WO2017074301A1 - Use of solid surfactant composites in well cementing - Google Patents
Use of solid surfactant composites in well cementing Download PDFInfo
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- WO2017074301A1 WO2017074301A1 PCT/US2015/057380 US2015057380W WO2017074301A1 WO 2017074301 A1 WO2017074301 A1 WO 2017074301A1 US 2015057380 W US2015057380 W US 2015057380W WO 2017074301 A1 WO2017074301 A1 WO 2017074301A1
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- Prior art keywords
- solid
- surfactant
- fluid
- moles
- spacer fluid
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/40—Spacer compositions, e.g. compositions used to separate well-drilling from cementing masses
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- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B33/00—Sealing or packing boreholes or wells
- E21B33/10—Sealing or packing boreholes or wells in the borehole
- E21B33/13—Methods or devices for cementing, for plugging holes, crevices or the like
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- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B33/00—Sealing or packing boreholes or wells
- E21B33/10—Sealing or packing boreholes or wells in the borehole
- E21B33/13—Methods or devices for cementing, for plugging holes, crevices or the like
- E21B33/14—Methods or devices for cementing, for plugging holes, crevices or the like for cementing casings into boreholes
- E21B33/16—Methods or devices for cementing, for plugging holes, crevices or the like for cementing casings into boreholes using plugs for isolating cement charge; Plugs therefor
Definitions
- Embodiments relate well cementing operations and, more particularly, in certain embodiments, to use of solid surfactant composites in well cementing operations.
- cement compositions are commonly utilized.
- Cement compositions may be used in primary cementing operations whereby pipe strings, such as casing and liners, are cemented in wellbores.
- a cement composition may be pumped into an annulus between the exterior surface of the pipe string (e.g., casing, liner, etc.) disposed therein and the walls of the wellbore (or a larger conduit in the wellbore).
- the cement composition may set in the annular space, thereby forming an annular sheath of hardened, substantially impermeable material (i.e., a cement sheath) that may support and position the pipe string in the wellbore and may bond the exterior surface of the pipe string to the wellbore walls (or the larger conduit).
- a cement sheath may support and position the pipe string in the wellbore and may bond the exterior surface of the pipe string to the wellbore walls (or the larger conduit).
- the cement sheath surrounding the pipe string should function to prevent the migration of fluids in the annulus, as well as protect the pipe string from corrosion.
- Cement compositions may also be used in remedial cementing methods, such as in squeeze cementing for sealing voids in a pipe string, cement sheath, gravel pack, subterranean formation, and the like.
- Preparation of the wellbore for cementing operations may be important in achieving optimal zonal isolation.
- wellbores may be cleaned and prepared for the cement composition with a fluid train that precedes the cement composition and can include spacer fluids, flushes, water-based muds, and the like.
- Spacer fluids may be used in wellbore preparation for drilling fluid displacement before introduction of the cement composition.
- the spacer fluids may enhance solids removal while also separating the drilling fluid from a physically incompatible fluid, such as a cement composition.
- Spacer fluids may also be placed between different drilling fluids during drilling change outs or between a drilling fluid and completion brine.
- a liquid surfactant may be blended with the spacer fluid, for example, to allow the spacer fluid to be compatible with water- or oil-based drilling fluids. Inclusion of the liquid surfactant may enable the spacer fluid to achieve improved cleaning by removal of residual drilling fluid from the wellbore.
- the inclusion of liquids surfactants in the spacer fluids may serve the purpose of water-wetting surfaces in the wellbore, such as the wellbore wall and casing surfaces, resulting in better cement bonding.
- the use of liquid surfactants may be problematic. For example, liquid surfactants require the use of additional equipment on location to mix the spacer fluid and liquid surfactant properly, thus increasing the complexity of the well operation. Additionally, certain liquid surfactants may include one or more flammable components, thus increasing the expense associated with shipment, storage, and handling thereof.
- FIG. 1 is a schematic illustration of an example system for the preparation and delivery of a spacer fluid comprising a solid surfactant composite.
- FIG. 2 is a schematic illustration of an example in which a spacer fluid comprising a solid surfactant composite is used between a cement composition and a drilling fluid.
- FIG. 3 is a schematic illustration of the embodiment of FIG. 3 showing displacement of the drilling fluid.
- Embodiments relate well cementing operations and, more particularly, in certain embodiments, to use of solid surfactant composites in well cementing operations.
- the well cementing operations may include the use of the solid surfactant composites in spacer fluids used, for example, in well cementing operations.
- a solid surfactant composite may be dry blended with particulate solids, wherein the dry blend may be included in a spacer fluid.
- One of the many potential advantages to these methods and compositions is that the use of a solid surfactant composite instead of liquid surfactants may reduce and potentially eliminate the need for additional mixing equipment for the surfactant at the well site, thus simplifying preparation of the spacer fluid. Additionally, hazards associated with handling of certain liquid surfactants, which may be flammable, at the well site may also be eliminated with the use of a solid surfactant composite.
- a solid surfactant composite may include a water-wetting surfactant and a solid carrier.
- the solid surfactant composite may include a dispersant, a defoaming agent, or a combination thereof.
- the solid surfactant composite may have a wide variety of shapes and sizes of individual particles suitable for use in cementing applications.
- individual particles of the solid surfactant composite may have well- defined physical as well as irregular geometries, including the physical shape of platelets, shavings, fibers, flakes, ribbons, rods, strips, spheroids, hollow beads, toroids, pellets, tablets, or any other physical shape.
- the solid surfactant composite may have a particle size in the range of about 5 microns to about 1,500 microns and, alternatively, a particle size in the range of about 20 microns to about 500 microns. However, particle sizes outside these defined ranges also may be suitable for particular applications.
- any of a variety of water- wetting surfactants may be included in the solid surfactant composite that may be capable of water-wetting well surfaces, such as the wellbore wall and casing surface.
- the function that a particular surfactant may perform depends on a variety of factors. These factors may include, but are not limited to, the choice of the hydrophobic and hydrophilic portions and the relative amounts thereof and the presence of any cationic, ionic, non-ionic, amphoteric, or Zwitterionic groups.
- the water-wetting surfactant may be included in the solid surfactant composite in an amount, without limitation, of from about 5% to about 99.9% by weight of the solid surfactant composite.
- the water- wetting surfactant may be included in an amount of from about 5%, about 10%, about 20%, about 30%, about 40%, about 50%, about 60%, about 70%, about 80%, about 90%, or about 99.9% by weight of the solid surfactant composite.
- suitable water-wetting surfactants may include alcohol ethoxylates, alcohol ethoxysulfates, alkyl phenol ethoxylates (e.g., nonyl phenol ethoxylates), glycol ethers, and combinations thereof. Certain of the water-wetting surfactants may be used as water-soluble salts.
- the water-wetting surfactants may be selected from alkali metal, alkaline earth metal, ammonium, and alkanolammonium salts of alcohol ethoxylates, alcohol ethoxysulfates, and alkyl phenol ethoxylates.
- alkali metal alkaline earth metal
- ammonium alkanolammonium salts of alcohol ethoxylates
- alcohol ethoxysulfates alcohol ethoxysulfates
- alkyl phenol ethoxylates alkyl phenol ethoxylates
- suitable alcohol ethoxylates may include C 6 to C1 ⁇ 2 alcohols substituted with from about 2 moles to about 15 moles and, alternatively, from about 5 moles to about 12 moles of ethylene oxide.
- the C 6 to C15 alcohols may be linear or branched.
- suitable alcohol ethoxylates may include C 4 to Cs alcohols substituted with about 4 moles to about 8 moles of ethylene oxide, Cs to C 12 alcohols substituted with about 4 moles to about 8 moles of ethylene oxide, and C12 to Ci 4 alcohols substituted with about 10 moles to about 14 moles of ethylene oxide.
- suitable alcohol ethoxylates may include butanol, hexanol or pentanol substituted with 6 moles of ethylene oxide, nonyl, decyl alcohol, or dodecyl alcohol substituted with 6 moles of ethylene oxide, or docecyl alcohol, tridecyl alcohol, or tetradecyl alcohol substituted with 12 moles of ethylene oxide.
- suitable alcohol ethoxylates may include isodecyl alcohol substituted with 6 moles of ethylene oxide or isotridecyl alcohol substituted with 12 moles ethylene oxide. Combinations of suitable alcohol ethoxylates may also be used.
- suitable alcohol ethoxysulfates may include Cio to C1 ⁇ 2 alcohols substituted with about 2 moles to about 15 moles of ethylene oxide.
- the Cio to C1 ⁇ 2 alcohols may be linear or branched.
- Suitable Cio to C1 ⁇ 2 alcohol ethoxylates may include docecyl alcohol, tridecyl alcohol, or tetradecyl alcohol substituted with from 2 moles to about 15 moles and, alternatively from about 6 moles to about 12 moles of ethylene oxide.
- Additional examples of suitable alcohol ethoxylates may include ethoxylated dodecyl alcohol ammonium sulfate or ethoxylated tetradecyl ammonium sulfate. Combinations of suitable alcohol ethoxysulfates may also be used.
- suitable alkyl phenol ethoxylates may include an alkyl group with from 1 to 12 carbon atoms and, alternatively, from about 8 to 12 carbon atoms.
- the alkyl phenol ethoxylates may have from 2 moles to about 18 moles of ethylene oxide and, alternatively, from about 8 moles to about 12 moles of ethylene oxide.
- One example of a suitable alkyl phenol ethoxylate is nonyl phenol ethoxylate having from about 8 moles to about 12 moles of ethylene oxide and, alternatively, about 10 moles of ethylene oxide.
- suitable glycol ethers may include an alkyl ether of a mono-, di-, or triethylene glycol.
- the alkyl ether may include a Ci to Cs alkyl ether of a mono-, di-, or triethylene glycol.
- the glycol ether may include diethy!ene glycol methyl ether, dipropylene glycol methyl ether, 2-butoxy etnanol, ethers of a C 2 to Ce di ydric alkanol that comprise at least one Ci to C 6 alkyl group, mono ethers of dihydric alkanols, methoxypropanol, butoxyethanol, hexoxyethanol, isomers thereof, and combinations thereof.
- a suitable glycol ether may comprise ethylene glycol monobutyl ether.
- the glycol ethers may be used by themselves in the solid surfactant composite or as a co- surfactant with one or more of the additional water- wetting surfactants described herein.
- a glycol ether such as ethylene glycol monobutyl ether may be used as a co-surfactant (50% to 90% by weight) with an alcohol ethoxylates, such as butanol, hexanol or pentanol substituted with from 4 moles to about 8 moles and, alternatively, about 6 moles of ethylene oxide.
- the water- wetting surfactant may be disposed on a solid carrier.
- the solid carrier may include any of a variety of solid materials, such as diatomaceous earth, amorphous silica, starch, clay such as kaolin clay, and combinations thereof.
- the solid carrier may be included in the solid surfactant composite in an amount, without limitation, of from about 0.1% to about 95% by weight of the solid surfactant composite.
- the solid carrier may be included in an amount of from about 0.1%, about 10%, about 20%, about 30%, about 40%, about 50%, about 60%, about 70%, about 80%, about 90%, or about 95% by weight of the solid surfactant composite.
- One of ordinary skill in the art, with the benefit of this disclosure, should be able to select an appropriate solid carrier and concentration thereof for a particular application.
- the solid surfactant composite may include a dispersant.
- suitable dispersants may include any of a variety of commonly used cement dispersants, such as sulfonated dispersants; sulfonated polymer dispersants; naphthalene sulfonates; melamine sulfonates; sulfonated melamine formaldehyde condensate; sulfonated naphthalene formaldehyde condensate; sulfonate acetone formaldehyde condensate; ethoxylated poly aery lates; or combinations thereof.
- a suitable dispersant may include a naphthalene sulfonate condensed with from about 4 moles to about 8 moles and, alternatively, about 6 moles of formaldehyde.
- the dispersant may be included in the solid surfactant composite in an amount, without limitation, of from about 10% to about 90% by weight of the solid surfactant composite.
- the dispersant may be included in an amount of from about 10%, about 20%, about 30%, about 40%, about 50%, about 60%, about 70%, about 80%, or about 90% by weight of the solid surfactant composite.
- One of ordinary skill in the art, with the benefit of this disclosure, should be able to select an appropriate dispersant and concentration thereof for a particular application.
- the solid surfactant composite may include a defoaming agent.
- the defoaming agent may be include in the solid surfactant composite in addition to, or separate from, the dispersant.
- Suitable defoaming agents may include compounds used in well operations to prevent a well treatment fluid from foaming during mixing and pumping.
- suitable defoaming agents may include polyol compositions, siloxanes such as polydimethyl siloxane, acetylenic diols, and combinations thereof.
- the defoaming agent may be included in the solid surfactant composite in addition to, or separate from, the dispersant.
- the defoaming agent may be included in the solid surfactant composite in an amount, without limitation, of from about 0.1% to about 20% by weight of the solid surfactant composite.
- the defoaming agent may be included in an amount of from about 0.1 %, about 5%, about 10%, about 15%, or about 20% by weight of the solid surfactant composite.
- One of ordinary skill in the art, with the benefit of this disclosure, should be able to select an appropriate defoaming agent and concentration thereof for a particular application.
- a solid surfactant composite may comprise an alcohol ethoxylate, a solid carrier comprising amorphous silica, a dispersant, and a defoaming agent.
- the solid surfactant composite may comprise a Cs to C 12 alcohol substituted with about 4 moles to about 8 moles of ethylene oxide, amorphous silica, a sulfonated naphthalene formaldehyde condensate, and a siloxane.
- the solid surfactant composite may comprise isodecyl alcohol substituted with 6 moles of ethylene oxide, amorphous silica, naphthalene sulfonate condensed with 6 moles of formaldehyde, and a polydimethyl siloxane,
- a solid surfactant composite may comprise an alcohol ethoxylate, a solid carrier, a dispersant, and a defoaming agent.
- the solid surfactant composite may comprise a C 12 to C 14 alcohol substituted with about 10 moles to about 14 moles of ethylene oxide, amorphous silica, diatomaceous earth, a sulfonated naphthalene formaldehyde condensate, and a siloxane.
- the solid surfactant composite may comprise isotridecyl alcohol substituted with 12 moles ethylene oxide, amorphous silica, diatomaceous earth, naphthalene sulfonate condensed with 6 moles of formaldehyde, and a polydimethyl siloxane.
- the solid surfactant composite may be prepared by any suitable technique.
- the components e.g., water- wetting surfactant, solid carrier, dispersant, and/or defoaming agent
- This mixture may then be dried, such as by spray drying, to form a substantially dry solid product.
- the solid surfactant composite may be used in a spacer fluid.
- a spacer fluid may comprise the solid surfactant composite and a base fluid. When added to the base fluid, the water-wetting surfactant on the solid surfactant composite will generally dissolve, with resulting release of the water-wetting surfactant into the base fluid.
- the solid surfactant composite may be included in the spacer fluid in an amount sufficient for a particular application.
- the solid surfactant composite may be added to the spacer fluid in an amount in a range of from about 0.1 % to about 20% by weight of the spacer fluid and, alternatively, from about 1 % to about 5% by weight.
- the solid surfactant composite may be present in an amount of about 0.1 %, about 1%, about 2%, about 4%, about 6%, about 8%, about 10% ⁇ , about 15%, or about 20% by weight of the spacer fluid.
- the base fluid may be an oil-base fluid or aqueous-base fluid.
- aqueous-base fluids may comprise fresh water, salt water (e.g., water containing one or more dissolved salts), brine, seawater, or any combination thereof.
- suitable oil-base fluids may include water-in-oil emulsions.
- the base fluid may be used to prepare a spacer fluid that is not emulsified.
- the base fluid may be included in the spacer fluids in an amount in the range of from about 15% to about 99.9% by weight of the spacer fluid and, alternatively, from about 25% to about 85% by weight of the spacer fluid.
- the base fluid may be present in an amount of about 15%, about 20%, about 30%, about 40%, about 50%, about 60%, about 70%, about 80%, about 90%, about 99%, or about 99% ⁇ by weight of the spacer fluid.
- the spacer fluids generally should have a density suitable for a particular application as desired by those of ordinary skill in the art, with the benefit of this disclosure.
- the spacer fluids may have a density in the range of from about 4 pounds per gallon ("ppg") to about 24 ppg, in the range of about 4 ppg to about 17 ppg, or in the range of about 8 ppg to about 13 ppg.
- the spacer fluids may be foamed or unfoamed or comprise other means to reduce their densities known in the art, such as lightweight additives. Those of ordinary skill in the art, with the benefit of this disclosure, should recognize the appropriate density for a particular application.
- the spacer fluid may include a solid particulate additive.
- the solid particulate additive may be included in the spacer fluid as desired to perform a particular function.
- the solid particulate additive may be included in the spacer fluid to weight the fluid to a desired density, assist in well cleaning by abrasive action in the wellbore, and/or as a viscosifier.
- Suitable solid particulate additives may include, without limitation, weighting agents, vitrified shale, cement kiln dust, silica flour, bentonite, pumice, fly ash, and combinations thereof.
- Weighting agents are typically materials may be used to increase the density of a well treatment fluid, such as a spacer fluid, and may have a specific gravity of about 2 or higher (e.g. , about 2, about 4, etc.). Examples of weighting agents that may be used include, but are not limited to, hematite, hausmannite, barite, calcium carbonate, and combinations thereof.
- the solid particulate additive may be included in the spacer fluids in an amount in the range of from about 10% to about 84.9% by weight of the spacer fluid.
- the solid particulate additive may be present of about 10%, about 20%, about 30%, about 40%, about 50%, about 60%, about 70%, about 80%, or about 84.9 by weight of the spacer fluid.
- the solid particulate additive and the solid surfactant composite may be dry blended prior to combination with the base fluid to form the spacer fluid.
- This dry blend may be prepared offsite and then transported to the well site, for example, where it may be combined with the base fluid.
- preparation of the spacer fluid may be simplified as only one solid additive may need to be included in the spacer fluid.
- costs may be reduced as transporting of multiple individual solid additives may not be needed if all the solid additives for the spacer fluid are included in the dry blend.
- the dry blend may include the solid particulate additive (or additives) in an amount of from about 80% to about 99.9%, alternatively, from about 90% to about 99.9%, and alternatively, from about 95% to about 99% by weight of the dry blend.
- the dry blend may include the solid surfactant composite in an amount of from about 0.1% to about 20%, alternatively, from about 0.1% to about 10%, and alternatively, from about 1% to about 5% by weight of the dry blend.
- additives may be included in the spacer fluids as deemed appropriate by one skilled in the art, with the benefit of this disclosure.
- additional additives include, but are not limited to: viscosifying agents (e.g., clays, hydratable polymers, hydroxyl ethyl cellulose), fluid loss control additives, lost circulation materials, filtration control additives, dispersants, foaming additives, defoamers, corrosion inhibitors, scale inhibitors, and formation conditioning agents.
- viscosifying agents e.g., clays, hydratable polymers, hydroxyl ethyl cellulose
- fluid loss control additives e.g., lost circulation materials
- filtration control additives e.g., dispersants
- foaming additives e.g., defoamers
- corrosion inhibitors e.g., scale inhibitors, and formation conditioning agents.
- Suitable spacer fluids may be prepared in accordance with any suitable technique.
- the desired quantity of water may be introduced into a mixer (e.g., a cement blender) followed by the dry blend.
- the dry blend may comprise the solid surfactant component and the solid particulate additive, as described herein. Additional liquid additives, if any, may be added to the water as desired prior to, or after, combination with the dry blend. This mixture may be agitated for a sufficient period of time to form a pumpable slurry.
- pumps may be used for delivery of this pumpable slurry into the wellbore.
- the spacer fluid and/or the dry blend may be prepared at the well site or prepared offsite and then transported to the well site.
- the dry blend and/or spacer fluid may transported to the well site using any suitable mode of transportation, including, without limitation, a truck, railcar, barge, or the like.
- the spacer fluid and/or dry blend may be formulated at the well site, for example, where the components of the spacer fluid and/or dry blend may be delivered from a transport (e.g., a vehicle or pipeline) and then mixed prior to placement downhole.
- a transport e.g., a vehicle or pipeline
- other suitable techniques for preparing the spacer fluids may be used in accordance with embodiments of the present invention.
- the spacer fluid (as described herein) may be used for displacing a first fluid from a wellbore, the wellbore penetrating a subterranean formation.
- the method may comprise combining components comprising a solid surfactant composite, solid particulate additive, and/or a base fluid to provide a spacer fluid.
- One or more optional additives may also be included in the spacer fluid as discussed herein.
- the method may further comprise introducing the spacer fluid into the wellbore to displace at least a portion of the first fluid from the wellbore.
- the spacer fluid may displace the first fluid from a wellbore annulus, such as the annulus between a pipe string and the subterranean formation or between the pipe string and a larger conduit.
- the first fluid displaced by the spacer fluid may comprise a drilling fluid.
- the spacer fluid may be used to displace the drilling fluid from the wellbore.
- the spacer fluid may also remove the drilling fluid from the walls of the wellbore. Additional steps in the method may include, without limitation, introducing a pipe string into the wellbore, introducing a cement composition into the wellbore with the spacer fluid separating the cement composition and the first fluid.
- the spacer fluid may prevent the cement composition from contacting the first fluid, such as a drilling fluid.
- the spacer fluid may also remove the drilling fluid, dehydrated/gelled drilling fluid, and/or filter cake solids from the wellbore in advance of the cement composition. Removal of these compositions from the wellbore may enhance bonding of the cement composition to surfaces in the wellbore.
- the displaced drilling fluid may include, for example, any number of fluids, such as solid suspensions, mixtures, and emulsions.
- a non-limiting example of a suitable drilling fluid may comprise an oil-based drilling fluid.
- An example of a suitable oil-based drilling fluid comprises an invert emulsion.
- the oil-based drilling fluid may comprise an oleaginous fluid.
- oleaginous fluids examples include, but are not limited to, a-olefins, internal olefins, alkanes, aromatic solvents, cycloalkanes, liquefied petroleum gas, kerosene, diesel oils, crude oils, gas oils, fuel oils, paraffin oils, mineral oils, low-toxicity mineral oils, olefins, esters, amides, synthetic oils (e.g., polyolefins), polydiorganosiloxanes, siloxanes, organosiloxanes, ethers, dialkylcarbonates, hydrocarbons, and combinations thereof.
- a-olefins examples include, but are not limited to, a-olefins, internal olefins, alkanes, aromatic solvents, cycloalkanes, liquefied petroleum gas, kerosene, diesel oils, crude oils, gas oils, fuel oils, paraffin oils, mineral oils, low-toxicity mineral oils, olef
- the cement composition introduced into the wellbore may comprise hydraulic cement and water.
- hydraulic cements may be utilized in accordance with the present invention, including, but not limited to, those comprising calcium, aluminum, silicon, oxygen, iron, and/or sulfur, which set and harden by reaction with water.
- Suitable hydraulic cements include, but are not limited to, Portland cements, pozzolana cements, gypsum cements, high alumina content cements, slag cements, silica cements, and combinations thereof.
- the hydraulic cement may comprise a Portland cement.
- the Portland cements may include cements classified as Classes A, C, H, or G cements according to American Petroleum Institute, API Specification for Materials and Testing for Well Cements, API Specification 10, Fifth Ed., July 1 , 1990.
- the hydraulic cement may include cements classified as ASTM Type I, II, or III.
- the solid surfactant composite may be used in a wide variety of subterranean operations, including well cementing operations.
- An example method may comprise providing a solid surfactant composite comprising a water-wetting surfactant and a solid carrier; mixing components comprising the solid surfactant composite and a base fluid to provide a spacer fluid; and introducing a spacer fluid into a wellbore such that the spacer fluid displaces a drilling fluid in the wellbore.
- the solid surfactant composite may be spray dried.
- the solid surfactant composite may further comprise at least one additive selected from the group consisting of a dispersant, a defoaming agent, and any combination thereof.
- the water-wetting surfactant comprises at least one surfactant selected from the group consisting of an alcohol ethoxylate, an alcohol ethoxysulfate, an alkyl phenol ethoxylate, a glycol ether, and any combination thereof.
- the water-wetting surfactant may comprise an alcohol ethoxylate, wherein the alcohol ethoxylate comprises Cs to C12 alcohol ethoxylated with about 4 moles to about 8 moles of ethylene oxide.
- the solid carrier may comprise amorphous silica, and wherein the solid surfactant composite further comprises a naphthalene sulfonate formaldehyde condensate and a polydimethyl siloxane.
- the water- wetting surfactant may comprise an alcohol ethoxylate, wherein the alcohol ethoxylate comprises C12 to C14 alcohol ethoxylated with about 10 moles to about 14 moles of ethylene oxide.
- the solid carrier may comprise amorphous silica and diatomaceous earth, and wherein the solid surfactant composite further comprises a naphthalene sulfonate formaldehyde condensate and a polydimethyl siloxane.
- the components mixed to prepare the spacer fluid may further comprise a solid particulate additive, and the mixing comprising mixing a dry blend comprising the solid surfactant and the solid particulate additive with the base fluid.
- the solid particulate additive comprises at least one solid material selected from the group consisting of a weighting agent, vitrified shale, cement kiln dust, silica flour, bentonite, pumice, fly ash, hematite, hausmannite, barite, calcium carbonate, and any combination thereof.
- the base fluid may comprise an aqueous-base fluid selected from the group consisting of fresh water, salt water, brine, seawater, and any combination thereof.
- the spacer fluid may not be emulsified. The spacer fluid may be introduced into a wellbore annulus.
- a composition may be provided that comprises a solid surfactant composite comprising a water-wetting surfactant and a solid carrier; and a solid particulate additive dry blended with the solid surfactant composite.
- the solid surfactant composite may be spray dried.
- the solid surfactant composite may further comprise at least one additive selected from the group consisting of a dispersant, a defoaming agent, and any combination thereof.
- the water-wetting surfactant comprises at least one surfactant selected from the group consisting of an alcohol ethoxylate, an alcohol ethoxysulfate, an alkyl phenol ethoxylate, a glycol ether, and any combination thereof.
- the water-wetting surfactant may comprise an alcohol ethoxylate, wherein the alcohol ethoxylate comprises Cs to C 12 alcohol ethoxylated with about 4 moles to about 8 moles of ethylene oxide.
- the solid carrier may comprise amorphous silica, and wherein the solid surfactant composite further comprises a naphthalene sulfonate formaldehyde condensate and a polydimethyl siloxane.
- the water-wetting surfactant may comprise an alcohol ethoxylate, wherein the alcohol ethoxylate comprises C 12 to C 14 alcohol ethoxylated with about 10 moles to about 14 moles of ethylene oxide.
- the solid carrier may comprise amorphous silica and diatomaceous earth, and wherein the solid surfactant composite further comprises a naphthalene sulfonate formaldehyde condensate and a polydimethyl siloxane.
- the solid particulate additive comprises at least one solid material selected from the group consisting of a weighting agent, vitrified shale, cement kiln dust, silica flour, bentonite, pumice, fly ash, hematite, hausmannite, barite, calcium carbonate, and any combination thereof.
- a system may comprise a solid surfactant composite for use in a spacer fluid, wherein the solid surfactant component comprises a water-wetting surfactant and a solid carrier; a base fluid for use in the spacer fluid; and a pump fluid fluidly coupled to a tubular in fluid communication with a wellbore, wherein the tubular is configured to convey the spacer fluid to the wellbore.
- the system may further comprise a vessel disposed upstream of the pump, wherein the spacer fluid is disposed in the vessel.
- the solid surfactant composite may be spray dried.
- the solid surfactant composite may further comprise at least one additive selected from the group consisting of a dispersant, a defoaming agent, and any combination thereof.
- the water-wetting surfactant comprises at least one surfactant selected from the group consisting of an alcohol ethoxylate, an alcohol ethoxysulfate, an alkyl phenol ethoxylate, a glycol ether, and any combination thereof.
- the water-wetting surfactant may comprise an alcohol ethoxylate, wherein the alcohol ethoxylate comprises Cs to C 12 alcohol ethoxylated with about 4 moles to about 8 moles of ethylene oxide.
- the solid carrier may comprise amorphous silica, and wherein the solid surfactant composite further comprises a naphthalene sulfonate formaldehyde condensate and a polydimethyl siloxane.
- the water-wetting surfactant may comprise an alcohol ethoxylate, wherein the alcohol ethoxylate comprises C 12 to C 14 alcohol ethoxylated with about 10 moles to about 14 moles of ethylene oxide.
- the solid carrier may comprise amorphous silica and diatomaceous earth, and wherein the solid surfactant composite further comprises a naphthalene sulfonate formaldehyde condensate and a polydimethyl siloxane.
- the components mixed to prepare the spacer fluid may further comprise a solid particulate additive, and the mixing comprising mixing a dry blend comprising the solid surfactant and the solid particulate additive with the base fluid.
- the solid particulate additive comprises at least one solid material selected from the group consisting of a weighting agent, vitrified shale, cement kiln dust, silica flour, bentonite, pumice, fly ash, hematite, hausmannite, barite, calcium carbonate, and any combination thereof.
- the base fluid may comprise an aqueous- base fluid selected from the group consisting of fresh water, salt water, brine, seawater, and any combination thereof.
- the spacer fluid may not be emulsified. The spacer fluid may be introduced into a wellbore annulus.
- FIG. 1 illustrates an example system 100 that may be used for preparation and delivery of a spacer fluid downhole. It should be noted that while FIG. 1 generally depicts a land-based operation, those skilled in the art will readily recognize that the principles described herein are equally applicable to subsea operations that employ floating or sea-based platforms and rigs, without departing from the scope of the disclosure. As illustrated on FIG. 1, the system 100 may include a vessel 105 and a pump 110.
- the pump 110 may be positioned downstream of the vessel 105 and may be fluidly coupled to a tubular 115 that is in fluid communication with the wellbore 120.
- the tubular 115 may be configured to circulate or otherwise deliver the spacer fluid to the wellbore 120.
- the tubular 115 may be comprised, for example, of one or more different pipes that extend into the wellbore 120.
- the pump 110 may be, for example, one or more high pressure or low pressure pumps, which may be depend on, without limitation, the viscosity and density of the spacer fluid. Without limitation, the pump 110 may draw the spacer fluid from the vessel 105, elevate the spacer fluid to an appropriate pressure, and then introduce the spacer fluid to the tubular 115 for delivery downhole.
- the vessel 105 and pump 110 may be disposed on one or more cement trucks, for example.
- system 100 may further include a recirculating mixer, a batch mixer and/or a jet mixer, which may be used for example, in preparation and/or storage of the spacer fluid.
- additional components include, but are not limited to, supply hoppers, valves, condensers, adapters, joints, gauges, sensors, compressors, pressure controllers, pressure sensors, flow rate controllers, flow rate sensors, temperature sensors, and the like.
- FIG. 2 depicts one or more subterranean formations 200 penetrated by wellbore 120 with drilling fluid 205 disposed therein.
- the drilling fluid 205 may include the example drilling fluids disclosed herein as well as other suitable drilling fluids that will be readily apparent to those of ordinary skill in the art.
- the wellbore 120 is shown extending generally vertically into the one or more subterranean formations 200, the principles described herein are also applicable to wellbores that extend at an angle through the one or more subterranean formations 200, such as horizontal and slanted wellbores.
- the wellbore 120 comprises walls 210.
- a surface casing 215 may be cemented to the walls 210 of the wellbore 120 by cement sheath 220.
- one or more additional pipe strings may also be disposed in the wellbore 120.
- one or more centralizers may be attached to the casing 225, for example, to centralize the casing 225 in the wellbore 120 prior to and during the cementing operation.
- a cement composition 235 may be introduced into the wellbore 120.
- the cement composition 235 may be pumped down the interior of the casing 225.
- a pump e.g. pump 110 on FIG. 1
- the cement composition 235 may include the example cement compositions disclosed herein as well as other suitable cement compositions that will be readily apparent to those of ordinary skill in the art.
- other techniques may also be utilized for introduction of the cement composition 235.
- reverse circulation techniques may be used that include introducing the cement composition 235 into the wellbore 120 by way of the wellbore annulus 230 instead of through the casing 225.
- the spacer fluid 240 may be used to separate the drilling fluid 205 from the cement composition 235.
- the previous description with reference to FIG. 1 for preparation of a spacer fluid may be used for delivery of the spacer fluid 240 into the wellbore 120.
- a pump e.g., pump 110 on FIG. 1
- the spacer fluid 240 may be used with the cement composition 235 for displacement of the drilling fluid 205 from the wellbore 120 as well as preparing the wellbore 120 for the cement composition 235.
- the spacer fluid 240 may function, inter alia, to remove the drilling fluid 205, drilling fluid 205 that is dehydrated/gelled, and/or filter cake solids from the wellbore 120 in advance of the cement composition 235. While not shown, one or more plugs or other suitable devices may be used to physically separate the drilling fluid 205 from the spacer fluid 240 and/or the spacer fluid 240 from the cement composition 235.
- the drilling fluid 205 has been displaced from the wellbore annulus 230.
- the spacer fluid 240 and the cement composition 235 may be allowed to flow down the interior of the casing 225 through the bottom of the casing 225 (e.g., casing shoe 300) and up around the casing 225 into the wellbore annulus 230, thus displacing the drilling fluid 205.
- At least a portion of the displaced drilling fluid 205 may exit the wellbore annulus 230 via a flow line 125 and be deposited, for example, in one or more retention pits 130 (e.g., a mud pit), as shown in FIG. 1.
- retention pits 130 e.g., a mud pit
- the cement composition 235 may continue to be circulated until it has reached a desired location in the wellbore annulus 230.
- the spacer fluid 240 (or a portion thereof) and/or the cement composition 235 may be left in the wellbore annulus 230.
- the spacer fluid 240 may be disposed in the wellbore annulus 230 above or on top of the cement composition 235.
- the cement composition 235 may set in the wellbore annulus 230 to form an annular sheath of hardened, substantially impermeable material (i.e., a cement sheath) that may support and position the casing 225 in the wellbore 120.
- the exemplary spacer fluid disclosed herein may directly or indirectly affect one or more components or pieces of equipment associated with the preparation, delivery, recapture, recycling, reuse, and/or disposal of the sugar cane ash and associated spacer fluids.
- the spacer fluid (or components thereof) may directly or indirectly affect one or more mixers, related mixing equipment, mud pits, storage facilities or units, composition separators, heat exchangers, sensors, gauges, pumps, compressors, and the like used generate, store, monitor, regulate, and/or recondition the exemplary sugar cane ash and fluids containing the same.
- the disclosed spacer fluid may also directly or indirectly affect any transport or delivery equipment used to convey the spacer fluid (or components thereof) to a well site or downhole such as, for example, any transport vessels, conduits, pipelines, trucks, tubulars, and/or pipes used to compositionally move the spacer fluid (or components thereof) from one location to another, any pumps, compressors, or motors (e.g., topside or downhole) used to drive the spacer fluid (or components thereof), into motion, any valves or related joints used to regulate the pressure or flow rate of the spacer fluid, and any sensors (i.e., pressure and temperature), gauges, and/or combinations thereof, and the like.
- any transport or delivery equipment used to convey the spacer fluid (or components thereof) to a well site or downhole
- any transport vessels, conduits, pipelines, trucks, tubulars, and/or pipes used to compositionally move the spacer fluid (or components thereof) from one location to another
- any pumps, compressors, or motors e.g., topside or downhole
- the disclosed spacer fluid may also directly or indirectly affect the various downhole equipment and tools that may come into contact with the spacer fluid such as, but not limited to, wellbore casing, wellbore liner, completion string, insert strings, drill string, coiled tubing, slickline, wireline, drill pipe, drill collars, mud motors, downhole motors and/or pumps, cement pumps, surface-mounted motors and/or pumps, centralizers, turbolizers, scratchers, floats (e.g., shoes, collars, valves, etc.), logging tools and related telemetry equipment, actuators (e.g., electromechanical devices, hydromechanical devices, etc.), sliding sleeves, production sleeves, plugs, screens, filters, flow control devices (e.g., inflow control devices, autonomous inflow control devices, outflow control devices, etc.), couplings (e.g., electro-hydraulic wet connect, dry connect, inductive coupler, etc.), control lines (e.g., electrical, fiber optic, hydraulic, etc.), surveillance
- Example 1 Two solid surfactant composites were prepared in accordance with the following procedures.
- the solid surfactant composites are identified as Solid Surfactant Composite A (SSCA) and Solid Surfactant Composite B (SSSB).
- SSCA Solid Surfactant Composite A
- SSSB Solid Surfactant Composite B
- naphthalene sulfonate condensed with 6 moles of formaldehyde 20% by weight of naphthalene sulfonate condensed with 6 moles of formaldehyde; 23% by weight of diatomaceous earth; 17% by weight of amorphous silica; 30% by weight of isotridecyl alcohol with 12 moles of ethylene oxide; and 10% by weight of polydimethyl siloxane emulsion.
- the naphthalene sulfonate formaldehyde condensate was mixed in a blender with the diatomaceous earth followed by addition of the amorphous silica. This mixture was mixed until a homogenous mixture was formed.
- the isotridecyl alcohol was then added to the blender containing this mixture and mixed until homogenous.
- the polydimethyl siloxane emulsion was added to the blender and mixed until homogenous. Thereafter, the resulting mixture was spray dried to produce SSCB.
- SSCA Solid Surfactant Composite A
- OBM synthetic oil-based mud
- the spacer fluid and the OBM were mixed in various proportions.
- the rheology was measured at the test temperature (190 °F) using a FANNTM Model 35 viscometer.
- the composition of the spacer fluid and the test results are provided below.
- Tuned SpacerTM III Blend is a dry blend available from Halliburton Energy Services, Inc., that comprises from about 60-80 weight % vitrified shale, from about 5-20 weight % sepiolite, from about 5-20 weight % diatomaceous earth, and from about 1-10 weight percent welan gum.
- Fe-2TM Agent is an organic acid available from Halliburton Services, Inc.
- D-AIR-5000TM Defoamer is a defoaming additive available from Halliburton Energy Services, Inc.
- SSCB Solid Surfactant Composite B
- OBM synthetic oil-based mud
- the spacer fluid and the OBM were mixed in various proportions.
- the rheology was measured at the test temperature (190 °F) using a FANNTM Model 35 viscometer.
- the composition of the spacer fluid and the test results are provided below. Table 3.
- gps refers to gallons of the additive per 30- pound sack of the Tuned SpacerTM III Blend and the abbreviation “lb/bbl” refers to pounds of the additive per 42 gallon barrel of the spacer fluid.
- gps refers to gallons of the additive per 30- pound sack of the Tuned SpacerTM III Blend and the abbreviation “lb/bbl” refers to pounds of the additive per 42 gallon barrel of the spacer fluid.
- Additional dry surfactant composites were prepared to test the wettability of the dry surfactant composites and their compatibility with an oil-based drilling fluid (OBM).
- the additional dry surfactants comprised different water-wetting surfactants as provided below:
- Solid Surfactant Composite C Nonylphenol with 10.5 moles of ethylene oxide (Surfactant C)
- Solid Surfactant Composite D Ethoxylated tetradecyl ammonium sulfate (Surfactant D).
- Solid Surfactant Composite E Ethylene glycol monobutyl ether and hexanol with 6 moles of ethylene oxide in weight ratio of 9:1 (Surfactant E).
- SSCE Solid Surfactant Composite E
- the wettability of the solid surfactant composite was tested by including 8.932 lb/bbl of SSCC and 10.556 lb/bbl of SSCE in the spacer fluid.
- An apparent wettability meter test was used to measure Hogan (HN) readings.
- HN Hogan
- the rheological values for different ratios of the spacer fluid to the OBM are provided in Tables 8-10 below.
- the rheological values of the combined spacer fluid/OBM were also determined with no water-wetting surfactant and with a corresponding liquid surfactant.
- Tables 4-6 inclusion spacer fluid comprising a solid surfactant composite provide comparable drilling fluid compatibility as corresponding liquid surfactants.
- compositions and methods are described in terms of “comprising,” “containing,” or “including” various components or steps, the compositions and methods can also “consist essentially of or “consist of the various components and steps.
- indefinite articles “a” or “an,” as used in the claims, are defined herein to mean one or more than one of the element that it introduces.
- ranges from any lower limit may be combined with any upper limit to recite a range not explicitly recited, as well as, ranges from any lower limit may be combined with any other lower limit to recite a range not explicitly recited, in the same way, ranges from any upper limit may be combined with any other upper limit to recite a range not explicitly recited.
- any numerical range with a lower limit and an upper limit is disclosed, any number and any included range falling within the range are specifically disclosed.
- every range of values (of the form, "from about a to about b,” or, equivalently, “from approximately a to b,” or, equivalently, “from approximately a-b") disclosed herein is to be understood to set forth every number and range encompassed within the broader range of values even if not explicitly recited.
- every point or individual value may serve as its own lower or upper limit combined with any other point or individual value or any other lower or upper limit, to recite a range not explicitly recited.
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- Mining & Mineral Resources (AREA)
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- Fluid Mechanics (AREA)
- Environmental & Geological Engineering (AREA)
- Physics & Mathematics (AREA)
- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- Geochemistry & Mineralogy (AREA)
- Curing Cements, Concrete, And Artificial Stone (AREA)
- Soil Conditioners And Soil-Stabilizing Materials (AREA)
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- Consolidation Of Soil By Introduction Of Solidifying Substances Into Soil (AREA)
Abstract
Description
Claims
Priority Applications (10)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PCT/US2015/057380 WO2017074301A1 (en) | 2015-10-26 | 2015-10-26 | Use of solid surfactant composites in well cementing |
| US15/759,469 US10584273B2 (en) | 2015-10-26 | 2015-10-26 | Use of solid surfactant composites in well spacer fluids |
| BR112018005760-6A BR112018005760B1 (en) | 2015-10-26 | 2015-10-26 | METHOD AND SYSTEM FOR USING SOLID SURFACTANT COMPOUNDS IN WELL CEMENTING OPERATIONS |
| MX2018003760A MX2018003760A (en) | 2015-10-26 | 2015-10-26 | Use of solid surfactant composites in well cementing. |
| AU2015413284A AU2015413284B2 (en) | 2015-10-26 | 2015-10-26 | Use of solid surfactant composites in well cementing |
| CA2998489A CA2998489C (en) | 2015-10-26 | 2015-10-26 | Use of solid surfactant composites in well cementing |
| GB1803872.9A GB2557779B (en) | 2015-10-26 | 2015-10-26 | Use of solid surfactant composites in well cementing |
| ARP160102906A AR106125A1 (en) | 2015-10-26 | 2016-09-23 | USE OF SOLID TENSIOACTIVE COMPOUNDS IN WELL CEMENTATION |
| NO20180404A NO347758B1 (en) | 2015-10-26 | 2018-03-22 | Use of solid surfactant composites in well cementing |
| US16/737,596 US11312893B2 (en) | 2015-10-26 | 2020-01-08 | Use of solid surfactant composites in well cementing |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PCT/US2015/057380 WO2017074301A1 (en) | 2015-10-26 | 2015-10-26 | Use of solid surfactant composites in well cementing |
Related Child Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US15/759,469 A-371-Of-International US10584273B2 (en) | 2015-10-26 | 2015-10-26 | Use of solid surfactant composites in well spacer fluids |
| US16/737,596 Division US11312893B2 (en) | 2015-10-26 | 2020-01-08 | Use of solid surfactant composites in well cementing |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2017074301A1 true WO2017074301A1 (en) | 2017-05-04 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/US2015/057380 Ceased WO2017074301A1 (en) | 2015-10-26 | 2015-10-26 | Use of solid surfactant composites in well cementing |
Country Status (9)
| Country | Link |
|---|---|
| US (2) | US10584273B2 (en) |
| AR (1) | AR106125A1 (en) |
| AU (1) | AU2015413284B2 (en) |
| BR (1) | BR112018005760B1 (en) |
| CA (1) | CA2998489C (en) |
| GB (1) | GB2557779B (en) |
| MX (1) | MX2018003760A (en) |
| NO (1) | NO347758B1 (en) |
| WO (1) | WO2017074301A1 (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10472552B2 (en) | 2017-08-08 | 2019-11-12 | Bj Services, Llc | Spacer fluids for cementing well bores |
| WO2020023227A1 (en) * | 2018-07-25 | 2020-01-30 | Halliburton Energy Services, Inc. | Surfactant compositions comprising solid substrates for subterranean well operations |
| US11168242B2 (en) | 2019-02-01 | 2021-11-09 | Halliburton Energy Services, Inc. | Compatible low crystalline silica spacers |
| US11312893B2 (en) | 2015-10-26 | 2022-04-26 | Halliburton Energy Services, Inc. | Use of solid surfactant composites in well cementing |
| US11939518B2 (en) | 2022-02-28 | 2024-03-26 | Halliburton Energy Services, Inc. | Wellbore treatment fluid |
| WO2025216971A1 (en) | 2024-04-12 | 2025-10-16 | Sasol Chemie Gmbh & Co Kg | Solid surfactant package for spacer fluids |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10266745B2 (en) | 2017-02-03 | 2019-04-23 | Saudi Arabian Oil Company | Anti-bit balling drilling fluids, and methods of making and use thereof |
| WO2020033861A2 (en) * | 2018-08-10 | 2020-02-13 | Matthew Oehler | Proppant dispensing system |
| US11939513B2 (en) | 2021-10-28 | 2024-03-26 | Select Chemistry, Llc | Surfactant impregnated lost circulation, scrubbing, and scouring material |
| WO2023101801A1 (en) * | 2021-12-01 | 2023-06-08 | Rockwater Energy Solutions, Llc | Compositions of aphron sealing lost circulation spacer |
| US12269993B2 (en) * | 2022-02-15 | 2025-04-08 | Halliburton Energy Services, Inc. | Surfactant package and methods of making and using same |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3850248A (en) * | 1973-11-19 | 1974-11-26 | Halliburton Co | Method of using a spacer fluid for spacing drilling muds and cement |
| EP0814232B1 (en) * | 1996-06-19 | 2003-12-03 | Halliburton Energy Services, Inc. | Well completion spacer fluids |
| US6668927B1 (en) * | 2003-03-21 | 2003-12-30 | Halliburton Energy Services, Inc. | Well completion foamed spacer fluids and methods |
| US20150129217A1 (en) * | 2013-11-12 | 2015-05-14 | Baker Hughes Incorporated | Wellbore Cement Compositions and Wellbore Cementing Methods |
| WO2015076845A1 (en) * | 2013-11-25 | 2015-05-28 | Halliburton Energy Services, Inc. | Viscosified treatment fluids comprising polyol derivatized cellulose and methods relating thereto |
Family Cites Families (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6221381B1 (en) | 1994-06-28 | 2001-04-24 | The University Of British Columbia | Enhancing milk production by adding to feed a nonionic surfactant coated on a carrier |
| US6258757B1 (en) * | 1997-03-14 | 2001-07-10 | Halliburton Energy Services, Inc. | Water based compositions for sealing subterranean zones and methods |
| US6302209B1 (en) * | 1997-09-10 | 2001-10-16 | Bj Services Company | Surfactant compositions and uses therefor |
| US5996692A (en) * | 1998-02-13 | 1999-12-07 | Atlantic Richfield Company | Surfactant composition and method for cleaning wellbore and oil field surfaces using the surfactant composition |
| US6271181B1 (en) * | 1999-02-04 | 2001-08-07 | Halliburton Energy Services, Inc. | Sealing subterranean zones |
| US7293609B2 (en) * | 2004-10-20 | 2007-11-13 | Halliburton Energy Services, Inc. | Treatment fluids comprising vitrified shale and methods of using such fluids in subterranean formations |
| US7318477B2 (en) * | 2005-05-10 | 2008-01-15 | Akzo Nobel N.V. | Method and composition for cleaning a well bore prior to cementing |
| JP5529373B2 (en) | 2007-11-20 | 2014-06-25 | 花王株式会社 | Particle surface modification method |
| AU2009282194B2 (en) * | 2008-08-12 | 2012-04-19 | Dow Agrosciences Llc | Synergistic pesticidal compositions comprising an active compound, an ammonium salt, and a nonionic surfactant |
| US8082992B2 (en) * | 2009-07-13 | 2011-12-27 | Halliburton Energy Services, Inc. | Methods of fluid-controlled geometry stimulation |
| US8529693B2 (en) | 2010-12-10 | 2013-09-10 | Troy Corporation | Adhesive strength enhancers for cementitious compositions |
| US9464223B2 (en) * | 2013-03-14 | 2016-10-11 | Flotek Chemistry, Llc | Methods and compositions for use in oil and/or gas wells |
| US9944842B2 (en) * | 2014-02-05 | 2018-04-17 | Baker Hughes, A Ge Company, Llc | Methods of pre-flushing reservoir paths for higher return of hydrocarbon fluids |
| US10329472B2 (en) | 2015-03-04 | 2019-06-25 | Halliburton Energy Services, Inc. | Wellbore additives that include liquid-infiltrated porous silica |
| AU2015413284B2 (en) | 2015-10-26 | 2021-07-01 | Halliburton Energy Services, Inc. | Use of solid surfactant composites in well cementing |
-
2015
- 2015-10-26 AU AU2015413284A patent/AU2015413284B2/en active Active
- 2015-10-26 MX MX2018003760A patent/MX2018003760A/en unknown
- 2015-10-26 WO PCT/US2015/057380 patent/WO2017074301A1/en not_active Ceased
- 2015-10-26 GB GB1803872.9A patent/GB2557779B/en active Active
- 2015-10-26 BR BR112018005760-6A patent/BR112018005760B1/en active IP Right Grant
- 2015-10-26 US US15/759,469 patent/US10584273B2/en active Active
- 2015-10-26 CA CA2998489A patent/CA2998489C/en active Active
-
2016
- 2016-09-23 AR ARP160102906A patent/AR106125A1/en active IP Right Grant
-
2018
- 2018-03-22 NO NO20180404A patent/NO347758B1/en unknown
-
2020
- 2020-01-08 US US16/737,596 patent/US11312893B2/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3850248A (en) * | 1973-11-19 | 1974-11-26 | Halliburton Co | Method of using a spacer fluid for spacing drilling muds and cement |
| EP0814232B1 (en) * | 1996-06-19 | 2003-12-03 | Halliburton Energy Services, Inc. | Well completion spacer fluids |
| US6668927B1 (en) * | 2003-03-21 | 2003-12-30 | Halliburton Energy Services, Inc. | Well completion foamed spacer fluids and methods |
| US20150129217A1 (en) * | 2013-11-12 | 2015-05-14 | Baker Hughes Incorporated | Wellbore Cement Compositions and Wellbore Cementing Methods |
| WO2015076845A1 (en) * | 2013-11-25 | 2015-05-28 | Halliburton Energy Services, Inc. | Viscosified treatment fluids comprising polyol derivatized cellulose and methods relating thereto |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US11312893B2 (en) | 2015-10-26 | 2022-04-26 | Halliburton Energy Services, Inc. | Use of solid surfactant composites in well cementing |
| US10472552B2 (en) | 2017-08-08 | 2019-11-12 | Bj Services, Llc | Spacer fluids for cementing well bores |
| WO2020023227A1 (en) * | 2018-07-25 | 2020-01-30 | Halliburton Energy Services, Inc. | Surfactant compositions comprising solid substrates for subterranean well operations |
| US11434414B2 (en) | 2018-07-25 | 2022-09-06 | Halliburton Energy Services, Inc. | Surfactant compositions comprising solid substrates for subterranean well operations |
| US11884880B2 (en) | 2018-07-25 | 2024-01-30 | Halliburton Energy Services, Inc. | Surfactant compositions comprising solid substrates for subterranean well operations |
| US11168242B2 (en) | 2019-02-01 | 2021-11-09 | Halliburton Energy Services, Inc. | Compatible low crystalline silica spacers |
| US11578249B2 (en) | 2019-02-01 | 2023-02-14 | Halliburton Energy Services, Inc. | Compatible low crystalline silica spacers |
| US11939518B2 (en) | 2022-02-28 | 2024-03-26 | Halliburton Energy Services, Inc. | Wellbore treatment fluid |
| WO2025216971A1 (en) | 2024-04-12 | 2025-10-16 | Sasol Chemie Gmbh & Co Kg | Solid surfactant package for spacer fluids |
Also Published As
| Publication number | Publication date |
|---|---|
| AU2015413284B2 (en) | 2021-07-01 |
| MX2018003760A (en) | 2018-07-06 |
| GB2557779B (en) | 2021-11-24 |
| BR112018005760B1 (en) | 2022-07-26 |
| US20200140740A1 (en) | 2020-05-07 |
| AR106125A1 (en) | 2017-12-13 |
| NO20180404A1 (en) | 2018-03-22 |
| GB2557779A (en) | 2018-06-27 |
| CA2998489A1 (en) | 2017-05-04 |
| US10584273B2 (en) | 2020-03-10 |
| US11312893B2 (en) | 2022-04-26 |
| CA2998489C (en) | 2020-09-29 |
| AU2015413284A1 (en) | 2018-04-12 |
| GB201803872D0 (en) | 2018-04-25 |
| BR112018005760A2 (en) | 2018-10-09 |
| US20180265763A1 (en) | 2018-09-20 |
| NO347758B1 (en) | 2024-03-18 |
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