09-09||Baker Hughes Incorporated||Polyols for breaking of borate crosslinked fracturing fluid|
|US6810959B1 (en) *||2002-03-22||2004-11-02||Bj Services Company, U.S.A.||Low residue well treatment fluids and methods of use|
|WO2004007894A3 (en) *||2002-07-11||2004-05-13||Marc A Chalmers||Apparatus and method for accelerating hydration of particulate polymer|
|US7741251B2 (en)||2002-09-06||2010-06-22||Halliburton Energy Services, Inc.||Compositions and methods of stabilizing subterranean formations containing reactive shales|
|US8251141B2 (en)||2003-05-16||2012-08-28||Halliburton Energy Services, Inc.||Methods useful for controlling fluid loss during sand control operations|
|US8962535B2 (en)||2003-05-16||2015-02-24||Halliburton Energy Services, Inc.||Methods of diverting chelating agents in subterranean treatments|
|US8091638B2 (en)||2003-05-16||2012-01-10||Halliburton Energy Services, Inc.||Methods useful for controlling fluid loss in subterranean formations|
|US8278250B2 (en)||2003-05-16||2012-10-02||Halliburton Energy Services, Inc.||Methods useful for diverting aqueous fluids in subterranean operations|
|US8181703B2 (en)||2003-05-16||2012-05-22||Halliburton Energy Services, Inc.||Method useful for controlling fluid loss in subterranean formations|
|US8631869B2 (en)||2003-05-16||2014-01-21||Leopoldo Sierra||Methods useful for controlling fluid loss in subterranean treatments|
|US7759292B2 (en)||2003-05-16||2010-07-20||Halliburton Energy Services, Inc.||Methods and compositions for reducing the production of water and stimulating hydrocarbon production from a subterranean formation|
|US7306039B2 (en) *||2003-08-13||2007-12-11||Bj Services Company||Methods of using crosslinkable compositions|
|US7082995B2 (en) *||2004-03-05||2006-08-01||Halliburton Energy Services, Inc.||Methods and compositions for reducing the viscosity of treatment fluids|
|US20060019836A1 (en) *||2004-06-02||2006-01-26||Fang Li||Multicomponent viscoelastic surfactant fluid and method of using as a fracturing fluid|
|US8895480B2 (en)||2004-06-04||2014-11-25||Baker Hughes Incorporated||Method of fracturing using guar-based well treating fluid|
|US7405183B2 (en) *||2004-07-02||2008-07-29||Halliburton Energy Services, Inc.||Methods and compositions for crosslinking polymers with boronic acids|
|US7687441B2 (en) *||2004-10-25||2010-03-30||Halliburton Energy Services, Inc.||Boronic acid networking agents and associated methods|
|US7345013B2 (en) *||2005-02-23||2008-03-18||Schlumberger Technology Corporation||Polymer Crosslinking System Comprising Soluble Zr(IV), Carbonate and Bicarbonate Ions|
|WO2007130440A3 (en) *||2006-05-05||2008-01-03||C Edward Baxter||Improved fracturing fluids for use in oil and gas recovery operations|
|US7730950B2 (en)||2007-01-19||2010-06-08||Halliburton Energy Services, Inc.||Methods for treating intervals of a subterranean formation having variable permeability|
|US7934557B2 (en)||2007-02-15||2011-05-03||Halliburton Energy Services, Inc.||Methods of completing wells for controlling water and particulate production|
|US8697610B2 (en) *||2007-05-11||2014-04-15||Schlumberger Technology Corporation||Well treatment with complexed metal crosslinkers|
|US8853135B2 (en) *||2008-05-07||2014-10-07||Schlumberger Technology Corporation||Method for treating wellbore in a subterranean formation with high density brines and complexed metal crosslinkers|
|US20090077931A1 (en) *||2007-09-20||2009-03-26||Jacqueline Westfield||Method of indicating divergent product benefits|
|WO2009059160A1 (en) *||2007-11-02||2009-05-07||E. I. Du Pont De Nemours And Company||High temperature aqueous-based zirconium fracturing fluid and use|
|US20090253594A1 (en)||2008-04-04||2009-10-08||Halliburton Energy Services, Inc.||Methods for placement of sealant in subterranean intervals|
|US9534167B2 (en)||2008-10-21||2017-01-03||Baker Hughes Incorporated||Fracturing method using polyboronic compound|
|US8173580B2 (en)||2008-10-21||2012-05-08||Baker Hughes Incorporated||Boron crosslinkers for fracturing fluids with appreciably lower polymer loading|
|US8420577B2 (en) *||2008-10-21||2013-04-16||Baker Hughes Incorporated||Methods of making polyboronic compounds and compositions related thereto|
|US8389763B2 (en) *||2008-10-21||2013-03-05||Bj Services Company||Methods of making polyboronic compounds and compositions related thereto|
|US8276667B2 (en) *||2008-12-03||2012-10-02||Schlumberger Technology Corporation||Delayed breaking of well treatment fluids|
|US9102855B2 (en) *||2008-12-18||2015-08-11||Schlumberger Technology Corporation||Removal of crystallinity in guar based materials and related methods of hydration and subterranean applications|
|US7998910B2 (en)||2009-02-24||2011-08-16||Halliburton Energy Services, Inc.||Treatment fluids comprising relative permeability modifiers and methods of use|
|GB2481773B (en) *||2009-07-09||2012-04-18||Titan Global Oil Services Inc||Compositions and processes for fracturing subterranean formations|
|US8030250B2 (en) *||2009-07-17||2011-10-04||Baker Hughes Incorporated||Method of treating subterranean formations with carboxylated guar derivatives|
|US8420576B2 (en)||2009-08-10||2013-04-16||Halliburton Energy Services, Inc.||Hydrophobically and cationically modified relative permeability modifiers and associated methods|
|US20110092696A1 (en) *||2009-10-21||2011-04-21||PfP Technology, LLC.||High performance low residue guar for hydraulic fracturing and other applications|
|US9194223B2 (en)||2009-12-18||2015-11-24||Baker Hughes Incorporated||Method of fracturing subterranean formations with crosslinked fluid|
|US8371383B2 (en) *||2009-12-18||2013-02-12||Baker Hughes Incorporated||Method of fracturing subterranean formations with crosslinked fluid|
|US8215397B2 (en) *||2009-12-30||2012-07-10||Schlumberger Technology Corporation||System and method of dynamic underbalanced perforating using an isolation fluid|
|EP2625243A1 (en)||2010-10-07||2013-08-14||Akzo Nobel Chemicals International B.V.||Low residue formation fracturing|
|US8921597B2 (en)||2011-06-06||2014-12-30||Baker Hughes Incorporated||Preparation of boron crosslinking agents for fracturing fluids|
|US20140196904A1 (en) *||2013-01-15||2014-07-17||Halliburton Energy Services, Inc.||Methods of Controlled Release pH Adjustment for Oilwell Stimulation|
|US20140262296A1 (en) *||2013-03-15||2014-09-18||Tucc Technology, Llc||Methods, Systems, and Compositions for the Controlled Crosslinking of Well Servicing Fluids|
|US20140364343A1 (en) *||2013-06-11||2014-12-11||Chemplex Advanced Materials, Llc||Produced Water Borate Crosslinking Compositions and Method of Use|
|WO2015009612A1 (en) *||2013-07-15||2015-01-22||Schlumberger Canada Limited||Fluid viscosity control|
|US20170355900A1 (en) *||2014-11-30||2017-12-14||Solvay Usa Inc.||Produced water borate crosslinking compositions and method of use|
|EP3184601A1 (en)||2015-12-23||2017-06-28||Agrana Beteiligungs- Aktiengesellschaft||Process fluid comprising environmentally compatible bio-stabilizers|
|WO2017135943A1 (en) *||2016-02-03||2017-08-10||Halliburton Energy Services, Inc.||In situ generation of ph control agents|
Family Cites Families (41)
|Publication number||Priority date||Publication date||Assignee||Title|
|US3079332A (en) *||1957-07-23||1963-02-26||Atlantic Refining Co||Method and composition for reducing fluid loss|
|US3202214A (en) *||1960-04-18||1965-08-24||Halliburton Co||Preparation and use of sodium silicate gels|
|US3208524A (en) *||1960-09-26||1965-09-28||Exxon Production Research Co||Process for controlling lost circulation|
|US3215634A (en) *||1962-10-16||1965-11-02||Jersey Prod Res Co||Method for stabilizing viscous liquids|
|US3346556A (en) *||1965-10-14||1967-10-10||Marine Colloids Inc||Treatment of manno galactan gums|
|US3411580A (en) *||1966-09-28||1968-11-19||Byron Jackson Inc||Mud removal method|
|US3766984A (en) *||1968-05-20||1973-10-23||Dow Chemical Co||Method for temporarily sealing a permeable formation|
|US3625286A (en) *||1970-06-01||1971-12-07||Atlantic Richfield Co||Well-cementing method using a spacer composition|
|US3740360A (en) *||1970-11-12||1973-06-19||Dow Chemical Co||Sealing composition and method|
|US4033415A (en) *||1973-03-30||1977-07-05||Halliburton Company||Methods for fracturing well formations|
|US3898165A (en) *||1972-04-18||1975-08-05||Halliburton Co||Compositions for fracturing high temperature well formations|
|US3974077A (en) *||1974-09-19||1976-08-10||The Dow Chemical Company||Fracturing subterranean formation|
|US4624868A (en) *||1979-12-17||1986-11-25||Colgate-Palmolive Company||Borated polysaccharide absorbents and absorbent products|
|US4514309A (en) *||1982-12-27||1985-04-30||Hughes Tool Company||Cross-linking system for water based well fracturing fluids|
|US4579670A (en) *||1984-03-26||1986-04-01||Big Three Industries, Inc.||Control of crosslinking reaction rate of aqueous fracturing fluids|
|US4619776A (en) *||1985-07-02||1986-10-28||Texas United Chemical Corp.||Crosslinked fracturing fluids|
|US4801389A (en) *||1987-08-03||1989-01-31||Dowell Schlumberger Incorporated||High temperature guar-based fracturing fluid|
|US5145590A (en) *||1990-01-16||1992-09-08||Bj Services Company||Method for improving the high temperature gel stability of borated galactomannans|
|US5082579A (en) *||1990-01-16||1992-01-21||Bj Services Company||Method and composition for delaying the gellation of borated galactomannans|
|US5160643A (en) *||1990-01-16||1992-11-03||Bj Services Company||Method for delaying the gellation of borated galactomannans with a delay additive such as glyoxal|
|US5036919A (en) *||1990-02-05||1991-08-06||Dowell Schlumberger Incorporated||Fracturing with multiple fluids to improve fracture conductivity|
|US4969526A (en) *||1990-02-05||1990-11-13||Dowell Schlumberger Incorporated||Non-interfering breaker system for delayed crosslinked fracturing fluids at low temperature|
|US4997487A (en) *||1990-03-07||1991-03-05||Halliburton Company||High temperature set retarded well cement compositions and methods|
|US5103905A (en) *||1990-05-03||1992-04-14||Dowell Schlumberger Incorporated||Method of optimizing the conductivity of a propped fractured formation|
|US5103913A (en) *||1990-12-12||1992-04-14||Dowell Schlumberger Incorporated||Method of fracturing high temperature wells and fracturing fluid therefore|
|US5252239A (en) *||1991-04-15||1993-10-12||General Motors Corporation||ER fluids having chemically defoliated vermiculite treated with an alkyl ammonium halide and methods of making and using the same|
|US5252235A (en)||1991-05-24||1993-10-12||Zirconium Technology Corporation||Borate cross-linking solutions|
|US5160445A (en) *||1991-05-24||1992-11-03||Zirconium Technology Corporation||Borate cross-linking solutions|
|US5266224A (en)||1991-05-24||1993-11-30||Zirconium Technology Corporation||Borate cross-linking solutions|
|US5252234A (en)||1991-05-24||1993-10-12||Zirconium Technology Corporation||Borate cross-linking solutions|
|US5252236A (en)||1991-05-24||1993-10-12||Zirconium Technology Corporation||Borate cross-linking solutions|
|US5165479A (en)||1991-07-22||1992-11-24||Halliburton Services||Method for stimulating subterranean formations|
|US5211859A (en) *||1991-11-26||1993-05-18||The Western Company Of North America||Low pH fracturing compositions|
|US5259455A (en) *||1992-05-18||1993-11-09||Nimerick Kenneth H||Method of using borate crosslinked fracturing fluid having increased temperature range|
|EP0594363A1 (en) *||1992-10-20||1994-04-27||Halliburton Company||Borate crosslinked fracturing fluids|
|US5372732A (en) *||1992-10-21||1994-12-13||Halliburton Company||Delayed release borate crosslinking agent|
|US5271466A (en) *||1992-10-30||1993-12-21||Halliburton Company||Subterranean formation treating with dual delayed crosslinking gelled fluids|
|US5330005A (en) *||1993-04-05||1994-07-19||Dowell Schlumberger Incorporated||Control of particulate flowback in subterranean wells|
|US5445223A (en) *||1994-03-15||1995-08-29||Dowell, A Division Of Schlumberger Technology Corporation||Delayed borate crosslinked fracturing fluid having increased temperature range|
|US5460226A (en) *||1994-05-18||1995-10-24||Shell Oil Company||Formation fracturing|
|US5393439A (en) *||1994-06-27||1995-02-28||Halliburton Company||Periodate fracturing fluid viscosity breakers|
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|US4686052A (en)||Stabilized fracture fluid and crosslinker therefor|
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