CA2513547A1 - Invertible well bore servicing fluid - Google Patents

Invertible well bore servicing fluid Download PDF

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Publication number
CA2513547A1
CA2513547A1 CA002513547A CA2513547A CA2513547A1 CA 2513547 A1 CA2513547 A1 CA 2513547A1 CA 002513547 A CA002513547 A CA 002513547A CA 2513547 A CA2513547 A CA 2513547A CA 2513547 A1 CA2513547 A1 CA 2513547A1
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CA
Canada
Prior art keywords
fluid
acid
invert emulsion
oil
emulsifier
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Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Abandoned
Application number
CA002513547A
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French (fr)
Inventor
Carl J. Thaemlitz
Robert S. Taylor
Ryan M. Foster
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Halliburton Energy Services Inc
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Halliburton Energy Services, Inc.
Carl J. Thaemlitz
Robert S. Taylor
Ryan M. Foster
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Application filed by Halliburton Energy Services, Inc., Carl J. Thaemlitz, Robert S. Taylor, Ryan M. Foster filed Critical Halliburton Energy Services, Inc.
Publication of CA2513547A1 publication Critical patent/CA2513547A1/en
Abandoned legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K8/00Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
    • C09K8/02Well-drilling compositions
    • C09K8/32Non-aqueous well-drilling compositions, e.g. oil-based
    • C09K8/36Water-in-oil emulsions
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K8/00Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
    • C09K8/02Well-drilling compositions
    • C09K8/04Aqueous well-drilling compositions
    • C09K8/26Oil-in-water emulsions

Abstract

An invert emulsion fluid, method for making same, and method for using same as a servicing fluid in a well bore. The invert emulsion fluid contains an oleaginous fluid, a non-~oleaginous fluid, and an emulsifier comprising one or more amines generally represented by the formula: wherein R is a cycloaliphatic hydrocarbon, each R' may be the same or different and is H or an alkyl having from about 1 to about 3 carbon atoms, each A may be the same or different and is NH or 0, and the sum of x and y ranges from about 1 to about 20. In a preferred embodiment, R is a radical selected from the group consisting of abietyl, dihydroabietyl, tetrahydroabietyl, and dehydroabietyl, R' is H, and A is 0.

Description

INVERTIBLE WELL BORE SERVICING FLUID
FIELD OF THE INVENTION
This invention generally relates to well bore servicing fluids. More specifically, the invention relates to an invertible well bore servicing fluid containing an amine emulsifier that allows the fluid to be reversibly converted from a water-in-oil emulsion to an oil-in-water emulsion upon contact with an acid.
BACKGROUND OF THE INVENTION
Well cementing is a process used in penetrating subterranean formations that produce oil and gas. In well cementing, a well bore is drilled while a drilling fluid is circulated through the well bore. The circulation of the drilling fluid is then terminated, and a string of pipe, e.g., casing, is run in the well bore. The drilling fluid in the well bore is conditioned by circulating it downwardly through the interior of the pipe and upwardly through the annulus, which is located between the exterior of the pipe and the walls of the well bore. Next, primary cementing is typically performed whereby a slurry of cement in water is placed in the annulus and permitted to set into a hard mass to thereby attach the string of pipe to the walls of the well bore and seal the annulus. By sealing the annulus, migration of reservoir fluids from one zone to another through the annulus is prevented.
'Various types of drilling fluids, also known as drilling muds, have been employed in the well cementing process. Oil-based drilling fluids have several advantages compared to water-based drilling fluids such as superior hole stability, especially in shale formations, and excellent lubrication properties. These lubrication properties permit the drilling of well bores having a significant vertical deviation, as is typical of off shore or deep water drilling operations. When a water-based drilling fluid is used to drill a highly deviated well bore, the torque and drag on the casing can undesirably cause the casing that lies against the low side .of the well bore to stick. In contrast, oil-based fluids form a thin, slick filter cake that helps prevent the casing from sticking.
Oil-based drilling fluids typically contain some water, making them water-in-oil type emulsions, also known as invert emulsions. The water may arise in the drilling fluid itself or from the well bore, or it may be intentionally added to affect the properties of the drilling fluid. The invert emulsion commonly contains both water-soluble and oil-soluble emulsifiers (i.e., emulsifying agents or surfactants}
to stabilize the invert emulsion. Examples of traditional emulsifiers employed in the invert emulsion include polyvalent metal soaps, phosphate esters, fatty acids, and fatty acid soaps. Typically, these emulsifiers impart oil wetting properties to the drilling fluids.
The use of traditional emulsifiers in drilling fluids can complicate the clean up process in open hole completion operations. In particular, oil-based solvents containing surfactants are used to penetrate the filter cake and reverse the wetability of the filter cake particles, thereby converting the oil-wet solids of the filter cake to water-wet solids. Water-wet solids in the filter cake are required so that a subsequent acid wash'' can be used to destroy or remove the particles. Acid usually cannot be placed in direct contact with a traditional invert emulsion. Otherwise, the direct acid contact would lead to the addition of the acid to the invert emulsion's internal aqueous phase, resulting in a significant increase in the viscosity of the invert emulsion. Cleaning the well bore in this staged manner can be time consuming. Unfortunately, the longer the time required to clean the well bore, the more likely the well bore is to become unstable and collapse.
If this occurs, the well bore will have to be re-drilled or opened up before production can occur. Thus, there is a tradeoff between increased production due to a fully cleaned-up well bore and the potential of collapse of the well bore due to instability.
To avoid risking the collapse of the well bore, drilling fluids containing, for example, ethoxylated soya amine emulsifiers, have been developed that provide for a faster clean up of the well bore. Such drilling fluids can be reversibly converted from a water-in-oil type emulsion (i.e., invert emulsion) to an oil-in water type emulsion that can be easily broken down with an acid soak solution. The invert emulsion is converted to an oil-in-water emulsion by mixing it with an aqueous acid solution that protonates the emulsion. If the subterranean formation produces crude oil, the aqueous acid solution commonly contains a strongly anionic sulfonate surfactant to prevent the formation of aqueous acid solution-crude oil emulsions in the well bore and crude oil sludging therein. However, it has been discovered that due to the presence of the anionic sulfonate surfactant, the emulsifier becomes water insoluble such that the emulsion remains as a water-in-oil emulsion. Further, the aqueous acid solution adds to the internal water phase, resulting in a significant increase in the viscosity of the invert emulsion. The high viscosity emulsion can undesirably seal off the subterranean formation, irreversibly damaging the formation and making oil production impossible.
As such, there continues to be a need for oil-based fluids with improved acid additive compatibility that can be quickly and easily converted from invert emulsions to oil-in-water emulsions without being concerned their viscosity might increase.
Using such oil-based fluids would ensure that the subterranean formation penetrated by the well bore does not become plugged. The present invention utilizes an oil-based fluid that may be inverted in a timely manner without risking damage to the formation and that is compatible with typical sulfonate acidizing additives.
SUMMARY OF THE INVENTION
The present invention includes an invert emulsion fluid that may be used to service a well bore. Typical applications include a drilling fluid, a completion fluid, a work-over fluid, a gravel packing fluid, a formation fracturing fluid, a stimulating fluid, and a packer fluid, all of which are known in the art. The invert emulsion fluid contains an oleaginous fluid, a non-oleaginous fluid, and an emulsifier comprising one or more amines generally represented by the formula:
(CH2CHR'A)XH
R-N
(CH2CHR'A)yH
wherein R is a cycloaliphatic hydrocarbon, each R' may be the same or different and is H or an alkyl having from about 1 to about 3 carbon atoms, each A may be the same or different and is NH or O, and the sum of x and y ranges from about 1 to about 20. In a preferred embodiment, R is a radical selected from the group consisting of abietyl, hydroabietyl, dihydroabietyl, tetrahydroabietyl, and dehydroabietyl, R' is H, and A is O. In yet a more preferred embodiment, the emulsifier comprises non-ethoxylated Rosin Amine D
and from about 1 to about 12 molar equivalents of ethoxylated Rosin Amine D relative to the non-ethoxylated Rosin Amine D. The presence of the emulsifier renders the invert emulsion fluid capable of being reversibly converted from an invert emulsion to an oil-in-water emulsion upon contact with an effective amount of an acid. The acid protonates the amine, thereby increasing the water solubility of the emulsion. Further, the oil-based fluid is capable of being converted from an oil-in-water emulsion back to an invert emulsion upon contact with an effective amount of a base.
The present invention further includes a method for using an invert emulsion fluid in a well bore. In this method, the invert emulsion fluid described above is placed in a well bore for servicing the well bore. After using the invert emulsion fluid, an acid solution is introduced to the invert emulsion fluid to reversibly convert the invert emulsion to an oil-in-water emulsion. The emulsion undergoes inversion even if an anionic sulfonate surfactant fox preventing crude oil sludging is present in the acid solution. The resulting oil-in-water emulsion has a lower viscosity and thus will not damage the subterranean formation by plugging the formation. Further, the oil-in water emulsion wets the subterranean formation, allowing for increased production. In addition, the oil-in-water emulsion can be easily removed from the well bore to prepare for subsequent processes, such as cementing and stimulation.
DETAILED DESCRIPTION OF THE PREFERRED EMBODllVIENTS
According to the present invention, an invert emulsion fluid for use in a well bore can be readily and reversibly converted to an oil-in-water emulsion by increasing the hydrogen ion concentration of the fluid. The hydrogen ion concentration may be increased by contacting the fluid with an effective amount of an acid to cause its conversion. One or more amine emulsifiers present in the fluid are protonated by the hydrogen ions. The resulting protonated amine has a cationic charge that increases its water and acid solubility. As a result, the fluid now favors a water external emulsion state. In addition, the fluid can be converted from an oil-in-water emulsion back to an invert emulsion by contacting the fluid with an effective amount of a base for deprotonation of the amine emulsifiers. Examples of suitable bases are those that would increase the hydroxyl ion concentration of the fluid, e.g., hydroxides, including those of sodium (caustic soda), calcium (lime or slaked lime), potassium (caustic potash), and magnesium.
The invert emulsion fluid includes an oleaginous fluid, a non-oleaginous fluid, and an emulsifier comprising one or more amines generally represented by the formula:
(CH2CHR'A)XH
l R-N

(CH2CHR'A)yH
wherein R is a cycloaliphatic hydrocarbon, each R' may be the same or different and is H or an alkyl having from about 1 to about 3 carbon atoms, each A may be the same or different and is NH or O, and the sum of x and y ranges from about 1 to about 20. In a preferred embodiment, R is a radical selected from the group consisting of abietyl, hydroabietyl, dihydroabietyl, tetrahydroabietyl, and dehydroabietyl, R' is H, and A is O. In other preferred embodiments, the one or more amines are ethoxylated rosin amines. The term "rosin amine"
is defined as the primary amines derived from various rosins or rosin acids, whereby the carboxyl of the rosin or rosin acid is converted to an amino (-NH2) group.
Examples of suitable rosin amines include: gum and wood rosin amines primarily containing abietyl; rosin amine derived from hydrogenated gum or wood rosin and primarily containing dehydroabietylamine, rosin amine derived from hydrogenated gum or wood rosin and primarily containing dihydro- and tetrahydroabietylamine; heat treated rosin amine derived from heat treated rosin; polymerized rosin amine derived from polymerized rosin; isomerized rosin amine derived from isomerized rosin and containing substantial amounts of abietylamine; and the rosin amines derived from pure rosin acids, e.g., abietylamine, dihydroabietylamine, dehydroabietylamine, and tetrahydroabietylamine.
As used in this specification, the abietyl, hydroabietyl, and dehydroabietyl amine radicals are referred to with the intention that they be considered broadly as covering rosin materials containing those radicals as major constitutents. As such, the products derived from rosin are considered to have the abietyl radical as the major constituent, the products derived from hydrogenated rosin are considered to have the hydroabietyl radicals as the major constituent and dehydrogenated rosin is considered to have dehydroabietyl as the major constituent. It is to be understood, however, that a specific rosin amine may include minor amounts of each of the various rosin amines.
A detailed description of the preparation of ethoxylated rosin amines is presented in U.S. Patent No. 2,510,284, which is incorporated by reference herein in its entirety. The preparation of ethoxylated rosin amines involves first producing either monoethanol rosin amine or diethanol rosin amine in the absence of a catalyst. The ethanol rosin amines are thereafter further reacted with ethylene oxide to increase the ethylene oxide content of the ethoxylated rosin amines.

In more preferred embodiments, the invert emulsion fluid contains an emulsifier that comprises from about 0 to about 25 weight (wt.) % non-ethoxylated Rosin Amine D (RAD) "
and from about 75 to about 100 wt. % ethoxylated RAD, based on the total weight of the invert emulsion fluid. As used throughout the specification, the symbol "%"
represents the term "percent". Rosin Amine D contains a mixture of primary amines derived from modified rosin, with its major constituent being dehydroabietyl amine, which has a condensed ring structure bonded to one nitrogen atom. RAD may be alkoxylated via ethoxylation on the nitrogen atom by reacting it with, e.g., from about 1 to about 11 moles of ethylene oxide, preferably from about 2 to about 6 moles of ethylene oxide. Examples of suitable commercially available RAD include the POLYRA.D products, which are commercially available from Hercules Inc. under various tradenames, e.g., POLYRAD OSOOTM, POLYR.AD
0515, POLYRA.D 1100, and POLYRAD 1110TH. By way of example, POLYR.AD
11 lOTM is composed of 90 wt. % RAD ethoxylated with 11 moles of ethylene oxide and 10 wt. % non-ethoxylated RAD. Examples of other suitable commercially available ethoxylated rosin amines include the Witco RAD products, such as Witco RAD 515 and Witco RAD
1100, which may be purchased from Akzo Nobel Inc.
Any known oleaginous fluid may be used to form the external oil phase of the invert emulsion fluid. The oleaginous fluid preferably comprises any petroleum oil, natural oil, synthetically derived oil, or combinations thereof. More preferably, the oleaginous fluid comprises at least one of an alpha olefin, an internal olefin, an ester, a diester of carbonic acid, a paraflln, kerosene oil, diesel oil, and mineral oil. In addition, any known non-oleaginous fluid may be used to form the internal phase of the invert emulsion fluid. The non-oleaginous fluid is preferably an aqueous fluid, more preferably tap or fresh water; sea water; naturally-occurnng brine; a chloride-based, bromide-based, or ~ormate-based brine containing monovalent and/or polyvalent cations; or combinations thereof.
Examples of chloride-based brines include sodium chloride and calcium chloride. Examples of bromide-based brines include sodium bromide, calcium bromide, and zinc bromide.
Examples of formate-based brines include sodium formate, potassium formate, and cesium formate.
The invert emulsion fluid is a well bore servicing fluid, i.e., a fluid used to drill, complete, work over, or in any way service a well bore. For example, the invert emulsion fluid may serve as a drilling fluid, a completion fluid, a work-over fluid, a gravel packing fluid, a formation fracturing fluid, a stimulating fluid, or a packer fluid.
Other types of fluids _7-for which the invert emulsion fluid may be used would be apparent to one skilled in the art.
The concentration of each component in the invert emulsion fluid depends upon the intended use of the invert emulsion fluid.
If the intended use of the invert emulsion fluid is as a gravel packing fluid, a completion fluid, or a work-over fluid, the amount of emulsifier present in the fluid preferably ranges from about 0.1 volume (vol.) % to about 10 vol. % based on the total volume of the fluid, more preferably from about 0.5 vol. % to about 5.0 vol.
%, and most preferably from about 0.8 vol. % to about 4 vol. %. The emulsifier in the invert emulsion fluid preferably contains a 75:25 wt. % ratio of the ethoxylated Rosin Amine D
relative to the non-ethoxylated Rosin Amine D, more preferably a 85:15 wt.% ratio, and most preferably a 98:2 wt.% ratio. Further, the amount of oleaginous fluid present in the invert emulsion fluid preferably ranges from about 15 vol. % to about 85 vol. % based on the volume of the liquid fraction of the invert emulsion fluid, more preferably from about 30 vol. % to about 70 vol.
%, and most preferably from about 40 vol. % to about 60 vol. %. In addition, the amount of non-oleaginous fluid present in the invert emulsion fluid preferably ranges from about 85 vol.
to about 15 vol. % based on the volume of the liquid fraction of the invert emulsion fluid, more preferably from about 70 vol. % to about 30 vol. %, and most preferably from about 60 vol. % to about 40 vol. %.
If the intended use of the invert emulsion fluid is as a drilling fluid, the amount of emulsifier present in the fluid preferably ranges from about 0.2 vol. % to about 8.0 vol. %.
based on the total volume of the fluid, more preferably from about 0.5 vol. %
to about 5.0 vol. %, and most preferably from about 0.1 vol. % to about 4.0 vol. %. The emulsifier in the invert emulsion fluid preferably contains a 75:25 wt. % ratio of the ethoxylated Rosin Amine D relative to the non-ethoxylated Rosin Amine D, more preferably a 85:15 wt.%
ratio, and most preferably a 98:2 wt.% ratio. Further, the amount of oleaginous fluid present in the invert emulsion fluid preferably ranges from about 1 vol. % to about 50 vol. %
based on the volume of the invert emulsion fluid, more preferably from about 2 vol. % to about 50 vol. %, and most preferably from about 5 vol. °/ to about 45 vol. %. In addition, the amount of non-oleaginous fluid present in the invert emulsion fluid preferably ranges from about 50 vol.
to about 1 vol. % based on the volume of the invert emulsion fluid, more preferably from about 50 vol. % to about 2 vol. %, and most preferably from about 45 vol. % to about 5 vol.
%.

- g -The invert emulsion fluid of the present invention may also include one or more additional emulsifiers such as a polyaminated fatty acid, a diethanolamide of a fatty acid, an imidazoline, a phosphate ester, a phosphonate ester, a fatty acid, a dimer fatty acid, polymeric fatty acids, and combinations thereof. A suitable polyaminated fatty acid is commercially available from Halliburton Inc. under the tradename LE SUPERMUL. A suitable diethanolamide of a fatty acid is commercially available from Akzo Nobel Ine.
under the tradename Witcamide S 11. The amount of additional emulsifier present in the invert emulsion fluid preferably ranges from about 0.0 vol. % to about 3 vol. % based on the total volume of the invert emulsion fluid, more preferably from about 0.1 vol. % to about 2 vol. %, and most preferably from about 0.2 vol. % to about 1 vol. %. The additional emulsifier improves the oil-wetting properties of the invert emulsion fluid.
The invert emulsion fluid may further include additional additives as deemed appropriate by one skilled in the art. It is preferred that any additional materials do not interfere with the reversibility of the fluid. For example, wetting agents, organophilic clays, viscosiflers, weighting agents, bridging agents, and fluid loss control agents may be added to the invert emulsion fluid to obtain certain properties.
The steps used to prepare the invert emulsion fluid for use in the well bore would be apparent to one skilled in the art. For example, a desired quantity of the oleaginous fluid may be mixed with a suitable amount of the amine emulsifier, followed by sequentially adding the remaining components with continuous mixing. The resulting mixture is then vigorously agitated while adding the oleaginous fluid. The emulsifer lowers the interfacial tension between the oleaginous fluid and the non-oleaginous fluid, enabling the non-oleaginous fluid to form a stable dispersion of fine droplets in the oleaginous fluid.
Otherwise, the high interfacial tension between the oleaginous fluid and the non-oleaginous fluid would cause the two fluids to spontaneously separate when the agitation ceases.
The present invention also includes a method for using the previously described invert emulsion fluid in a well bore. The method comprises placing the invert emulsion fluid in a well bore and contacting the invert emulsion fluid with an acid solution to reversibly convert the invert emulsion to an oil-in-water emulsion. Before contacting the invert emulsion fluid with an acid solution, the invert emulsion fluid is employed to service the well bore as mentioned previously. The particular steps used to service the well bore depend upon the type of servicing performed and would be apparent to one skilled in the art.
Furthermore, the oil-in-water emulsion may be converted back to an invert emulsion by contact with a base solution.
The acid solution comprises water and an acid, e.g., an inorganic acid such as hydrochloric acid, an organic acid such as acetic acid, formic acid, or glycolic acid, or combinations thereof. The strength of the acid solution should be su~cient to protonate the amine emulsifier. Preferably, about one molar equivalent of acid per one molar equivalent of the ethyoxylated Rosin Amine D is added to the invert emulsion fluid. In preferred embodiments, the acid is hydrochloric acid that is present in the acid solution in an amount ranging from about 1 wt. % to about 36 wt. % based on the weight of the water, more preferably from about 10 wt. % to about 15 wt. %.
The acid solution may also contain an anionic sulfonate surfactant for preventing the formation of aqueous acid solution-crude oil emulsions and crude oil sludging.
The anionic sulfonate surfactant may be selected from the group of linear or branched alkylbenzyl sulfonates such as linear or branched dodecylbenzenesulfonate or dodecylbenzenesulfonic acid, alkyl diphenyloxide disulfonates, and alpha-olefin sulfonates and sulfosuccinates: Of these, linear dodecylbenzenesulfonic acid is preferred. The anionic sulfonate surfactant is present in the aqueous acid solution in an amount preferably ranging from about 0.1 wt. % to about 1.5 wt. % based on the weight of the water, more preferably from about 0.4 wt. % to about 0.8 wt. %.
The base solution comprises water and a base, e.g., LiOH, NaOH, KOH, RbOH, Ca(OH)2, Sr(OH)Z, Ba(OH)a, or combinations thereof. The strength of the base solution should be suffcient to deprotonate the amine emulsifier, while the quantity of the base solution depends upon the amount of deprotonation that needs to be accomplished.
Well bore clean-up is much easier and quicker to carry out using the invert emulsion fluid of the present invention. A filter cake forms when the invert emulsion fluid comes into contact with a producing formation. Instead of washing the well bore with a detergent solution prior to acid washing, the use of the invert emulsion fluid allows the well bore to be washed using only the acid solution. The acid solution is injected into the well bore to protonate the amine surfactant, thereby converting the fluid on the filter cake from a water-in-oil emulsion to an oil-in-water emulsion. In particular, the addition of the acid solution causes the oleaginous fluid to change from the continuous phase to the discontinuous phase and the non-oleaginous fluid to change from the discontinuous phase to the continuous phase.

The discontinuous phase, also known as the dispersed phase, forms a stable dispersion of fine droplets throughout the continuous phase. As a result of the conversion, the oil-wet particles of the filter cake become water-wet, allowing the acid to readily reach and dissolve the acid soluble particles in the filter cake. Thus, the well bore can be cleaned mare effectively and rapidly using the invert emulsion fluid of the present invention as opposed to conventional well bore servicing fluids.
The invert emulsion fluid readily undergoes conversion from a water-in-oil emulsion to an oil-in-water emulsion despite the presence of the anionic sulfonate surfactant. The resulting oil-in-water emulsion has a relatively low viscosity. Thus, the oil-in-water emulsion is less likely to plug the subterranean formation and thus minimizes damage to the formation.
When the fluid is to be used as a formation fracturing fluid, the fluid may further comprise a gelling agent. The gelling agent preferably includes a fernc iron or aluminum polyvalent metal salt of a phosphoric acid ester, a proppant material, and an effective amount of a delayed gel breaker to break a gel formed by the gelling agent and the oleaginous fluid. The phosphoric acid ester utilized in the gelling agent generally has the formula:
O
R- P-O-R' OH
wherein R is an alkyl group having from about 8 to about 24 carbon atoms and R' is an alkyl group having from about 1 to about 4 carbon atoms. The phosphoric acid ester is preferably decane phosphoric acid mono methyl ester. The fernc iron or aluminum polyvalent metal salt of the phosphoric acid ester is present in the invert emulsion fluid in an amount ranging from about 0.1 wt. % to about 2.5 wt. % based on the weight of the oleaginous fluid, more preferably from about 0.2 wt. % to about 1 wt. %. The proppant material is present in the invert emulsion fluid in an amount ranging from about 1 to about 14 pounds of proppant material per gallon of oleaginous fluid. The delayed gel breaker, which is dissolved in the aqueous phase of the invert emulsion fluid, is present in the fluid in an amount ranging from about 0.01 wt. % to about 3 wt. % by weight of the oleaginous fluid, more preferably from about 0.05 wt. % to about 1 wt. %.

The invert emulsion fluid may be employed as a fracturing fluid by pumping it through a well bore into a subterranean formation to be stimulated. The fluid is pumped at a rate and pressure such that one or more fractures are formed and extended in the subterranean formation. The proppant material suspended in the fluid is deposited in the fractures when the gel is broken and returned to the surface. The proppant material remains in the fractures and functions to prevent the fractures from closing whereby conductive channels are formed through which produced fluids can readily flow from the subterranean formation into the well bore.
Proppant materials that may be used in the invert emulsion fluid are known in the art.
Examples of poppant materials include graded sand, resin coated sand, sintered bauxite, various particulate ceramic materials, and glass beads. The particular size of the proppant material employed depends on the particular formation being fractured and other variables.
Generally, the proppant particle sizes are in the range of from about 2 to about 200 mesh on the U.S. Sieve Series scale. The delayed gel breakers may be any suitable breaker for causing the gelled fluid to revert to a thin fluid after the fractures are formed in the subterranean formation. The gel breakers are preferably materials that are slowly soluble in water. The breaking of the gel does not take place until the gel breakers are dissolved in the water. Examples of slowly soluble breakers are given in U.S. Patent No.
5,846,915, which is incorporated by reference herein. A preferred gel breaker is hard burned magnesium oxide having a particle size that will pass through a 200 mesh Tyler screen. Hard burned magnesium oxide is commercially available from Clearwater Inc. of Pittsburgh, Pennsylvania. The hard burned magnesium oxide and other similar breakers are not immediately present for breaking the gel due to their slowly soluble nature.
Other breakers such as alkali metal carbonates, alkali metal bicarbonates, alkali metal acetates, other alkaline earth metal oxides, alkali metal hydroxides, amines, and weak acids can be encapsulated with slowly water soluble or other similar encapsulating materials. Such encapsulating materials are known to those skilled in the art and function to delay the breaking of the gelled fluid for a required period of time. Examples of suitable encapsulating materials include precipitated silicay elastomers, polyvinylidene chloride (PVDC), nylon, waxes, polyurethanes, and cross-linked partially hydrolyzed acrylics. When an alkaline breaker, e.g., magnesium oxide, is utilized, the acid group of the phosphonic acid ester in the gelling agent is neutralized, resulting in an initial increase in the viscosity of the gelled hydrocarbon liquid after which the gel is broken.
Another type of breaker that can be utilized when the gelling agent is a ferric iron polyvalent metal salt of the phosphoric acid ester is a reducing agent that reduces ferric iron to ferrous iron. Ferric iron is capable of forming a viscous coordination complex with a phosphoric acid ester, and the complex can be disassociated by reducing the fernc iron to the ferrous state. The disassociation causes the gelled hydrocarbon liquid to break. Examples of suitable reducing agents include but are not limited to stannous chloride, thioglycolic acid (2-mercaptoacetic acid), hydrazine sulfate, sodium diethyldithiocarbamate, sodium dimethyldithiocarbamate, sodium hypophosphite, potassium iodide, hydroxylamine hydrochloride, thioglycol (2-mercaptoethanol), ascorbic acid, sodium thiosulfate, sodium dithionite, and sodium sulfite. Of these, the preferred reducing agents for use at a temperature of about 90 °C are stannous chloride, thioglycolic acid, hydrazine sulfate, sodium diethyldithiocarbamate, and sodium dimethyldithiocarbamate. The most preferred reducing agent is thioglycolic acid, which may be delayed by salt formation or encapsulation.
The reducing agent may also be delayed by encapsulating it with a slowly water soluble or other similar encapsulating material.
In contrast to phosphoric acid esters utilized in conventional fracturing fluids, the phosphoric acid esters present in the invert emulsion fluid do not suffer from the problem that they decompose in refinery distillation towers to form volatile phosphorus which condenses on the trays of the distillation towers and cause plugging. In particular, the phosphoric acid esters of the present invention have much higher thermal stability and consequently do not as readily decompose or disassociate. Thus, their use minimizes the formation of volatile phosphorus in refinery distillation towers.
Additional disclosure related to the gelling agent described above can be found in Patent Application No. 09/792,165, entitled "Methods and Compositions for Treating Subterranean Formations with Gelled Hydrocarbon Fluids", which is incorporated by reference herein in its entirety.
EXAMPLES
The invention having been generally described, the following examples are given as particular embodiments of the invention and to demonstrate the practice and advantages hereof. It is understood that the examples are given by way of illustration and are not intended to limit the specification or the claims to follow in any manner.
An invert emulsion fluid to be used as a completion fluid was prepared in accordance with the present invention. That is, I34 mL of HDF-2000 (i.e., mineral oil commercially available from Total Solvants) was combined with 12.6 mL of Witco RAD 515 (i.e., an amine emulsifier commercially available from Akzo Nobel Inc.) and stirred on a Hamilton Beach mixer. Then 210 mL of sodium bromide brine having a density of 12.3 lblgal was added to the resulting solution while stirring. Next, 4 mL of Witcamide 511 (i. e., an emulsifier commercially available from Akzo Nobel Tnc.) was added to the solution, followed by stirring the resulting mixture for about five minutes. The resulting fluid appeared as a white emulsion and had a density of about 10.1 lb/gal. Using a Fann electrical stability meter, i.e., a standard in the petroleum industry, the electrical stability of the fluid was found to be 80 volts at ambient temperature, which is indicative of the existence of a water-in-oil emulsion.
While stirnng, the above fluid was treated with 15 wt.% hydrochloric acid (0.4 ml).
Within seconds, the fluid appeared to convert to an oil-in-water emulsion.
This conversion was confirmed by measuring the electrical stability of the fluid, which was 0.0 volts. The electrically conductive property of the fluid is proof that the fluid had been inverted and became water external.
The ail-in-water emulsion was then stirred while being treated with 36 wt.%
sodium hydroxide solution (1.0 mL). ). Within a few seconds the oil-in-water emulsion converted back into a water-in-oil emulsion. After stirring for approximately five minutes, the electrical stability of the fluid was measured to be 20 volts at ambient temperature, indicating that the fluid had been converted back to a water-in-oil emulsion.
The rheological properties of the resulting fluid were measured at 120 °F using the Fann 35A viscometer.
The electrical stability at 120 °F was 21 volts, and the 600 rpm and 300 rpm Fann viscometer dial readings in degrees were 131 and 80, respectively.
While the preferred embodiments of the invention have been shown and described, modifications thereof can be made by one skilled in the art without departing from the spirit and teachings of the invention. The embodiments described herein are exemplary only, and are not intended to be limiting. Many variations and modifications of the invention disclosed herein are possible and are within the scope of the invention. Use of the term "optionally"

with respect to any element of a claim is intended to mean that the subject element is required, or alternatively, is not required. Both alternatives are intended to be within the scope of the claim.
Accordingly, the scope of protection is not limited by the description set out above, but is only limited by the claims which follow, that scope including all equivalents of the subject matter of the claims. Each and every claim is incorporated into the specification as an embodiment of the present invention. Thus the claims are a further description and are an addition to the preferred embodiments of the present invention. The discussion of a reference in the Description of Related Art is not an admission that it is prior art to the present invention, especially any reference that may have a publication date after the priority date of this application. The disclosures of all patents, patent applications, and publications cited herein are hereby incorporated by reference, to the extent that they provide exemplary, procedural or other details supplementary to those set forth herein.

Claims (33)

1. A method far using an invert emulsion fluid in a well bore, comprising:
(a) placing an invert emulsion fluid in a well bore, wherein the invert emulsion fluid comprises:
(i) an oleaginous fluid;
(ii) a non-oleaginous fluid; and (iii) an emulsifier comprising one or more amines generally represented by the formula:

wherein R is a cycloaliphatic hydrocarbon, each R' may be the same or different and is H or an alkyl having from about 1 to about 3 carbon atoms, each A may be the same or different and is NH or O, and the sum of x and y ranges from about to about 20; and (b) contacting the invert emulsion fluid with an acid solution to reversibly convert the invert emulsion to an oil-in-water emulsion.
2. The method of claim 1 wherein R is a radical selected from the group consisting of abietyl, hydroabietyl, dihydroabietyl, tetrahydroabietyl, and dehydroabietyl, R' is H, and A is O.
3. The method of claim 1 wherein the emulsifier comprises non-ethoxylated Rosin Amine D and from about 1 to about 12 molar equivalents of ethoxylated Rosin Amine D
relative to the non-ethoxylated Rosin Amine D.
4. The method of claim 3 wherein the ethoxylated Rosin Amine D is formed by reacting Rosin Amine D with from about 5 to about 11 moles of ethylene oxide.
5. The method of claim 1 wherein the invert emulsion fluid is a well bore servicing fluid selected from a group consisting of a drilling fluid, a completion fluid, a work-over fluid, a gravel packing fluid, a formation fracturing fluid, and a stimulating fluid.
6. The method of claim 5 wherein an amount of emulsifier present in the gravel packing fluid, the completion fluid, and the work-over fluid ranges from about 0.1 volume % to about 10.0 volume % based on a total volume of the fluid.
7. The method of claim 5 wherein an amount of emulsifier present in the drilling fluid ranges from about 0.2 volume % to about 8.0 volume % based on a total volume of the fluid.
8. The method of claim 1 wherein the oleaginous fluid is selected from a group consisting of an alpha olefin, an internal olefin, an ester, a diester of carbonic acid, a paraffin, kerosene oil, diesel oil, mineral oil, and combinations thereof.
9. The method of claim 1 wherein the non-oleaginous fluid is selected from a group consisting of fresh water, sea water, naturally-occurring brine, a chloride-based brine, a bromide-based brine, a formate-based brine, and combinations thereof.
10. The method of claim 1 wherein the invert emulsion fluid further comprises an additional emulsifier.
11. The method of claim 9 wherein the additional emulsifier is selected from a group consisting of a polyaminated fatty acid, a diethanolamide of a fatty acid, a phosphate ester, a phosphonate ester, a fatty acid, a dimer fatty acid, polymeric fatty acids, and combinations thereof.
12. The method of claim 1 wherein the invert emulsion fluid further comprises:
a gelling agent comprising a ferric iron or aluminum polyvalent metal salt of a phosphonic acid ester, the phosphonic acid ester being generally represented by the formula:

wherein R is an alkyl group having from about 8 to about 24 carbon atoms and R1 is an alkyl group having from about 1 to about 4 carbon atoms;
a proppant material; and an effective amount of a delayed gel breaker to break a gel formed by the gelling agent and the oleaginous fluid.
13. The method of claim 12 wherein the phosphonic acid ester is decane phosphoric acid mono methyl ester.
14. The method of claim 12 wherein the delayed gel breaker is selected from a group consisting of amines, weak acids, and alkaline earth metal oxides including magnesium oxide, alkali metal carbonates, alkali metal bicarbonates, alkali metal acetates, and alkali metal hydroxides.
15. The method of claim 12 wherein the polyvalent metal salt is ferric iron and the delayed gel breaker is a reducing agent that reduces ferric iron to ferrous iron.
16. The method of claim 15 wherein the reducing agent is selected from a group consisting of stannous chloride, thioglycolic acid and its salts, hydrazine sulfate, sodium diethyldithiocarbamate, sodium dimethyldithiocarbamate, sodium hypophosphite, hydroxylamine hydrochloride, thioglycol, ascorbic acid and its salts, sodium thiosulfate, and sodium sulfite.
17. The method of claim 1 wherein the acid solution comprises an anionic sulfonate surfactant for preventing crude ail sludging.
18. The method of claim 1, further comprising contacting the oil-in-water emulsion with a base solution to reversibly convert the oil-in-water emulsion to an invert emulstion.
19. A fluid for use in a well bore, comprising:
(a) an oleaginous fluid;
(b) a non-oleaginous fluid; and (c) an emulsifier comprising one or more amines generally represented by the formula:

wherein R is a cycloaliphatic hydrocarbon, each R' may be the same or different and is H or an alkyl having from about 1 to about 3 carbon atoms, each A may be the same or different and is NH or O, and the sum of x and y ranges from about 1 to about 20, and wherein the fluid is capable of being reversibly converted from an invert emulsion to an oil-in-water emulsion upon contact with an effective amount of an acid.
20. The fluid of claim 19 wherein R is a radical selected from a group consisting of abietyl, dihydroabietyl, tetrahydroabietyl, and dehydroabietyl, R' is H, and A
is O.
21. The fluid of claim 19 wherein the emulsifier comprises non-ethoxylated Rosin Amine D and from about 1 to about 12 molar equivalents of ethoxylated Rosin Amine D
relative to the non-ethoxylated Rosin Amine D.
22. The fluid of claim 19 wherein the fluid is a well bore servicing fluid selected from a group consisting of a drilling fluid, a completion fluid, a work-over fluid, a gravel packing fluid, a formation fracturing fluid, and a stimulating fluid.
23. The fluid of claim 22 wherein an amount of emulsifier present in the gravel packing fluid, the completion fluid, and the work-over fluid ranges from about 0.1 volume % to about 10.0 volume % based on a total volume of the fluid.
24. The fluid of claim 22 wherein an amount of emulsifier present in the drilling fluid ranges from about 0.2 volume % to about 8.0 volume % based on a total volume of the fluid.
25. The fluid of claim 19, further comprising an additional emulsifier.
26. The fluid of claim 25 wherein the additional emulsifier is selected from a group consisting of a polyaminated fatty acid, a diethanolamide of a fatty acid, a phosphate ester, a phosphonate ester, a fatty acid, a dimer fatty acid, a polymeric fatty acid, and combinations thereof.
27. The fluid of claim 19, further comprising:
a gelling agent comprising a ferric iron or aluminum polyvalent metal salt of a phosphoric acid ester, the phosphonic acid ester being generally represented by the formula:

wherein R is an alkyl group having from about 8 to about 24 carbon atoms and R' is an alkyl group having from about 1 to about 4 carbon atoms;
a proppant material; and an effective amount of a delayed gel breaker to break a gel formed by the gelling agent and the oleaginous fluid.
28. The fluid of claim 27 wherein the phosphoric acid ester is decane phosphoric acid mono methyl ester.
29. The fluid of claim 27 wherein the delayed gel breaker is selected from a group consisting of amines, weak acids, and alkaline earth metal oxides including magnesium oxide, alkali metal carbonates, alkali metal bicarbonates, alkali metal acetates, and alkali metal hydroxides.
30. The fluid of claim 27 wherein the polyvalent metal salt is ferric iron and the delayed gel breaker is a reducing agent that reduces ferric iron to ferrous iron.
31. The fluid of claim 27 wherein the reducing agent is selected from a group consisting of stannous chloride, thioglycolic acid and its salts, hydrazine sulfate, sodium diethyldithiocarbamate, sodium dimethyldithiocarbamate, sodium hypophosphite, hydroxylamine hydrochloride, thioglycol, ascorbic acid and its salts, sodium thiosulfate, and sodium sulfite.
32. The fluid of claim 19 wherein the fluid is capable of being converted from the oil-in-water emulsion back to the invert emulsion upon contact with an effective amount of a base.
33. A method for making a fluid for use in a wellbore, comprising admixing:
(a) an oleaginous fluid;
(b) a non-oleaginous fluid; and (c) an emulsifier comprising one or more amines generally represented by the formula:

wherein R is a cycloaliphatic hydrocarbon, each R' may be the same or different and is H or an alkyl having from about 1 to about 3 carbon atoms, each A may be the same or different and is NH or O, and the sum of x and y ranges from about 1 to about 20, and wherein the fluid is capable of being reversibly converted from an invert emulsion to an oil-in-water emulsion upon contact with an effective amount of an acid.
CA002513547A 2003-01-24 2004-01-08 Invertible well bore servicing fluid Abandoned CA2513547A1 (en)

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Families Citing this family (63)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6806233B2 (en) * 1996-08-02 2004-10-19 M-I Llc Methods of using reversible phase oil based drilling fluid
US6544934B2 (en) * 2001-02-23 2003-04-08 Halliburton Energy Services, Inc. Methods and compositions for treating subterranean formations with gelled hydrocarbon fluids
US7125826B2 (en) * 2001-09-14 2006-10-24 Halliburton Energy Services, Inc. Methods of using invertible oil external-water internal fluids in subterranean applications
EP1783188A1 (en) * 2003-01-24 2007-05-09 Halliburton Energy Services, Inc. Invertible well bore servicing fluid field of the invention
US7152697B2 (en) * 2003-02-03 2006-12-26 M-I Llc Delayed phase changing agent for invert emulsion drilling fluid
US7534745B2 (en) * 2004-05-05 2009-05-19 Halliburton Energy Services, Inc. Gelled invert emulsion compositions comprising polyvalent metal salts of an organophosphonic acid ester or an organophosphinic acid and methods of use and manufacture
US7709421B2 (en) * 2004-09-03 2010-05-04 Baker Hughes Incorporated Microemulsions to convert OBM filter cakes to WBM filter cakes having filtration control
WO2006029019A2 (en) * 2004-09-03 2006-03-16 Baker Hughes Incorporated Method of removing an invert emulsion filter cake after the drilling process using a single phase microemulsion
US8091644B2 (en) * 2004-09-03 2012-01-10 Baker Hughes Incorporated Microemulsion or in-situ microemulsion for releasing stuck pipe
US20060223714A1 (en) * 2005-04-05 2006-10-05 M-L L.L.C. Invert emulsion based completion and displacement fluid and method of use
US8105989B2 (en) 2005-04-05 2012-01-31 M-I L.L.C. Water based completion and displacement fluid and method of use
US7334639B2 (en) * 2005-09-30 2008-02-26 M-I Llc In-situ solidification of invert emulsion fluids to form gas tight annular barrier
US7754661B2 (en) * 2006-11-28 2010-07-13 Innovative Chemical Technologies Canada Ltd Recycling of oil-based drilling muds
US7350575B1 (en) * 2007-01-11 2008-04-01 Halliburton Energy Services, Inc. Methods of servicing a wellbore with compositions comprising Sorel cements and oil based fluids
US7763572B2 (en) * 2007-01-11 2010-07-27 Halliburton Energy Services, Inc. Compositions comprising quaternary material and sorel cements
US7431086B2 (en) * 2007-01-11 2008-10-07 Halliburton Energy Services, Inc. Methods of servicing a wellbore with compositions comprising quaternary material and sorel cements
US7893011B2 (en) * 2007-01-11 2011-02-22 Halliburton Energy Services Inc. Compositions comprising Sorel cements and oil based fluids
DK2102130T3 (en) * 2007-01-11 2015-05-04 Halliburton Energy Services Inc Compositions comprising sorrel cements and oil-based fluids, and methods for treating a borehole therewith
US20080169103A1 (en) * 2007-01-12 2008-07-17 Carbajal David L Surfactant Wash Treatment Fluids and Associated Methods
US8220548B2 (en) * 2007-01-12 2012-07-17 Halliburton Energy Services Inc. Surfactant wash treatment fluids and associated methods
CA2677840C (en) 2007-02-19 2015-11-24 M-I L.L.C. Breaker and displacement fluid and method of use
US20080217012A1 (en) * 2007-03-08 2008-09-11 Bj Services Company Gelled emulsions and methods of using the same
MX2009009750A (en) * 2007-03-13 2009-11-10 Mi Llc Shale hydration inhibition agent and method of use.
US8871695B2 (en) * 2007-04-25 2014-10-28 Baker Hughes Incorporated In situ microemulsions used as spacer fluids
US8091646B2 (en) * 2007-07-03 2012-01-10 Baker Hughes Incorporated Single phase microemulsions and in situ microemulsions for cleaning formation damage
US8210263B2 (en) 2007-07-03 2012-07-03 Baker Hughes Incorporated Method for changing the wettability of rock formations
US7975764B2 (en) * 2007-09-26 2011-07-12 Schlumberger Technology Corporation Emulsion system for sand consolidation
US8415279B2 (en) * 2008-04-22 2013-04-09 Baker Hughes Incorporated Microemulsions used as spacer fluids
US7617872B1 (en) * 2008-05-09 2009-11-17 Schlumberger Technology Corporation System and method for perforated well sand control
US7906464B2 (en) 2008-05-13 2011-03-15 Halliburton Energy Services, Inc. Compositions and methods for the removal of oil-based filtercakes
AU2009281690B2 (en) * 2008-08-11 2015-02-12 M-I Australia Pty Ltd Compositions and methods for inhibiting emulsion formation in hydrocarbon bodies
CN102131888A (en) * 2008-08-29 2011-07-20 Pt绿科印度尼西亚公司 Composition of specifically formulated phosphate salts, used for increasing density of completion fluids, and as a hi -temperature and easy to use completion fluids in the oil and gas industry
US20110160099A1 (en) * 2008-09-11 2011-06-30 M-I L.L.C. Invert emulsion wellbore fluids and method for reducing toxicity thereof
US7833943B2 (en) 2008-09-26 2010-11-16 Halliburton Energy Services Inc. Microemulsifiers and methods of making and using same
US20100243242A1 (en) * 2009-03-27 2010-09-30 Boney Curtis L Method for completing tight oil and gas reservoirs
WO2010148226A2 (en) * 2009-06-17 2010-12-23 M-I L.L.C. Application of degradable fibers in invert emulsion fluids for fluid loss control
US20110036582A1 (en) * 2009-08-14 2011-02-17 Ladva Hemant K Solid incorporated reversible emulsion for a fracturing fluid
US9004167B2 (en) * 2009-09-22 2015-04-14 M-I L.L.C. Methods of using invert emulsion fluids with high internal phase concentration
US8853136B2 (en) * 2009-10-14 2014-10-07 Basf Se Process for tertiary mineral oil production using surfactant mixtures
CA2774183A1 (en) * 2009-10-16 2011-04-21 Exxonmobil Upstream Research Company Hydrocarbon recovery operations fluids and methods for using the same
AU2014240322B2 (en) * 2009-11-26 2015-09-17 M-I Australia Pty Ltd Compositions and methods for inhibiting naphthenate solids formation from liquid hydrocarbons
EP2504407B1 (en) * 2009-11-26 2015-03-25 M-I Australia Pty Ltd Compositions and methods for inhibiting naphthenate solids formation from liquid hydrocarbons
US20110186293A1 (en) * 2010-02-01 2011-08-04 Gurmen M Nihat Use of reactive solids and fibers in wellbore clean-out and stimulation applications
MX348072B (en) 2010-06-30 2017-05-25 M-I L L C * Breaker and displacement fluid.
US8720562B2 (en) 2010-10-19 2014-05-13 Halliburton Energy Services, Inc. Wellbore cementing compositions and methods of making and using same
US9045675B2 (en) 2011-02-15 2015-06-02 Schlumberger Technology Corporation Non-aqueous, acid soluble, high-density completion fluids and process
US20130000900A1 (en) * 2011-07-01 2013-01-03 Halliburton Energy Services, Inc. Down-hole placement of water-swellable polymers
US9115304B2 (en) 2012-04-09 2015-08-25 Halliburton Energy Services, Inc. Wellbore servicing fluid system and methods of use
US20140106992A1 (en) * 2012-10-15 2014-04-17 Halliburton Energy Services, Inc. Invert emulsion with encapsulated breaker for well treatment
US9890321B2 (en) 2012-10-22 2018-02-13 Halliburton Energy Services, Inc. Wellbore servicing compositions and methods of making and using same
MX369446B (en) * 2013-04-19 2019-11-08 Multi Chem Group Llc Treatment fluids comprising weakly emulsifying surfactants and associated methods.
WO2014176438A1 (en) * 2013-04-24 2014-10-30 Board Of Regents, The University Of Texas System Use of amines in recovery of active oils
US9328280B2 (en) 2013-05-08 2016-05-03 Chevron Phillips Chemical Company Lp Additives for oil-based drilling fluids
AU2013395635B2 (en) 2013-07-31 2017-04-13 Halliburton Energy Services, Inc. Wellbore servicing materials and methods of making and using same
EP3022272A4 (en) * 2013-09-11 2017-02-22 Halliburton Energy Services, Inc. Asphaltene-dissolving oil-external emulsion for acidization and methods of using the same
MY194304A (en) 2013-11-27 2022-11-27 Cabot Corp Methods to separate brine from invert emulsions used in drilling and completion fluids
US20170002252A1 (en) 2015-06-30 2017-01-05 Exxonmobil Chemical Patents Inc. Lubricant Compositions and Methods of Making and Using Same
US10844264B2 (en) 2015-06-30 2020-11-24 Exxonmobil Chemical Patents Inc. Lubricant compositions comprising diol functional groups and methods of making and using same
WO2017142557A1 (en) * 2016-02-19 2017-08-24 M-I L.L.C. Reversible oil-based mud
WO2017209734A1 (en) * 2016-05-31 2017-12-07 Halliburton Energy Services, Inc. Emulsified fluid system for fracturing application
WO2018200432A1 (en) * 2017-04-24 2018-11-01 Huntsman Petrochemical Llc Novel water-in-oil hydraulic fracturing fluid and method of using such
WO2020041114A1 (en) * 2018-08-21 2020-02-27 Arc Products, Inc. Converting invert emulsions to emulsions using polyvalent salts of polymeric weak acids
BR112023018385A2 (en) * 2021-03-10 2023-12-05 Schlumberger Technology Bv SYSTEMS AND METHODS FOR DISTRIBUTING DEGRADABLE POLYESTER DURING GRAVEL FILLING

Family Cites Families (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3125517A (en) * 1964-03-17 Chzchzoh
US2510284A (en) 1948-12-18 1950-06-06 Hercules Powder Co Ltd Ethylene oxide condensates of ethanol rosin amines
US4230586A (en) * 1978-08-07 1980-10-28 The Lubrizol Corporation Aqueous well-drilling fluids
US4663076A (en) * 1984-05-10 1987-05-05 Milchem Incorporated Invert emulsion drilling fluid comprising oligamide composition
US4816551A (en) 1985-11-19 1989-03-28 Mi Drilling Fluids Company Oil based drilling fluids
US4713183A (en) 1986-03-12 1987-12-15 Dresser Industries, Inc. Oil based drilling fluid reversion
US5254531A (en) * 1989-02-09 1993-10-19 Henkel Kommanditgesellschaft Auf Aktien Oleophilic basic amine compounds as an additive for invert drilling muds
US6218342B1 (en) * 1996-08-02 2001-04-17 M-I Llc Oil-based drilling fluid
US5888944A (en) 1996-08-02 1999-03-30 Mi L.L.C. Oil-based drilling fluid
US6806233B2 (en) * 1996-08-02 2004-10-19 M-I Llc Methods of using reversible phase oil based drilling fluid
US5916484A (en) * 1997-05-13 1999-06-29 Halliburton Energy Services, Inc. Metal corrosion inhibited organic acid compositions
AUPP536198A0 (en) 1998-08-20 1998-09-10 Hybrid Electronics Australia Pty Ltd Colour-correction of light-emitting diode pixel modules
US6511944B2 (en) * 2001-02-23 2003-01-28 Halliburton Energy Services, Inc. Methods and compositions for treating subterranean formations with gelled hydrocarbon fluids
US6544934B2 (en) * 2001-02-23 2003-04-08 Halliburton Energy Services, Inc. Methods and compositions for treating subterranean formations with gelled hydrocarbon fluids
US7125826B2 (en) * 2001-09-14 2006-10-24 Halliburton Energy Services, Inc. Methods of using invertible oil external-water internal fluids in subterranean applications
US6608006B2 (en) * 2001-09-14 2003-08-19 Halliburton Energy Services, Inc. Methods of drilling well bores using invertible oil external-water internal drilling fluids
EP1783188A1 (en) * 2003-01-24 2007-05-09 Halliburton Energy Services, Inc. Invertible well bore servicing fluid field of the invention

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US20040147404A1 (en) 2004-07-29
US7238646B2 (en) 2007-07-03
US6989354B2 (en) 2006-01-24
NO20053779L (en) 2005-08-24
AR042561A1 (en) 2005-06-29
EP1783188A1 (en) 2007-05-09
MXPA05007835A (en) 2005-10-18
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US20060079407A1 (en) 2006-04-13
EP1601740A1 (en) 2005-12-07

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