Patent Application
20240117238
The invention generally concerns nanoparticles that can be used as well-treatment additives. The nanoparticles can contain a carrier material and an asphaltene inhibitor.
Asphaltenes are a heavy fraction of crude oil and contains heterocyclic macromolecules having molecular weight of approximately 700 to 1,000 g/mole. Asphaltenes are typically present in hydrocarbon reservoirs. Asphaltenes may become problematic once they are destabilized in solution, leading to asphaltene deposition and precipitation. Asphaltene can become destabilized due to a number of factors such as changes in temperature, pressure, chemical composition of crude oil, and/or shear rate during petroleum production. Asphaltene deposition and precipitation can occur throughout the petroleum production system, from inside the reservoir formation to pumps, tubing, wellheads, safety valves, flow lines, and surface facilities used in the petroleum production process. The nature of asphaltene deposits may depend on the composition of the crude oil and/or the conditions under which precipitation occurred. Asphaltene deposits can appear hard and coal-like or sticky and tar-like. Asphaltene deposition and precipitation can cause plugging problems, such as pore throat plugging, which may cause blockages and lead to lower production rates. Asphaltene deposition may increase hydrocarbon viscosity which may lead to separation problems. Asphaltene deposition and precipitation can cause adverse effects in both production and refining of petroleum.
Asphaltene inhibitors can be used to control formation of asphaltene deposits by controlling the precipitation of asphaltene. Various asphaltene inhibitors are known that can prevent or reduce asphaltene precipitation from crude oil, prevent or reduce deposition of asphaltene on surfaces that come contact with crude oil, and/or help in removal of an asphaltene deposit already formed on a surface. For example, US patent application publications 20170058185 and 20190177630 disclose phenol aldehyde, and aromatic core containing asphaltene inhibitors, respectively.
The typical approach for treating well formations with asphaltene inhibitors includes delivery of the inhibitors through a capillary string in a continuous treatment downhole. This can leave portions of the reservoir untreated and can also consume large amounts of the inhibitor. Pre-existing infrastructure is needed to deploy the treatment and is not easily retrofitted to wells that exhibit a sudden onset of asphaltene formation/deposits.
A discovery has been made that provides a solution to at least one or more of the problems associated with treating subterranean formations (e.g., reservoirs) and/or wells (e.g., oil, gas and water wells) with asphaltene inhibitors. In one aspect, a solution can reside in the development of a nanoparticle that can include a carrier material and an asphaltene inhibitor(s). The nanoparticle can be structured such that it is capable of releasing the asphaltene inhibitor(s) over prolonged or extended periods of time. In one aspect, the nanoparticle can be structured such that the asphaltene inhibitor can be attached to the carrier material. The nanoparticle can allow for a slow release profile of the asphaltene inhibitor after being introduced into wells or subterranean formations. In some aspects, the release profile can be at least for 10, 20, 30, 40, 50, 60, 70, 80, 90, 100, 200, 300, 400, 500, 1,000, 2,000, 3,000, or 4,000, days or more, or from 10 days to 500 days, or from 20 days to 365 days, or from 500 days to 2500 days, or from 500 days to 2000 days, or from 10 days to 10 years after well treatment. The time the nanoparticle continues to return meaningful concentrations of the asphaltene inhibitor(s) can vary depending on the production rate of the well. This, in turn, can reduce the costs, expenses, and overall inefficiencies with having to perform continuous or more periodic well treatments such as with the processes currently used in the well-treatment industry. In one particular aspect, asphaltene inhibitor containing nanoparticles of the invention can be used to treat subterranean formations and/or wells by squeeze treatment. The subterranean formations and/or wells can be treated with the nanoparticles of the invention with currently available infrastructure. In certain aspects, 100 kilograms (kg) to 5000000 (kg), preferably, 2000 (kg) to 50000 kg (or any range or number therein such as 100, 200, 300, 400, 500, 600, 700, 800, 900, 1000, 2000, 3000, 4000, 5000, 6000, 7000, 8000, 9000, 10000, 20000, 30000, 40000, 50000, 60000, 70000, 80000, 90000, 100000, 200000, 300000, 400000, 500000, 600000, 700000, 800000, 900000, 1000000, 2000000, 3000000, 4000000, or 5000000) of the nanoparticles can be used to treat, such as via squeeze treatment, subterranean formations and/or wells for 1000 barrels to 200000000 barrels, preferably 300000 barrels to 8000000 barrels, of oil produced of oil produced (or any range or number therein such as 1000, 5000, 10000, 20000, 30000, 40000, 50000, 60000, 70000, 80000, 90000, 100000, 200000, 300000, 400000, 500000, 600000, 700000, 800000, 900000, 1000000, 2000000, 3000000, 4000000, 5000000, 6000000, 7000000, 8000000, 9000000, 10000000, or 20000000, 30000000, 40000000, 50000000, 60000000, 70000000, 80000000, 90000000, 100000000, 200000000).
One aspect of the present invention is directed to a nanoparticle that contains a releasable asphaltene inhibitor. The nanoparticle can further contain a carrier material. The asphaltene inhibitor can be impregnated within the nanoparticle, and/or can be bound or otherwise adhered on at least a portion of an outer surface of the nanoparticle. For example, the nanoparticle can contain a carrier material matrix, and the asphaltene inhibitor in the nanoparticle i) can be impregnated within the matrix, ii) can be surrounded by the matrix and/or iii) can be bound or otherwise adhered to at least a portion of the surface of the matrix. The nanoparticle can have a size of 5 nm to 1000 nm, preferably, 10 nm to 500 nm (or any range or number therein such as 5, 10, 15, 20, 25, 30, 35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90, 95, 100, 200, 300, 400, 500, 600, 700, 800, 900, or 1000). The size can be determined by the diameter of the nanoparticle. In certain aspects, the nanoparticle can have a diameter of 5 nm to 1000 nm, preferably 50 nm to 400 nm (or any range or number therein such as 5, 10, 15, 20, 25, 30, 35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90, 95, 100, 200, 300, 400, 500, 600, 700, 800, 900, or 1000). In some aspects, the nanoparticle can contain 5 wt. % to 95 wt. % of the carrier material and 5 wt. % to 95 wt. % of the asphaltene inhibitor. In some particular aspects, the nanoparticle can contain 20 wt. % to 80 wt. % of the carrier material and 20 wt. % to 80 wt. % of the asphaltene inhibitor. In some aspects, the carrier material matrix can be a porous matrix. In some aspects, the carrier material matrix can be an open-celled porous matrix. In some aspects, the carrier material can contain a metalloid matrix (e.g. a silica matrix), a polymer matrix, a carbon matrix, a transition or post-transition metal oxide matrix, lipid matrix, wax matrix, or a column 2 metal oxide matrix, a clay matrix, a metal organic framework (MOF) matrix, a zeolite matrix, a zeolite imidazolate framework (ZIF) matrix, a covalent organic framework (COF) matrix, or any combinations thereof In some aspects, the carrier material can contain silica matrix. In some aspects, the silica matrix can contain porous silica. In some aspects, the silica matrix can contain open-celled porous silica. The open-celled porous silica can be microporous, mesoporous or macroporous silica. The silica can be crystalline silica (e.g., α-quartz, β-quartz, α-tridymite, β-tridymite, α-cristobalite, β-cristobalite, keatite, coesite, stishovite, and/or moganite). The silica can be amorphous silica (e.g., diatomite silica, calcined silica, flux-calcined silica, fused silica, silica fume, or synthetic amorphous silica (e.g., fumed silica or precipitated silica)). In some particular aspects, the open-celled porous matrix (e.g., silica matrix) can contain pores having an average pore size of 0.1 nm to 200 nm. In some aspects, at least a portion of the asphaltene inhibitor in the nanoparticle can be contained in the pores of the porous matrix, such as open-celled porous silica matrix. In certain aspects, the nanoparticle can have a core-shell structure, containing a core containing the asphaltene inhibitor and a shell containing carrier material matrix. In certain aspects, the shell can contain porous silica matrix, such as open-celled porous silica matrix. In certain aspects, 90 wt. % or more of the core, based on the total weight of the core, can be comprised of the asphaltene inhibitor. In certain aspects, the shell can further contain the asphaltene inhibitor, and at least a portion of the asphaltene inhibitor in the shell can be comprised in the pores of the porous matrix of the shell and/or attached to at least a portion of a surface of the shell. In some aspects, the carrier matrix and asphaltene inhibitor containing nanoparticle do not have a core-shell structure. In some aspects, the carrier matrix can form the bulk of the nanoparticle and the asphaltene inhibitor can be bound or otherwise adhered to an outer surface of the carrier matrix, and/or at least a portion of the asphaltene inhibitor in the nanoparticle can be comprised in the pores of the porous carrier material matrix. In some aspects, the carrier matrix and asphaltene inhibitor containing nanoparticle can be free of, or substantially free of a metal. In certain aspects, the carrier material can contain a polymer matrix. In some aspects, the polymer matrix can contain a polymer such as polyolefin, paraffin wax, fatty glyceride, polyacrylamide, polystyrene, epoxide, polyester or any combinations thereof. In some aspects, the polymer can have a melting point of 30° C. to 300° C. In some particular aspects, the polymer can have a melting point of 50° C. to 200° C. In some aspects, the polymer matrix can contain polyolefin. In some aspects, the polyolefin can be polyethylene. In some aspects, the polyethylene can be oxidized polyethylene. In some particular aspects, the polyethylene, such as oxidized polyethylene can have i) a weight average molecular weight (Mw) of 2000 g/mol. to 20000 g/mol, and/or ii) a melting point of 30° C. to 300° C., preferably 50° C. to 200° C. In certain aspects, polyethylene, such as oxidized polyethylene can form the bulk of the particle, and the asphaltene inhibitor can be impregnated within, e.g. distributed through the bulk of the particle, and can be bound or otherwise adhered to an outer surface of the particle. In certain aspects, the carrier material can contain a transition metal oxide matrix. In certain aspects, the transition metal can be titanium. In certain aspects, the carrier material can contain a post-transition metal oxide matrix In certain aspects, the carrier material can contain a carbon matrix. In some aspects, the carbon matrix can be a porous carbon matrix. In some aspects, the carbon matrix can be an open-celled porous carbon matrix. In some particular aspects, the open-celled porous carbon matrix can contain pores having an average size of, less than 2 nanometers (nm) (e.g., 0.5 nm to 2 nm), 2 nanometers (nm) to 2000 nm, 2 nm to 1000 nm, 2 nm to 500 nm, 2 nm to 100 nm, 2 nm to 50 nm, or any size or range therein (e.g., 2 nm, 5 nm, 10 nm, 15 nm, 20 nm, 25 nm, 30 nm, 35 nm, 40 nm, 45 nm, 50 nm, 55 nm, 60 nm, 65 nm, 70 nm, 75 nm, 80 nm, 85 nm, 90 nm, 95 nm, 100 nm, 200 nm, 300 nm, 400 nm, 500 nm, 600 nm, 700 nm, 800 nm, 900 nm, 1000 nm, 1100 nm, 1200 nm, 1300 nm, 1400 nm, 1500 nm, 1600 nm, 1700 nm, 1800 nm, 1900 nm, or 2000 nm).
In certain aspects, the nanoparticle can contain a lipid matrix. In certain aspects, the nanoparticle can contain a wax matrix. In certain aspects, the nanoparticle can contain a column 2 metal oxide matrix. The asphaltene inhibitor can be a suitable asphaltene inhibitor known in the art. In some aspects, the asphaltene inhibitor can be a dispersant, a threshold inhibitor, or any chemical that affects asphaltene formation, asphaltene deposition, and/or transportation behavior of asphaltene. In certain aspects, the commercially available asphaltene inhibitors can be used includes but are not limited to FLOTREAT DF 267 from Clariant, FLOTREAT DF 15980 from Clariant, FATHOM XT SUB SEA525 from Baker Hughes, ASPH16507A from NALCO Champion and ASI 1262 from Total Additives. In some aspects, the asphaltene inhibitor is capable of acting as an asphaltene inhibitor and as a surface modifying agent or a surfactant, non-limiting examples of which include cationically charged asphaltnene inhibitors (e.g., imidazoline based), non-ionic asphaltene inhibitors (e.g., resin based), and/or anionically charged inhibitors (e.g., ester-based).
In some aspects, the asphaltene inhibitor can be physically entrapped within and/or detachably attached, e.g., chemically bonded, adsorbed, or otherwise adhered to the carrier material. The asphaltene inhibitor can be chemically bonded through an ionic bond, a covalent bond, a hydrogen bond, or a van der Waals interaction to the carrier material. In some aspects, the asphaltene inhibitor can be absorbed onto the carrier material. The asphaltene inhibitor can be capable of being released from the nanoparticle in a controlled manner over an extended period (e.g., at least for 10, 20, 30, 40, 50, 60, 70, 80, 90, 100, 200, 300, 400, 500, 1,000, 2,000, 3,000, or 4,000, days or more, or from 10 days to 500 days, or from 20 days to 365 days, or from 500 days to 2500 days, or from 500 days to 2000 days, or from 10 days to 10 years after well treatment). In certain aspects, 100 kilograms (kg) to 5000000 (kg), preferably, 2000 (kg) to 50000 kg (or any range or number therein such as 100, 200, 300, 400, 500, 600, 700, 800, 900, 1000, 2000, 3000, 4000, 5000, 6000, 7000, 8000, 9000, 10000, 20000, 30000, 40000, 50000, 60000, 70000, 80000, 90000, 100000, 200000, 300000, 400000, 500000, 600000, 700000, 800000, 900000, 1000000, 2000000, 3000000, 4000000, or 5000000) of the nanoparticles can be used to treat, such as via squeeze treatment, subterranean formations and/or wells for 1000 barrels to 200000000 barrels, preferably 300000 barrels to 8000000 barrels, of oil produced of oil produced (or any range or number therein such as 1000, 5000, 10000, 20000, 30000, 40000, 50000, 60000, 70000, 80000, 90000, 100000, 200000, 300000, 400000, 500000, 600000, 700000, 800000, 900000, 1000000, 2000000, 3000000, 4000000, 5000000, 6000000, 7000000, 8000000, 9000000, 10000000, or 20000000, 30000000, 40000000, 50000000, 60000000, 70000000, 80000000, 90000000, 100000000, 200000000). In certain aspects, the nanoparticle can further contain a surface modifying agent. The surface modifying agent can be impregnated within the nanoparticle, and/or can be bound or otherwise adhered on the surface of the nanoparticle. In certain aspects, the surface modifying agent can be bound or otherwise adhered on the surface of the nanoparticle. In certain aspects, the surface modifying agent can be sorbitan monooleate, sodium dodecylbenzene sulfonate, cetylpyridinium chloride, benzyl dim ethyl hexade cyl-amm onium chloride, bis(2-ethylhexyl)phosphate, cetrimonium chloride, cetrimonium bromide, 3-aminopropyltriethoxysilane, n-octadecyltrimethoxysilane or any combinations thereof. In some aspects, the carrier material can contain the polymer matrix, and the nanoparticle can have the surface modifying agent bound or otherwise adhered on the surface of the nanoparticle. In some aspects, the surface modifying agent of the polymer matrix containing nanoparticle can be sorbitan monooleate, sodium dodecylbenzene sulfonate, cetylpyridinium chloride, benzyldimethylhexadecyl-ammonium chloride, bis(2-ethylhexyl)phosphate, or any combinations thereof. In some aspects, the core-shell nanoparticle can contain the surface modifying agent bound or otherwise adhered on the surface of the nanoparticle. In certain aspects, the surface modifying agent of the core-shell nanoparticle can be 3-aminopropyltriethoxysilane and/or n-octadecyltrimethoxysilane. In some particular aspects, the surface modifying agent of the core-shell nanoparticle can be 3-aminopropyltriethoxysilane. In some aspects, the core-shell nanoparticle can further contain a surface active agent in the core. In some particular aspects, the surface active agent can be a cationic surfactant such as cetrimonium chloride, cetrimonium bromide, or any combinations thereof.
Also disclosed are methods for producing the nanoparticles of the present invention. The method can include contacting the asphaltene inhibitor with the carrier material to form the nanoparticle. In certain aspects, the carrier material can contain a polymer matrix, and the method can include contacting the polymer, the asphaltene inhibitor and a continuous phase (e.g. an immiscible solvent), at a temperature above the melting point of the polymer to form an emulsion containing the polymer and the asphaltene inhibitor, and cooling the emulsion to form a nanoparticle containing the polymer and asphaltene inhibitor. In certain aspects, the polymer and the asphaltene inhibitor can be contacted to form a mixture having a temperature greater than the melting point of the polymer, and the mixture can be contacted with the immiscible solvent to form the emulsion. The polymer and the asphaltene inhibitor can form a discontinuous droplet phase, and the immiscible solvent can form a continuous phase of the emulsion. The polymer and/or the asphaltene inhibitor can be heated before, during, and/or after contacting with each other to form the mixture having a temperature greater than the melting point of the polymer. The immiscible solvent can be immiscible with the polymer and the asphaltene inhibitor. In some aspects, the immiscible solvent can be water, acetic acid, butanol, ethylene glycol, acetyl acetone, or any combinations thereof, preferably water. In some aspects, a surface modifying agent can be contacted with the immiscible solvent, before, during, and/or after contacting the mixture with the immiscible solvent. In certain aspects, the mixture (e.g., of the polymer and the asphaltene inhibitor) can further contain the surface modifying agent, and the surface modifying agent can be contacted with the immiscible solvent and/or with the mixture. The surface modifying agent can be a non-ionic surfactant, an anionic surfactant, a cationic surfactant, an amphoteric surfactant, a zwitterionic surfactant, a block co-polymer, an organic compound, or any combinations thereof. In some aspects, the surface modifying agent used for preparing the polymer and the asphaltene inhibitor containing nanoparticle can include sorbitan monooleate, sodium dodecylbenzene sulfonate, cetylpyridinium chloride, benzyldimethylhexadecyl-ammonium chloride, bis(2-ethylhexyl)phosphate, or any combinations thereof. Without wishing to be bound by theory it is believed that surface modifying agent can control emulsion droplet formation, and/or stabilize the synthesized nanoparticles. In certain aspects, the surface modifying agent can get bound or otherwise adhered on the surface of the nanoparticle. In certain aspects, the polymer can be polyolefin, paraffin wax, fatty glyceride, polyacrylamide, polystyrene, epoxide, polyester or any combinations thereof. In some aspects, the polymer can be polyolefin. In some aspects, the polyethylene can be oxidized polyethylene.
In certain aspects, the carrier material can contain a metal oxide or metalloid oxide matrix (e.g., a silica matrix). The method can include contacting the asphaltene inhibitor with a metal oxide or metalloid oxide (e.g. silica) precursor to form a nanoparticle containing metal oxide or metalloid oxide (e.g. silica), and the asphaltene inhibitor. In certain aspects, the silica precursor can be a silicon alkoxide to form a silica matrix. In some particular aspects, the silica alkoxide can be propyl trimethoxysilane. In some aspects, the nanoparticle produced can have a core-shell structure comprising a core comprising the asphaltene inhibitor and a shell comprising the metal oxide or metalloid oxide (e.g. silica) matrix. In some aspects, the asphaltene inhibitor and the metal oxide or metalloid oxide (e.g. silica) precursor can be contacted in a solution. In certain aspects, the asphaltene inhibitor and/or the metal oxide or metalloid oxide (e.g. silica) precursor can be added to the solution at 50° C. to 90° C. In some aspects, the method further includes adding a catalyst to the solution. The catalyst can catalyze formation of the metal oxide or metalloid oxide (e.g. silica) from the metal oxide or metalloid oxide (e.g. silica) precursor. In some aspects, the catalyst can be triethanolamine, and/or ammonium hydroxide, preferably triethanolamine. In certain aspects, the solution can have a pH of 6 to 11, preferably 7.5 to 11, after addition of the catalyst. In some aspects, the method can include adding a surface active agent to the solution. In some aspects, the surface active agent used for preparing the metal oxide or metalloid oxide (e.g. silica), and the asphaltene inhibitor containing core-shell nanoparticle can be a cationic surfactant. In some aspects, the cationic surfactant can be a cetyltrimethylammonium halide, such as cetyltrimethylammonium chloride and/or cetyltrimethylammonium bromide, preferably cetyltrimethylammonium bromide. In some aspects, the surface active agent can be positioned in the core of the core-shell nanoparticle produced. In certain aspects, the method can include addition of a surface modifying agent to the solution, where the surface modifying agent can get bound and/or adhered to the outer surface of the shell and the nanoparticle. In some particular aspects, the surface modifying agent added to the solution can be (3-aminopropyl)triethoxysilane (APTES) and/or n-octadecyltrimethoxysilane and/or Phenyltrimethoxysilane, preferably (3-aminopropyl)triethoxysilane.
One aspect is directed to a well treatment composition containing a plurality of the nanoparticles of the present invention. The plurality of the nanoparticles can have an average size of 10 nm to 500 nm, preferably 50 nm to 400 nm. In some aspects, the well treatment composition can be a fluid. In some aspects, the well treatment composition can be a dispersion. In some aspects, the well treatment composition can further contain a solvent. The solvent can be water, salt water, an organic solvent, an acidic aqueous solution, low sulfate seawater, an aqueous sodium carbonate solution, a surfactant, or other flush fluid, or any combinations thereof. In some aspects, the plurality of the nanoparticles can be dispersed in the solvent. In certain aspects, the solvent can contain water. In certain aspects, the solvent can contain organic solvent. In some aspects, the organic solvent can contain aromatic hydrocarbons, such as C6-C15 aromatic hydrocarbons. In certain aspects, the organic solvent can contain toluene, xylene, C9 aromatic hydrocarbons, C10 aromatic hydrocarbons, or any combinations thereof. Commercially available organic solvent that can be used includes but is not limited to SHELLSOL A150 (C9-C10 aromatic hydrocarbon solvent) sold by Shell chemicals. The well treatment composition can be a controlled-release composition capable of releasing the asphaltene inhibitor over an extended period of time, such as at least for 10, 20, 30, 40, 50, 60, 70, 80, 90, 100, 200, 300, 400, 500, 1,000, 2,000, 3,000, or 4,000, days or more, or from 10 days to 500 days, or from 20 days to 365 days, or from 500 days to 2500 days, or from 500 days to 2000 days, or from 10 days to 10 years after well treatment. In certain aspects, well treatment composition containing 100 kilograms (kg) to 5000000 (kg), preferably, 2000 (kg) to 50000 kg (or any range or number therein such as 100, 200, 300, 400, 500, 600, 700, 800, 900, 1000, 2000, 3000, 4000, 5000, 6000, 7000, 8000, 9000, 10000, 20000, 30000, 40000, 50000, 60000, 70000, 80000, 90000, 100000, 200000, 300000, 400000, 500000, 600000, 700000, 800000, 900000, 1000000, 2000000, 3000000, 4000000, or 5000000) of the nanoparticles can be used to treat, such as via squeeze treatment, subterranean formations and/or wells for 1000 barrels to 200000000 barrels, preferably 300000 barrels to 8000000 barrels, of oil produced of oil produced (or any range or number therein such as 1000, 5000, 10000, 20000, 30000, 40000, 50000, 60000, 70000, 80000, 90000, 100000, 200000, 300000, 400000, 500000, 600000, 700000, 800000, 900000, 1000000, 2000000, 3000000, 4000000, 5000000, 6000000, 7000000, 8000000, 9000000, 10000000, or 20000000, 30000000, 40000000, 50000000, 60000000, 70000000, 80000000, 90000000, 100000000, 200000000).
Another aspect is directed to a method of treating a subterranean formation (e.g., a reservoir or an uncased well) or a wellbore. The method includes injecting the well treatment composition described herein, into a wellbore. The wellbore can intersect the subterranean formation. The subterranean formation can be a hydrocarbon formation. In some aspects, the treating can be squeeze treating the subterranean well formation or wellbore. In some aspects, the treating can be continuous treating or spear treating the subterranean well formation or wellbore.
In some aspects, an asphaltene inhibitor squeeze treatment can be performed by pushing a composition comprising the nanoparticle of the present invention into a producing formation and fixing the nanoparticle within the formation or near wellbore region materials. With respect to near wellbore region materials, non-limiting examples include gravel packs, sand, rock, etc., or any material in close proximity to the wellbore. In one aspect, a squeeze treatment can include any one of, any combination of, or all of (1) a pre-flush stage, which can include the injection of a volume of fluid that may contain chemicals, e.g., acids, chelating agents, surfactants, biocides, etc., to clean the production tubing and wellbore (preflush), (2) administration of the composition comprising the nanoparticle within the formation, and/or (3) administration of an overflush solution to further push the composition comprising the nanoparticle of the present invention into the formation. In certain aspects, the pre-flush fluid can contain a mutual solvent, a surfactant, an organic solvent, an asphaltene inhibitor (neat, e.g. without being attached to the carrier material), or any combinations thereof. In some aspects, the well can be shut in for a period of time after administration of the overflush solution. In certain aspects, the well can be shut in for 12 h to 36 h after administration of the overflush solution. In some aspects, spacer stages can be introduced between the stages, for example between the (1) pre-flush and (2) flush, and/or (2) flush and (3) over flush stages.
Also disclosed in the context of the present invention are aspects 1-53. Aspect 1 is a nanoparticle comprising a carrier material and an asphaltene inhibitor, wherein the asphaltene inhibitor is releasable from the carrier material, and wherein the nanoparticle has a size of 10 nanometers (nm) to 500 nm. Aspect 2 is the nanoparticle of aspect 1, having a size of 50 nm to 400 nm. Aspect 3 is the nanoparticle of any one of aspects 1 to 2, wherein the nanoparticle comprises 5 wt. % to 95 wt. %, preferably 20 wt. % to 80 wt. %, of the carrier material and 5 wt. % to 95 wt. %, preferably 20 wt. % to 80 wt. %, of the asphaltene inhibitor. Aspect 4 is the nanoparticle of any one of aspects 1 to 3, wherein the asphaltene inhibitor is physically entrapped within the carrier material and/or bound to the carrier material through an ionic bond, a covalent bond, a hydrogen bond, a van der Waals interaction or by adsorption onto a surface of the carrier material. Aspect 5 is the nanoparticle of aspect 4, wherein the asphaltene inhibitor is adsorbed onto the surface of the carrier material. Aspect 6 is the nanoparticle of any one of aspects 1 to 5, wherein at least a portion of the surface of the nanoparticle comprises a surface modifying agent. Aspect 7 is the nanoparticle of any one of aspects 1 to 6, wherein the carrier material comprises a silica matrix, a polymer matrix, a carbon matrix, a transition or post-transition metal oxide matrix, lipid matrix, wax matrix, a column 2 metal oxide matrix, a clay matrix, a metal organic framework (MOF) matrix, a zeolite matrix, a zeolite imidazolate framework (ZIF) matrix, a covalent organic framework (COF) matrix, or any combinations thereof. Aspect 8 is the nanoparticle of aspect 7, wherein the matrix is an open-celled porous matrix. Aspect 9 is the nanoparticle of any one of aspects 1 to 8, wherein the carrier material is a silica matrix (e.g., crystalline silica (e.g., α-quartz, β-quartz, α-tridymite, β-tridymite, α-cristobalite, β-cristobalite, keatite, coesite, stishovite, and/or moganite) or amorphous silica (e.g., diatomite silica, calcined silica, flux-calcined silica, fused silica, silica fume, or synthetic amorphous silica (e.g., fumed silica or precipitated silica)). Aspect 10 is the nanoparticle of aspect 9, wherein the silica matrix is an open-celled porous silica matrix, preferably having an average pore size of less than 2 nm (e.g., 0.5 to less than 2 nm), 2 nanometers (nm) to 2000 nm, 2 nm to 1000 nm, 2 nm to 500 nm, 2 nm to 100 nm, 2 nm to 50 nm, or any size or range therein (e.g., 2 nm, 5 nm, 10 nm, 15 nm, 20 nm, 25 nm, 30 nm, 35 nm, 40 nm, 45 nm, 50 nm, 55 nm, 60 nm, 65 nm, 70 nm, 75 nm, 80 nm, 85 nm, 90 nm, 95 nm, 100 nm, 200 nm, 300 nm, 400 nm, 500 nm, 600 nm, 700 nm, 800 nm, 900 nm, 1000 nm, 1100 nm, 1200 nm, 1300 nm, 1400 nm, 1500 nm, 1600 nm, 1700 nm, 1800 nm, 1900 nm, or 2000 nm). Aspect 11 is the nanoparticle of aspect 10, wherein at least a portion of the asphaltene inhibitor is comprised in the pores of the porous silica matrix. Aspect 12 is the nanoparticle of any one of aspects 1 to 11, wherein the nanoparticle has a core-shell structure comprising a core comprising the asphaltene inhibitor and a porous shell comprising the carrier material. Aspect 13 is the nanoparticle of aspect 12, wherein the nanoparticle has a diameter of 5 nm to 1000 nm, preferably, preferably 50 nm to 400 nm, or more preferably 250 nm to 350 nm, the thickness of the shell is 5 nm to 500 nm, preferably 50 nm to 150 nm (or any range or number therein, 5, 10, 15, 20, 25, 30, 35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90, 95, 100, 110, 120, 130, 140, 150, 160, 170, 180, 190, 200, 210, 220, 230, 240, 250, 260, 270, 280, 290, 300, 310, 320, 330, 340, 350, 360, 370, 380, 390, 400, 410, 420, 430, 440, 450, 460, 470, 480, 490, or 500), and/or wherein at least 90 wt. % of the core, based on the total weight of the core, comprises the asphaltene inhibitor. Aspect 14 is the nanoparticle of any one of aspects 12 to 13, wherein the shell comprises the asphaltene inhibitor on at least a portion of the shell surface and/or in the pores of the shell. Aspect 15 is the nanoparticle of any one of aspects 6 to 14, wherein the carrier material is a silica matrix, and the surface modifying agent is 3-Aminopropyltriethoxysilane and/or n-Octadecyltrimethoxysilane, preferably 3-Aminopropyltriethoxysilane, and the nanoparticle further comprises a cationic surfactant, preferably cetyltrimethylammonium Bromide (CTAB). Aspect 16 is the nanoparticle of any one of aspects 1 to 8 and 12 to 14, wherein the carrier material is a polymer matrix. Aspect 17 is the nanoparticle of aspect 16, wherein the polymer matrix comprises a polyolefin. Aspect 18 is the nanoparticle of aspect 17, wherein the polyolefin is a polyethylene, preferably an oxidized polyethylene. Aspect 19 is the nanoparticle of any one of aspects 16 to 18, wherein the polymer matrix has a melting point of 30° C. to 300° C., preferably 50° C. to 200° C. Aspect 20 is the nanoparticle of any one of aspects 1 to 19, wherein the asphaltene inhibitor is capable of being released from the nanoparticle over an extended period of time. Aspect 21 is the nanoparticle of any one of aspects 1 to 20, wherein 100 kilograms (kg) to 5000000 (kg), preferably, 2000 (kg) to 50000 kg (or any range or number therein such as 100, 200, 300, 400, 500, 600, 700, 800, 900, 1000, 2000, 3000, 4000, 5000, 6000, 7000, 8000, 9000, 10000, 20000, 30000, 40000, 50000, 60000, 70000, 80000, 90000, 100000, 200000, 300000, 400000, 500000, 600000, 700000, 800000, 900000, 1000000, 2000000, 3000000, 4000000, or 5000000) of the nanoparticles is capable of treating subterranean formations and/or wells for 1000 barrels to 200000000 barrels, preferably 300000 barrels to 8000000 barrels, of oil produced of oil produced (or any range or number therein such as 1000, 5000, 10000, 20000, 30000, 40000, 50000, 60000, 70000, 80000, 90000, 100000, 200000, 300000, 400000, 500000, 600000, 700000, 800000, 900000, 1000000, 2000000, 3000000, 4000000, 5000000, 6000000, 7000000, 8000000, 9000000, 10000000, or 20000000, 30000000, 40000000, 50000000, 60000000, 70000000, 80000000, 90000000, 100000000, 200000000). Aspect 22 is the nanoparticle of any one of aspects 1 to 21, wherein the asphaltene inhibitor is a dispersant, a threshold inhibitor, or a chemical that affects asphaltene formation, asphaltene deposition, and/or transportation behavior of asphaltene. Aspect 23 is the nanoparticle of any one of aspects 1 to 22, wherein the asphaltene inhibitor is also a surface modifying agent. Aspect 24 is the nanoparticle of aspect 23, wherein the asphaltene inhibitor is cationically charged asphaltnene inhibitors (e.g., imidazoline based), non-ionic asphaltene inhibitors (e.g., resin based), and/or anionically charged inhibitors (e.g., ester-based).
Aspect 25 is a well treatment composition comprising a plurality of the nanoparticles of any one of aspects 1 to 24. Aspect 26 is the well treatment composition of aspect 25, wherein the plurality of the nanoparticles has an average particle size of 10 nm to 500 nm, preferably 50 nm to 400 nm. Aspect 27 is the well treatment composition of any one of aspects 25 to 26, wherein the composition is a fluid. Aspect 28 is the well treatment composition of any one of aspects 25 to 27, wherein the well-treatment composition comprises 100 kilograms (kg) to 5000000 (kg), preferably, 2000 (kg) to 50000 kg (or any range or number therein such as 100, 200, 300, 400, 500, 600, 700, 800, 900, 1000, 2000, 3000, 4000, 5000, 6000, 7000, 8000, 9000, 10000, 20000, 30000, 40000, 50000, 60000, 70000, 80000, 90000, 100000, 200000, 300000, 400000, 500000, 600000, 700000, 800000, 900000, 1000000, 2000000, 3000000, 4000000, or 5000000) of the nanoparticles, and is capable of treating subterranean formations and/or wells for 1000 barrels to 200000000 barrels, preferably 300000 barrels to 8000000 barrels, of oil produced of oil produced (or any range or number therein such as 1000, 5000, 10000, 20000, 30000, 40000, 50000, 60000, 70000, 80000, 90000, 100000, 200000, 300000, 400000, 500000, 600000, 700000, 800000, 900000, 1000000, 2000000, 3000000, 4000000, 5000000, 6000000, 7000000, 8000000, 9000000, 10000000, or 20000000, 30000000, 40000000, 50000000, 60000000, 70000000, 80000000, 90000000, 100000000, 200000000). Aspect 29 is the well treatment composition of any one of aspects 25 to 28, further comprising water, a surfactant, or an organic solvent, or any combinations thereof. Aspect 30 is the well treatment composition of aspect 29, wherein the water comprises salt water, an acidic aqueous solution, a low sulfate seawater, or an aqueous sodium carbonate solution, or any combinations thereof.
Aspect 31 is a method of treating a subterranean formation or a wellbore, the method comprising injecting the composition of any one of aspects 25 to 30 into the wellbore, the wellbore intersecting the subterranean formation. Aspect 32 is the method of aspect 31, wherein treating is squeeze treating the subterranean formation or wellbore. Aspect 33 is the method of aspect 32, wherein squeeze treating comprises: (a) injecting a pre-flushing composition into the wellbore to displace fluids in the wellbore and/or to condition the subterranean formation; (b) subsequently injecting the composition of any one of aspects 25 to 30 into the wellbore under conditions sufficient such that the composition of any one of aspects 25 to 30 contacts the subterranean formation; and (c) subsequently injecting an over-flush composition into the wellbore to increase retention of the composition of any one of aspects 25 to 30 in the subterranean formation. Aspect 34 is the method of aspect 31, wherein treating is continuous treating or spear treating the subterranean formation or wellbore.
Aspect 35 is a method for making the nanoparticle of any one of aspects 1 to 24, the method comprising contacting the asphaltene inhibitor with the carrier material to form the nanoparticle. Aspect 36 is the method of aspect 35, wherein the carrier material comprises a polyethylene matrix and the method comprises: contacting polyethylene with the asphaltene inhibitor at a temperature above melting point of the polyethylene to form an emulsion comprising the polyethylene and the asphaltene inhibitor; and cooling the emulsion to form a nanoparticle comprising the polyethylene and asphaltene inhibitor. Aspect 37 is the method of aspect 36, wherein the polyethylene and the asphaltene inhibitor can be contacted to form a mixture having a temperature greater than the melting point of the polyethylene, and the mixture can be contacted with an immiscible solvent to form the emulsion, wherein a continuous phase of the emulsion comprises the immiscible solvent, and a discontinuous droplet phase of the emulsion comprises the polyethylene and asphaltene inhibitor. Aspect 38 is the method of aspect 37, wherein the immiscible solvent is water, acetic acid, butanol, ethylene glycol, acetyl acetone, or any combinations thereof, preferably water. Aspect 39 is the method of aspect 37 or 38, wherein a surface modifying agent is contacted with the immiscible solvent, before, during and/or after contacting the mixture with the immiscible solvent. Aspect 40 is the method of aspect 39, wherein the surface modifying agent is a non-ionic surfactant, an anionic surfactant, a cationic surfactant, an amphoteric surfactant, a zwitterionic surfactant, a block co-polymer, an organic compound, or any combinations thereof. Aspect 41 is the method of any one of aspects 39 to 40, wherein the surface modifying agent is sorbitan monooleate, sodium dodecylbenzene sulfonate, cetylpyridinium chloride, benzyldimethylhexadecyl-ammonium chloride, bi s(2-ethylhexyl)phosphate, or any combinations thereof. Aspect 42 is the method of aspect 35, wherein the carrier material comprises a silica matrix and the method comprises contacting the asphaltene inhibitor with a silica precursor to form a nanoparticle comprising silica and the asphaltene inhibitor. Aspect 43 is the method of aspect 42, wherein the silica precursor is a silicon alkoxide. Aspect 44 is the method of any one of aspects 42 to 43, wherein at least a portion of the asphaltene inhibitor in the nanoparticle is comprised within open celled pores of the silica matrix. Aspect 45 is the method of any one of aspects 42 to 44, wherein the nanoparticle has a core-shell structure comprising a core comprising the asphaltene inhibitor and a shell comprising the silica matrix. Aspect 46 is the method of any one of aspects 42 to 45, wherein the asphaltene inhibitor and the silica precursor is contacted in a solution. Aspect 47 is the method of aspect 46, further comprising adding a catalyst to the solution, wherein the catalyst catalyzes formation of the silica from the silica precursor. Aspect 48 is the method of aspect 47, wherein the catalyst is triethanolamine, and/or ammonium hydroxide, preferably triethanolamine. Aspect 49 is the method of any one of aspects 46 to 48, further comprising adding a surface active agent to the solution. Aspect 50 is the method of aspect 49, wherein the surface active agent is a cationic surfactant. Aspect 51 is the method of aspect 50, wherein the cationic surfactant is a cetyltrimethylammonium halide, such as cetyltrimethylammonium chloride and/or cetyltrimethylammonium bromide, preferably cetyltrimethylammonium bromide. Aspect 52 is the method of any one of aspects 42 to 51, further comprising adding a surface modifying agent comprising an alkyl siloxane with long alkyl chain, to the solution. Aspect 53 is the method of aspect 52, wherein the surface modifying agent comprises (3-Aminopropyl)triethoxysilane (APTES) and/or Phenyltrimethoxysilane.
In some embodiments, the asphaltene inhibitor in any of Aspects 1-53 can be a dispersant, a threshold inhibitor, or a chemical that affects asphaltene formation, asphaltene deposition, and/or transportation behavior of asphaltene.
The term “capable of being released” as it relates to the subterranean well treatment composition means that, under conditions of use, e.g., in a subterranean well, the asphaltene inhibitor can dissociate, desorb, hydrolyze, becomes chemically unbound, or becomes otherwise separated from the carrier material matrix of the nanoparticle and available for use for its intended purpose, e.g., prevention in formation, reduction in formation, and/or removal of asphaltene deposition in a subterranean well.
The term “asphaltene inhibitor” can include a chemical(s) compound, combination of chemical compounds, and/or a composition comprising a chemical compound(s) that prevents or reduces asphaltene precipitation from crude oil, prevents or reduces deposition of asphaltene on surfaces in contact with crude oil, and/or helps in removal of an asphaltene deposit already formed on a surface, or any combinations thereof.
The term “controlled release over an extended period of time” relates to the release rate of the asphaltene inhibitor from the nanoparticle. It can indicate that the asphaltene inhibitor is in an environment of use such as, e.g., a subterranean well, released from the nanoparticle over a longer period of time than if asphaltene inhibitor were not bound, adsorbed or otherwise adhered to the carrier material of the nanoparticle of the present invention.
The terms “formation fluid” or “formation fluids” includes liquids and gases present in a formation. Non-limiting examples, of formation fluid include hydrocarbon liquids and gases, water, salt water, sulfur and/or nitrogen containing hydrocarbons, inorganic liquids and gases and the like.
The terms “about” or “approximately” are defined as being close to as understood by one of ordinary skill in the art. In non-limiting embodiment, the terms are defined to be within 10%, preferably within 5%, more preferably within 1%, and most preferably within 0.5%.
The terms “wt. %,” “vol. %,” or “mol. %” refers to a weight, volume, or molar percentage of a component, respectively, based on the total weight, the total volume of material, or total moles, that includes the component. In a non-limiting example, 10 grams of component in 100 grams of the material is 10 wt. % of component.
The term “substantially” and its variations are defined to include ranges within 10%, within 5%, within 1%, or within 0.5%.
The terms “inhibiting close” or “reducing” or “preventing” or “avoiding” or any variation of these terms, when used in the claims and/or the specification includes any measurable decrease or complete inhibition to achieve a desired result. The term “effective,” as that term is used in the specification and/or claims, means adequate to accomplish a desired, expected, or intended result.
The use of the words “a” or “an” when used in conjunction with any of the terms “comprising,” “including,” “containing,” or “having” in the claims, or the specification, may mean “one,” but it is also consistent with the meaning of “one or more,” “at least one,” and “one or more than one.”
The nanoparticles and methods of the present invention can “comprise,” “consists essentially of,” or “consists of” particular elements, ingredients, components, compositions, etc. disclose throughout the specification. With respect to the transitional phrase “consisting essentially of,” in one non-limiting aspect a basic and novel characteristic of the nanoparticle(s) of the present invention is/are their ability to deliver a controllable release asphaltene inhibitor over an extended period of time during use (e.g., in subterranean wells) and/or the nanoparticles can be delivered through a squeeze treatment process.
The words “comprising” (and any form of comprising, such as “comprise” and “comprises”), “having” (and any form of having, such as “have” and “has”), “including” (and any form of including, such as “includes” and “include”) or “containing” (and any form of containing, such as “contains” and “contain”) are inclusive or open-ended and do not exclude additional, on recited elements or method steps.
Other objects, features and advantages of the present invention will become apparent from the following figures, a detailed description, and examples. It should be understood, however, that the figures, detailed description, and examples, while indicating specific embodiments of the invention, are given by way of illustration only, and are not meant to be a limiting. Additionally, it is contemplated that changes and modifications within the spirit and scope of the invention will become apparent to those skilled in the art from this detailed description.
A discovery has been made, which provides nanoparticulate carriers for asphaltene inhibitors. These nanoparticulate carriers can provide extended or sustained release of an asphaltene inhibitor in an environment of use, e.g., in a subterranean oil, gas well, water well, or any subterranean reservoir. Controlled release of such additives over an extended period of time decreases or eliminates the need to retreat wells or subterranean formations (e.g., hydrocarbon reservoirs) with the asphaltene inhibitors, providing a cost and labor savings, and less environmental risks. The discovery is premised on physically entrapping the asphaltene inhibitor within a carrier material matrix and/or bonding or adsorbing the asphaltene inhibitor to the carrier material matrix of the nanoparticles. The carrier material matrix can be silica matrix, a polymer matrix, a carbon matrix, a transition or post-transition metal oxide matrix, lipid matrix, wax matrix, a column 2 metal oxide matrix, or any combinations thereof.
The invention provides an elegant way to provide a cost-and labor-effective methods to deliver asphaltene inhibitor containing nanoparticles to wells so that they release the asphaltene inhibitors over a long period of time, in a manner that reduces or eliminates the need to retreat wells with the inhibitor. The invention also provides effective methods to deliver asphaltene inhibitor to fluids used to produce fluids (e.g., oil and gas) from subterranean formations. For example, delivery of asphaltene inhibitor to drilling fluid additives (mud additives), enhanced oil recovery (EOR) fluids, or the like.
The structure of the nanoparticles of the present invention also allows for their use in squeeze treatment processes rather than the typical approach of continuous treatment processes. An advantage of squeeze treatment processes when compared with continuous treatment processes for asphaltene inhibitors is that the squeeze treatment processes can more fully protect the subterranean formations (e.g., reservoirs) and/or wells (e.g., oil, gas and water wells). In some aspects, this more robust protection can be attributed to (1) the sustained release of the asphaltene inhibitor(s) from the carrier matrix materials of the nanoparticles of the present invention, (2) the size of the nanoparticles, which allows them to be placed into and retained in the subterranean formations and/or wells, and/or (3) the carrier matrix materials remaining stable or intact for prolonged periods of time (10, 20, 30, 40, 50, 100, 200, 300, 400, 500, 1,000, 2000, 3,000, or 4,000 days or longer) when introduced into the subterranean formations and/or wells. Another advantage is that the costs and infrastructure associated with continuous injection into the subterranean formations and/or wells can be avoided. The structure of the nanoparticles of the present invention advantageously opens up the possibility of commercial use of squeeze treatment of subterranean formations and/or wells with asphaltene inhibitors.
These and other non-limiting aspects of the present invention are discussed in further detail in the following sections.
The asphaltene inhibitor containing nanoparticle of the present invention can contain a carrier material and the asphaltene inhibitor attached to the carrier material such that small, but effective, amounts of asphaltene inhibitor can be removed from the nanoparticle over a period of time. The nanoparticle can contain 5 wt. % to 95 wt. %, or equal to any one of, at least any one of, or between any two of 5, 10, 15, 20, 25, 30, 35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90 and 95 wt. % of the carrier material and 5 wt. % to 95 wt. %, or equal to any one of, at least any one of, or between any two of 5, 10, 15, 20, 25, 30, 35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90 and 95 wt. % of the asphaltene inhibitor. The weight ratio of the carrier material and the asphaltene inhibitor in the nanoparticle can be 5:95 to 95:5, or equal to any one of, at least any one of, or between any two of 5:95, 10:90, 15:85, 20:80, 25:75, 30:70, 35:65, 40:60, 45:55, 50:50, 55:45, 60:40, 65:35, 70:30, 75:25, 80:20, 85:15, 90:10, and 95:5.
The asphaltene inhibitor can be capable of being released from the nanoparticle in a controlled manner over an extended period of time, e.g., for at least 10, 20, 30, 40, 50, 60, 70, 80, 90, 100, 200, 300, 400, 500, 1,000, 2,000, 3,000, or 4,000, days or more, or from 10 days to 500 days, or from 20 days to 365 days, or from 500 days to 2500 days, or from 500 days to 2000 days, or from 10 days to 10 years after well treatment. In certain aspects, 100 kilograms (kg) to 5000000 (kg), preferably, 2000 (kg) to 50000 kg (or any range or number therein such as 100, 200, 300, 400, 500, 600, 700, 800, 900, 1000, 2000, 3000, 4000, 5000, 6000, 7000, 8000, 9000, 10000, 20000, 30000, 40000, 50000, 60000, 70000, 80000, 90000, 100000, 200000, 300000, 400000, 500000, 600000, 700000, 800000, 900000, 1000000, 2000000, 3000000, 4000000, or 5000000) of the nanoparticles can be used to treat, such as via squeeze treatment, subterranean formations and/or wells for 1000 barrels to 200000000 barrels, preferably 300000 barrels to 8000000 barrels, of oil produced of oil produced (or any range or number therein such as 1000, 5000, 10000, 20000, 30000, 40000, 50000, 60000, 70000, 80000, 90000, 100000, 200000, 300000, 400000, 500000, 600000, 700000, 800000, 900000, 1000000, 2000000, 3000000, 4000000, 5000000, 6000000, 7000000, 8000000, 9000000, 10000000, or 20000000, 30000000, 40000000, 50000000, 60000000, 70000000, 80000000, 90000000, 100000000, 200000000).
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The nanoparticle 100, 200, 300, 400 can have a size (e.g., average diameter) of 5 nm to 1000 nm, preferably 50 nm to 400 nm (or any range or number therein such as 5, 10, 15, 20, 25, 30, 35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90, 95, 100, 200, 300, 400, 500, 600, 700, 800, 900, or 1000). In certain aspects, core 402 of the core-shell nanoparticle 400 can have a size (e.g., average diameter) of 50 nm to 500 nm, preferably 250 nm to 350 nm or equal to any one of, at least any one of, or between any two of 50, 60, 70, 80, 90, 100, 110, 120, 130, 140, 150, 160, 170, 180, 190, 200, 210, 220, 230, 240, 250, 260, 270, 280, 290, 300, 310, 320, 330, 340 350, 360, 370, 380, 390, 400, 410, 420, 430, 440, 450, 460, 470, 480, 490, or 500 nm. In certain aspects, the shell 401 of the core-shell nanoparticle 400 can have a thickness of 5 nm to 500 nm, preferably 50 nm to 150 nm (or any range or number therein, 5, 10, 15, 20, 25, 30, 35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90, 95, 100, 110, 120, 130, 140, 150, 160, 170, 180, 190, 200, 210, 220, 230, 240, 250, 260, 270, 280, 290, 300, 310, 320, 330, 340, 350, 360, 370, 380, 390, 400, 410, 420, 430, 440, 450, 460, 470, 480, 490, or 500), over the core 402. In some aspects, at least 90 wt. %, such as 90 wt. % to 100 wt. %, or equal to any one of, at least any one of, or between any two of 90, 91, 92, 93, 94, 95, 96, 97, 98, 99, 99.5, 99.8 and 100 wt. % of the core 402, based on the total weight of the core 402, can be comprised of the asphaltene inhibitor. In certain aspects, the weight ratio of the core 402 and the shell 401 in the core-shell nanoparticle 400 can be 1:1 to 50:1, or equal to any one of, at least any one of, or between any two of 1:1, 2:1, 3:1, 4:1, 5:1, 6:1, 7:1, 8:1, 9:1, 10:1, 15:1, 20:1, 25:1, 30:1, 35:1, 40:1, 45:1 and 50:1. Scanning electron microscopy (SEM) and transmission electron microscopy (TEM) can be used to characterize particle size. In some aspects, in aqueous solutions, nanoparticle size can be measured using laser particle size analysis. In some aspects, in organic solutions, nanoparticle size can be measured with imaging of the bulk and/or imaging of dried particles. In some aspects, SEM and TEM imaging can entail drying and gold sputter coating.
In other aspects of the present invention, the nanoparticles can have a size such that the ratio of the nanoparticle size to the pore throat size is ⅓ to 1/7, preferably about ¼ to ⅙, or more preferably about ⅕.
In certain aspects, the shape of the nanoparticles of the present invention can be substantially or completely spherical. Other shapes are also contemplated such as cubic, pyramidal, oval, random, etc.
The carrier material of the nanoparticle, such as of the nanoparticle 100, 200, 300, 400 can contain a carrier material matrix. In certain aspects, the carrier material matrix can be silica matrix, a polymer matrix, a carbon matrix, a transition or post-transition metal oxide matrix, lipid matrix, wax matrix, a column 2 metal oxide matrix, a clay, a metal organic framework (MOF), a zeolite, a zeolite imidazolate framework (ZIF), a covalent organic framework (COF), or any combinations thereof. In some aspects, the carrier material can contain a silica matrix. In some aspects, the carrier material of the nanoparticles, such as of the nanoparticles 100, 200, 300, 400 can contain silica matrix. In some aspects, the silica matrix can be a porous silica matrix. In some aspects, the silica matrix can be an open-celled porous silica matrix. The open-celled porous silica can be microporous, mesoporous or macroporous silica. The silica can be crystalline silica (e.g., α-quartz, β-quartz, α-tridymite, β-tridymite, α-cristobalite, β-cristobalite, keatite, coesite, stishovite, and/or moganite). The silica can be amorphous silica (e.g., diatomite silica, calcined silica, flux-calcined silica, fused silica, silica fume, or synthetic amorphous silica (e.g., fumed silica or precipitated silica)). In some preferred aspects, fused silica and fumed silica can be used. In some aspects, the open-celled porous silica can be mesoporous silica. In some particular aspects, the open-celled porous silica matrix can contains pores having an average size of 0.1 nm to 200 nm, or 2 nm to 50 nm, or equal to any one of, at least any one of, or between any two of 0.1, 0.5, 1, 2, 5, 10, 15, 20, 25, 30, 35, 40, 45, 50, 100, 150 and 200 nm. In some aspects, the average pore size of the open-celled porous silica can be nanometers 2 (nm) to 2000 nm, 2 nm to 1000 nm, 2 nm to 500 nm, 2 nm to 100 nm, 2 nm to 50 nm, or any size or range therein (e.g., 2 nm, 5 nm, 10 nm, 15 nm, 20 nm, 25 nm, 30 nm, 35 nm, 40 nm, 45 nm, 50 nm, 55 nm, 60 nm, 65 nm, 70 nm, 75 nm, 80 nm, 85 nm, 90 nm, 95 nm, 100 nm, 200 nm, 300 nm, 400 nm, 500 nm, 600 nm, 700 nm, 800 nm, 900 nm, 1000 nm, 1100 nm, 1200 nm, 1300 nm, 1400 nm, 1500 nm, 1600 nm, 1700 nm, 1800 nm, 1900 nm, or 2000 nm). In some aspects, the nanoparticle can contain open-celled porous silica matrix and at least a portion of the asphaltene inhibitor in the nanoparticle can be contained in the pores of the open-celled porous silica matrix. For example, in certain aspects, the carrier material 101, 201, 301 of the nanoparticle 100, 200, 300, can contain open celled porous silica matrix, and at least a portion of the asphaltene inhibitors 102, 202, 302 in the nanoparticle 100, 200, 300 can be positioned inside the open celled pores of the silica matrix 101, 201, 301. In certain aspects, the carrier material in the shell 401 of the core-shell nanoparticle 400, can contain open celled porous silica matrix. In some aspects, the shell 401 can further contain an asphaltene inhibitor and at least a portion of the asphaltene inhibitor in the shell can be contained in the open celled pores of the silica in the shell. In certain aspects, the silica containing nanoparticle, can be free of, or essentially free of, or contains less than 1 wt. %, such as less than 0.5 wt. %, such as less than 0.1 wt. %, such as less than 0.05 wt. %, such as less than 0.01 wt. %, of a metal such as column 2 metal, column 14 metal and/or a transition metal, such as beryllium (Be) magnesium (Mg), calcium (Ca), strontium (Sr), barium (Ba), radium (Ra), tin (Sn), lead (Pb), and/or Germanium (Ge).
In some aspects, the carrier material of the nanoparticles, such as of the nanoparticles 100, 200, 300, 400 can contain a polymer matrix. In some aspects, the polymer matrix can contain a polymer such as polyolefin, paraffin wax, fatty glyceride, polyacrylamide, polystyrene, epoxide, polyester, or any combinations thereof. In certain aspects, the polymer matrix can contain polyolefin. In some aspects, the polyolefin can be polyethylene. In certain aspects, the polyethylene can be oxidized polyethylene. The oxidized polyethylene can be polymers that are obtained by treatment of linear or branched polyethylenes with oxygen and/or oxygen containing gases. In certain aspects, melts of linear or branched polyethylenes can be treated with the oxygen and/or oxygen containing gases to obtain the oxidized polyethylene. The oxidized polyethylene can contain oxygen containing functional groups such as carboxyl, carbonyl, and/or hydroxyl groups in the polymer molecule. In some particular aspects, the polymer, such as the polyethylene, such as oxidized polyethylene can have a weight average molecular weight (Mw) of 2000 g/mol. to 20000 g/mol, or equal to any one of, at least any one of, or between any two of 2000, 3000, 4000, 5000, 6000, 7000, 8000, 9000, 10000, 11000, 12000, 13000, 14000, 15000, 16000, 17000, 18000, 19000, and 20000 g/mol, as measured by gel permeation chromatography (GPC). In some particular aspects, the polymer, such as the polyethylene, such as oxidized polyethylene can have melting point of a 30° C. to 300° C., or equal to any one of, at least any one of, or between any two of 30, 50, 75, 100, 125, 150, 175, 200, 225, 250, 275 and 300° C. Commercially available oxidized polyethylene that can be used includes but are not limited to Epolene E-14 and Epolene E-20 sold by Westlake Chemical. In certain aspects, i) polyethylene, such as oxidized polyethylene can form the bulk of the particle, and ii) the asphaltene inhibitor can be impregnated within, e.g. distributed through the bulk of the particle, and can be bound or otherwise adhered to an outer surface of the particle. In certain aspects, polyethylene, such as oxidized polyethylene containing nanoparticles can have a shape of the nanoparticle 300.
In some aspects, the carrier material of the nanoparticles, such as of the nanoparticles 100, 200, 300, 400 can contain a transition metal oxide matrix. Non-limiting examples of transition metals can include scandium (Sc), titanium (Ti), vanadium (V), chromium (Cr), manganese (Mn), iron (Fe), cobalt (Co), nickel (Ni), copper (Cu), zinc (Zn), yttrium (Y), zirconium (Zr), niobium (Nb), molybdenum (Mo), technetium (Tc), ruthenium (Ru), rhodium (Rh), palladium (Pd), silver (Ag), cadmium (Cd), hafnium (Hf), tantalum (Ta), tungsten (W), rhenium (Re), osmium (Os), iridium (Ir), platinum (Pt), gold (Au), mercury (Hg), rutherfordium (Rf), dubnium (Db), seaborgium (Sg), bohrium (Bh), hassium (Hs), meitnerium (Mt), darmstadtium (Ds), roentgenium (Rg) and/or copernicum (Cn). In certain aspects, the transition metal can be titanium. In certain aspects, the carrier material can contain porous titanium oxide matrix, such as open-celled porous titanium oxide matrix. The porous titanium oxide matrix, such as open-celled porous titanium oxide matrix can contain pores having an average size of 2 nm to 50 nm or equal to any one of, at least any one of, or between any two of 2, 5, 10, 15, 20, 25, 30, 35, 40, 45 and 50 nm. In certain aspects, the transition metal oxide containing nanoparticles can be free of, or essentially free of, or contains less than 1 wt. %, such as less than 0.5 wt. %, such as less than 0.1 wt. %, such as less than 0.05 wt. %, such as less than 0.01 wt. %, of silica.
In some aspects, the carrier material of the nanoparticles, such as of the nanoparticles 100, 200, 300, 400 can contain carbon matrix. In some aspects, the carbon matrix can be a porous carbon matrix. In some aspects, the carbon matrix can be an open-celled porous carbon matrix. In some particular aspects, the open-celled porous carbon matrix can contain pores having an average size of 2 nm to 50 nm or equal to any one of, at least any one of, or between any two of 2, 5, 10, 15, 20, 25, 30, 35, 40, 45 and 50 nm.
In certain aspects, the carrier material of the nanoparticles, such as of the nanoparticles 100, 200, 300, 400, can contain a lipid matrix. In certain aspects, the carrier material of the nanoparticles, such as of the nanoparticles 100, 200, 300, 400, can contain a wax matrix. In certain aspects, the career material of the nanoparticles, such as of the nanoparticles 100, 200, 300, 400, can contain a column 2 metal oxide matrix. Non-limiting examples of column 2 metals include beryllium (Be) magnesium (Mg), calcium (Ca), strontium (Sr), barium (Ba), or radium (Ra). In certain aspects, the column 2 metal oxide containing nanoparticles can be free of, or essentially free of, or contains less than 1 wt. %, such as less than 0.5 wt. %, such as less than 0.1 wt. %, such as less than 0.05 wt. %, such as less than 0.01 wt. %, of silica.
In some aspects, the carrier material of the nanoparticles, such as of the nanoparticles 100, 200, 300, 400 can contain a clay matrix. In some aspects, the clay matrix can be a porous clay matrix. In some aspects, the clay matrix can be an open-celled porous clay matrix. In some particular aspects, the open-celled porous clay matrix can contain pores having an average size of 2 nanometers (nm) to 2000 nm, 2 nm to 1000 nm, 2 nm to 500 nm, 2 nm to 100 nm, 2 nm to 50 nm, or any size or range therein (e.g., 2 nm, 5 nm, 10 nm, 15 nm, 20 nm, 25 nm, 30 nm, 35 nm, 40 nm, 45 nm, 50 nm, 55 nm, 60 nm, 65 nm, 70 nm, 75 nm, 80 nm, 85 nm, 90 nm, 95 nm, 100 nm, 200 nm, 300 nm, 400 nm, 500 nm, 600 nm, 700 nm, 800 nm, 900 nm, 1000 nm, 1100 nm, 1200 nm, 1300 nm, 1400 nm, 1500 nm, 1600 nm, 1700 nm, 1800 nm, 1900 nm, or 2000 nm). Non-limiting examples of clays that can be used in the context of the present invention include (1) kaolin-serpentine (kaolinite, halloysite, lizardite, chrysotile), (2) pyrophyllite-talc, (3) mica (illite, glauconite, celadonite), (4) vermiculite, (5) smectite (montmorillonite, nontronite, saponite), (6) chlorite (sudoite, clinochlore, chamosite), (7) sepiolite-palygorskite, (8) interstratified clay minerals (e.g., rectorite, corrensite, tosudite), and/or (9) allophane-imogolite. In some particular embodiments, the clay can be a halloysite.
In some aspects, the carrier material of the nanoparticles, such as of the nanoparticles 100, 200, 300, 400 can contain a metal organic framework (MOF) matrix. In some aspects, the MOF matrix can be a porous MOF matrix. In some aspects, the MOF matrix can be an open-celled porous MOF matrix. In some particular aspects, the open-celled porous MOF matrix can contain pores having an average size of 2 nanometers (nm) to 2000 nm, 2 nm to 1000 nm, 2 nm to 500 nm, 2 nm to 100 nm, 2 nm to 50 nm, or any size or range therein (e.g., 2 nm, 5 nm, 10 nm, 15 nm, 20 nm, 25 nm, 30 nm, 35 nm, 40 nm, 45 nm, 50 nm, 55 nm, 60 nm, 65 nm, 70 nm, 75 nm, 80 nm, 85 nm, 90 nm, 95 nm, 100 nm, 200 nm, 300 nm, 400 nm, 500 nm, 600 nm, 700 nm, 800 nm, 900 nm, 1000 nm, 1100 nm, 1200 nm, 1300 nm, 1400 nm, 1500 nm, 1600 nm, 1700 nm, 1800 nm, 1900 nm, or 2000 nm). MOFs can include compounds having metal ions or clusters coordinated to organic molecules to form one-, two-, or three-dimensional structures that can be porous. In general, it is possible to tune the properties of MOFs for specific applications using methods such as chemical or structural modifications. One approach for chemically modifying a MOF is to use a linker that has a pendant functional group for post-synthesis modification. Non-limiting examples of MOFs that can be used in the context of the present invention include IRMOF-3, MOF-69A, MOF-69B, MOF-69C, MOF-70, MOF-71, MOF-73, MOF-74, MOF-75, MOF-76, MOF-77, MOF-78, MOF-79, MOF-80, DMOF-1-NH2, UMCM-1-NH2, and MOF-69-80.
In some aspects, the carrier material of the nanoparticles, such as of the nanoparticles 100, 200, 300, 400 can contain a zeolite matrix. In some aspects, the zeolite matrix can be a porous zeolite matrix. In some aspects, the zeolite matrix can be an open-celled porous zeolite matrix. In some particular aspects, the open-celled porous zeolite matrix can contain pores having an average size of 2 nanometers (nm) to 2000 nm, 2 nm to 1000 nm, 2 nm to 500 nm, 2 nm to 100 nm, or 2 nm to 50 nm, or any size or range therein (e.g., 2 nm, 5 nm, 10 nm, 15 nm, 20 nm, 25 nm, 30 nm, 35 nm, 40 nm, 45 nm, 50 nm, 55 nm, 60 nm, 65 nm, 70 nm, 75 nm, 80 nm, 85 nm, 90 nm, 95 nm, 100 nm, 200 nm, 300 nm, 400 nm, 500 nm, 600 nm, 700 nm, 800 nm, 900 nm, 1000 nm, 1100 nm, 1200 nm, 1300 nm, 1400 nm, 1500 nm, 1600 nm, 1700 nm, 1800 nm, 1900 nm, or 2000 nm). Non-limiting examples of zeolites that can be used in the context of the present invention include Y-zeolites, beta zeolites, mordenite zeolites, ZSM-5 zeolites, and ferrierite zeolites. Zeolites may be obtained from a commercial manufacturer such as Zeolyst (Valley Forge, Pa., U.S.A.).
In some aspects, the carrier material of the nanoparticles, such as of the nanoparticles 100, 200, 300, 400 can contain a zeolite imidazole framework (ZIF) matrix. In some aspects, the ZIF matrix can be a porous ZIF matrix. In some aspects, the ZIF can be an open-celled porous ZIF matrix. In some particular aspects, the open-celled porous ZIF matrix can contain pores having an average size of 2 nanometers (nm) to 2000 nm, 2 nm to 1000 nm, 2 nm to 500 nm, 2 nm to 100 nm, or 2 nm to 50 nm, or any size or range therein (e.g., 2 nm, 5 nm, 10 nm, 15 nm, 20 nm, 25 nm, 30 nm, 35 nm, 40 nm, 45 nm, 50 nm, 55 nm, 60 nm, 65 nm, 70 nm, 75 nm, 80 nm, 85 nm, 90 nm, 95 nm, 100 nm, 200 nm, 300 nm, 400 nm, 500 nm, 600 nm, 700 nm, 800 nm, 900 nm, 1000 nm, 1100 nm, 1200 nm, 1300 nm, 1400 nm, 1500 nm, 1600 nm, 1700 nm, 1800 nm, 1900 nm, or 2000 nm). ZIFs are a class of metal-organic frameworks (MOFs) that can be topologically isomorphic with zeolites. Non-limiting examples of ZIFs that can be used in the context of the present invention include ZIF-1, ZIF-2, ZIF-3, ZIF-4, ZIF-5, ZIF-6, ZIF-7, ZIF-8, ZIF-9, ZIF-10, ZIF-11, ZIF-12, ZIF-14, ZIF-60, ZIF-62, ZIF-64, ZIF-65, ZIF-67, ZIF-68, ZIF-69, ZIF-70, ZIF-71, ZIF-72, ZIF-73, ZIF-74, ZIF-75, ZIF-76, ZIF-77, ZIF-78, ZIF-79, ZIF-80, ZIF-81, ZIF 82, ZIF-86, ZIF-90, ZIF-91, ZIF-92, ZIF-93, ZIF-95, ZIF-96, ZIF-97, ZIF-100 and hybrid ZIFs, such as ZIF-7-8, ZIF-8-90.
In some aspects, the carrier material of the nanoparticles, such as of the nanoparticles 100, 200, 300, 400 can contain a covalent organic framework (COF). In some aspects, the COF matrix can be a porous COF matrix. In some aspects, the COF can be an open-celled porous COF matrix. In some particular aspects, the open-celled porous COF matrix can contain pores having an average size of 2 nanometers (nm) to 2000 nm, 2 nm to 1000 nm, 2 nm to 500 nm, 2 nm to 100 nm, 2 nm to 50 nm, or any size or range therein (e.g., 2 nm, 5 nm, 10 nm, 15 nm, 20 nm, 25 nm, 30 nm, 35 nm, 40 nm, 45 nm, 50 nm, 55 nm, 60 nm, 65 nm, 70 nm, 75 nm, 80 nm, 85 nm, 90 nm, 95 nm, 100 nm, 200 nm, 300 nm, 400 nm, 500 nm, 600 nm, 700 nm, 800 nm, 900 nm, 1000 nm, 1100 nm, 1200 nm, 1300 nm, 1400 nm, 1500 nm, 1600 nm, 1700 nm, 1800 nm, 1900 nm, or 2000 nm). Covalent organic frameworks (COFs) can include periodic two- and three-dimensional (2D and 3D) polymer networks with high surface areas, low densities, and designed structures. COFs are porous, and crystalline, and made entirely from light elements (H, B, C, N, and O). Non-limiting examples of COFs that can be used in the context of the present invention include COF-1, COF-102, COF-103, PPy-COF 3 COF-102-C12, COF-102-allyl, COF-5, COF-105, COF-108, COF-6, COF-8, COF-10, COF-11 A, COF-14 A, COF-16 A, OF-18 A, TP-COF 3, Pc-PBBA, NiPc-PBBA, 2D-NiPc-BTDA COF, NiPc COF, BTP-COF, HHTP-DPB, COF-66, ZnPc-Py, ZnPc-DPB COF, ZnPc-NDI COF, ZnPc-PPE COF, CTC-COF, H2P-COF, ZnP-COF, CuP-COF, COF-202, CTF-1, CTF-2, COF-300, COF-LZU, COF-366, COF-42 and COF-43.
The asphaltene inhibitors can be physically entrapped within and/or detachably attached, e.g. chemically bonded, adsorbed, or otherwise adhered to the carrier material. In certain aspects, the asphaltene inhibitors can be physically entrapped within the carrier material. In certain aspects, the asphaltene inhibitors can be detachably attached, e.g. chemically bonded, adsorbed, or otherwise adhered to the carrier material. The asphaltene inhibitor can be chemically bonded through an ionic bond, a covalent bond, a hydrogen bond, or a van der Waals interaction with the carrier material. Adhesion to the nanoparticle can be through absorption or adsorption onto the particle. The asphaltene inhibitor can be separated from the nanoparticle and the carrier material in response to a stimulus (e.g., formation fluid, water, dilution, and/or pressure).
The asphaltene inhibitor used in the context of the present invention can be an asphaltene inhibitor known in the art. Generally, asphaltene inhibitors can help interfere with the precipitation and/or flocculation of asphaltene aggregates, which can help reduce or prevent the aggregates from depositing. In some aspects, the asphaltene inhibitor can be a dispersant, a threshold inhibitor, or a chemical that affects asphaltene formation, asphaltene deposition, and/or transportation behavior of asphaltene, or any combination thereof. Combinations of asphaltene inhibitors can be used such that the nanoparticle can include 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, or more different asphaltene inhibitors. In some particular aspects, the nanoparticles of the present invention can include a combination of asphaltene inhibitors such as dispersants and another non-dispersant inhibitor. In some aspects, the combination of asphaltene inhibitors can include imidiazoline-based inhibitors and resin-based inhibitors. In some aspects, the asphaltene inhibitor can have a dual effect. For example, the asphaltene inhibitor can be capable of acting as an asphaltene inhibitor and as a surface modifying agent or a surfactant, non-limiting examples of which include cationically charged asphaltnene inhibitors (e.g., imidazoline based), non-ionic asphaltene inhibitors (e.g., resin based), and/or anionically charged inhibitors (e.g., ester-based).
In certain aspects, the asphaltene inhibitor can be selected from aliphatic sulphonic acids; alkyl aryl sulphonic acids; aryl sulfonates; lignosulfonates; alkylphenol resins; aldehyde resins; sulfonated resins; polyolefin esters; polyolefin imides; polyolefin esters with alkyl, alkylenephenyl or alkylenepyridyl functional groups; polyolefin amides; polyolefin amides with alkyl, alkylenephenyl or alkylenepyridyl functional groups; polyolefin imides with alkyl, alkylenephenyl or alkylenepyridyl functional groups; alkenyl/vinyl pyrrolidone copolymers; graft polymers of polyolefins with maleic anhydride or vinyl imidazole; hyperbranched polyester amides; polyalkoxylated asphaltenes, amphoteric fatty acids, salts of alkyl succinates, sorbitan monooleate, polyisobutylene succinic anhydride, nonylphenol formaldehyde, nonylphenol formaldehyde resin, fatty acid amine condensate, or any combinations thereof. Commercially available asphaltene inhibitor can be used includes but are not limited to FLOTREAT DF 267 from Clariant, FLOTREAT DF 15980 from Clariant, FATHOM XT SUB SEA525 from Baker Hughes, ASPH16507A from NALCO Champion and ASI 1262 from Total Additives. In certain aspects, one or more asphaltene inhibitor can be excluded.
In certain aspects, the asphaltene inhibitor that can be used in the context of the present invention can include a dispersant. Asphaltene dispersants can help control asphaltene deposition. Such dispersants typically include a polar group (due to the presence of hetero-atoms like oxygen, nitrogen, and/or phosphorous) which attach to the surface of asphaltenes, and an alkyl group which can reduce or prevent the adhesion of asphaltene nanoaggregates. These two groups can interact with aggregated asphaltenes and with the help of a long alkyl tail they are capable of changing the polarity of the outer surface of aggregates. Therefore, the aggregates can have properties closer to those of crude oil and are more capable of remaining dispersed in the crude oil. Non-limiting examples of dispersants that can be used in the context of the present invention can be found in at least: U.S. Pat. No. 9,921,205; US Patent Application Publication Nos. 20040039125, 20040050752, 20040163995, 20040232042, 20040232043, 20040232044, 20040238404, 20050082231, 20050091915, 20060079434, 20060096757, and 20060096758; International Patent Applications Nos. 200174966, 2004033602, 2005010126, 2005054321, and 2006047745; Russian Patent Nos. 2172817, 2173320, 2185412, 2220999, 2223294, 2237799, 2250247, 2261887, and 2261983; Canadian Patent No. 2326288; European Patent No. 1091085; European Patent Application No. 2006795579; and Mexican Patent Application No. 2001013139, the contents of each of which are incorporated by reference into the present application. Some specific non-limiting examples include:
Some specific non-limiting examples of asphaltene dispersants include succinimide, maleic acid, polyolefin alkeneamine polymers, alkylphenol-formaldehyde resins in combination with hydrophilic-lipophilic vinyl polymers (see, e.g., CA 2, 029, 465 and CA 2, 075, 749), dodecylbenzenesulfonic acid (see U.S. Pat. No. 4,414,035 and also D.-L. Chang and H. S. Fogler (SPE paper No. 25185, 1993) and by M. N. Bouts et al. (J. Pet. Technol. 47, 782-7, 1995), oxalkylated amines (see U.S. Pat. No. 5,421,993), and/or alkylphenol resins and oxalkylated amines (see U.S. Pat. No. 6,180,683).
In certain aspects, the nanoparticles of the invention can have a surface modifying agent impregnated within the nanoparticle, and/or bound or otherwise adhered on the surface of the nanoparticle. In certain aspects, the surface modifying agent can be bound or otherwise adhered on the surface of the nanoparticle. In some aspects, the nanoparticles can have surface modifying agent bound or otherwise adhered to at least a portion of the outer surface of the nanoparticle. The weight ratio of the nanoparticle (e.g. without the surface modifying agent) and the surface modifying agent can be 95:5 to 60:40, or equal to any one of, at least any one of, or between any two of 95:5, 90:10, 85:15, 80:20, 75:25, 70:30, 65:35, 60:40, 55:45 and 50:50. The surface modifying agent can be a non-ionic surfactant, an anionic surfactant, a cationic surfactant, an amphoteric surfactant, a zwitterionic surfactant, a block co-polymer, an organic compound, or any combinations thereof. In certain aspects, the surface modifying agent is sorbitan monooleate, sodium dodecylbenzene sulfonate, cetylpyridinium chloride, benzyldimethylhexadecyl-ammonium chloride, bis(2-ethylhexyl)phosphate, cetrimonium chloride, cetrimonium bromide, 3-aminopropyltriethoxysilane, n-octadecyltrimethoxysilane or any combinations thereof. In certain aspects, the polymer, such as polyethylene, such as oxidized polyethylene containing nanoparticle of the invention can contain a surface modifying agent selected from sorbitan monooleate, sodium dodecylbenzene sulfonate, cetylpyridinium chloride, benzyldimethylhexadecyl-ammonium chloride, bis(2-ethylhexyl)phosphate, or any combinations thereof, wherein the surface modifying agent can be bound or otherwise adhered on the surface of the nanoparticle. In certain aspects, the silica containing core-shell nanoparticle of the invention can contain a surface modifying agent selected from alkyl-alkoxysilanes/alkyl silanes (e.g., 3-aminopropyltriethoxysilane and/or n-octadecyltrimethoxysilane) and/or aromatic alkoxysilanes/aromatic silanes (e.g., phenyltrimethoxysilane), preferably 3-aminopropyltriethoxysilane, wherein the surface modifying agent can be bound or otherwise adhered on the surface of the nanoparticle.
In some particular aspects of the present invention, the surface modifying agent can be a nonionic surface modifying agent such as polyoxyethylene sorbitan fatty acid ethers (e.g., sold under the trade name TWEEN®) or sorbitan fatty acid ethers (e.g., sold under the trade name SPAN®), or combinations thereof. Non-limiting examples include Tween 20, Tween 40, Tween 60, Tween 80, Tween 85, Span 20, Span 40, or Span 85, or combinations thereof.
In some aspects, the asphaltene inhibitor is capable of acting as an asphaltene inhibitor and as a surface modifying agent or a surface active agent/surfactant, non-limiting examples of which include cationic asphaltene inhibitors/dispersants (e.g., imidazoline based), non-ionic asphaltene inhibitors (e.g., resin based), and/or anionic asphaltene inhibitors, or any combination thereof.
In certain aspects, the silica containing core-shell nanoparticle of the invention can contain a surface active agent. The surface active agent can be positioned in the core of the core-shell nanoparticle. In certain aspects, the surface active agent can include any one of or any combination of the surface modifying agents discussed throughout this specification. In some particular aspects, the surface active agent can be a cationic surfactant. In certain aspects, the cationic surfactant can be cetrimonium chloride and/or cetrimonium bromide, preferably cetrimonium bromide. In some aspects, 0 to 10 wt. %, or equal to any one of, at least any one of, or between any two of 0, 0.2, 0.5, 1, 2, 3, 4, 5, 6, 7, 8, 9 and 10 wt. % of the core 402, based on the total weight of the core 402, can be comprised of the surface active agent.
The nanoparticles of the present invention can be prepared by contacting the asphaltene inhibitor with the carrier material. The carrier material can be a suitable form that can be contacted with the asphaltene inhibitor. In certain aspects, carrier material containing unloaded nanoparticles, e.g., nanoparticles without asphaltene inhibitor, can be contacted with the asphaltene inhibitor to form the nanoparticles of the present invention. In certain aspects, the carrier material can be in a melted form that can be contacted with the asphaltene inhibitor to form the nanoparticles of the present invention. The melted carrier material and asphaltene inhibitor combination can then be used to form nanoparticles and can be cooled. In certain aspects, precursor material of the carrier material can be contacted with the asphaltene inhibitor to form the nanoparticles of the present invention.
In certain aspects, the carrier material can contain polymer matrix, and the method of making the nanoparticles can include contacting the polymer with the asphaltene inhibitor at a temperature above the melting point of the polymer. In certain aspects, the melted polymer and the asphaltene inhibitor can form an emulsion containing the polymer and the asphaltene inhibitor, and the emulsion can be cooled to form a nanoparticle containing the polymer and asphaltene inhibitor. The emulsion can be formed by contacting the melted polymer and the asphaltene inhibitor with an immiscible solvent. In the emulsion, the continuous phase can be the immiscible solvent, and the discontinuous droplet phase can include the polymer and the asphaltene inhibitor. The polymer and the asphaltene inhibitor can be premixed and can be contacted with the immiscible solvent, or can be separately contacted with the immiscible solvent and mixed to form the emulsion. The polymer and the asphaltene inhibitor can be heated to a temperature above the melting point of the polymer prior and/or after contacting with the immiscible solvent. In some particular aspects, a high temperature pre-formed mixture containing the polymer and asphaltene inhibitor having a temperature above the melting point of the polymer can be contacted with the immiscible solvent to form the emulsion. The polymer and/or the asphaltene inhibitor can be heated to temperatures above the melting point of the polymer before, during and/or after contacting with each other. In some particular aspects, the high temperature pre-formed mixture can be formed by contacting the polymer and asphaltene inhibitor to form a pre-formed mixture, and heating the pre-formed mixture to form the high temperature pre-formed mixture. In some particular aspects, the high temperature pre-formed mixture can be formed by melting the polymer to form a polymer melt, and contacting the polymer melt with the asphaltene inhibitor to form the high temperature pre-formed mixture. In certain aspects, the method can further include contacting a surface modifying agent with the immiscible solvent. The surface modifying agent can be contacted with the immiscible solvent, before, during and/or after contacting the immiscible solvent with the polymer, and/or the asphaltene inhibitor. In certain aspects, the pre-formed mixture and/or the high temperature pre-formed mixture can contain the surface modifying agent and the surface modifying agent can be contacted with the immiscible solvent, with the pre-formed mixture, and/or the high temperature pre-formed mixture. Without wishing to be bound by theory, it is believed that the surface modifying agent can get adsorbed, or otherwise adhered to the surface of the discontinuous droplet phase, and can control the emulsion droplet formation, size of the nanoparticles formed, and stabilize the synthesized nanoparticle. In certain aspects, the surface modifying agent can be non-ionic surfactant, an anionic surfactant, a cationic surfactant, an amphoteric surfactant, a zwitterionic surfactant, a block co-polymer, an organic compound, or any combinations thereof. In certain aspects, the surface modifying agent can be sorbitan monooleate, sodium dodecylbenzene sulfonate, cetylpyridinium chloride, benzyldimethylhexadecyl-ammonium chloride, bis(2-ethylhexyl)phosphate, or any combinations thereof. The immiscible solvent used can be immiscible with the polymer and the asphaltene inhibitor. In certain aspects, the immiscible solvent can be water, acetic acid, butanol, ethylene glycol, acetyl acetone, or any combinations thereof. In some particular aspects, the immiscible solvent can be water. In some aspects, the emulsion can be oil-in-water emulsion. In certain aspects, the weight ratio of the polymer and the asphaltene inhibitor used can be 9:1 to 1:9, or equal to any one of, at least any one of, or between any two of 1:9, 2:8, 3:7, 4:6, 5:5, 6:4, 7:3, 8:2, and 9:1. In certain aspects, the weight ratio of the polymer and the surface modifying agent used can be 1:0.05 to 1:4 or equal to any one of, at least any one of, or between any two of 1:0.05, 1:0.1, 1:0.2, 1:0.5, 1:1, 1:1.5, 1:2, 1:3, and 1:4.
In certain aspects, the polymer can be polyolefin, paraffin wax, fatty glyceride, polyacrylamide, polystyrene, epoxide, polyester or any combinations thereof. In some aspects, the polymer can have a melting point of 30° C. to 300° C. In certain aspects, the polymer can be polyolefin. In some aspects, the polyolefin can be polyethylene. In certain aspects, the polyethylene can be oxidized polyethylene. In some particular aspects, the polyethylene, such as oxidized polyethylene can have a weight average molecular weight (Mw) of 2000 g/mol. to 20000 g/mol and/or a melting point of 30° C. to 300° C., preferably 50° C. to 200° C.
The core-shell nanoparticles containing a core containing asphaltene inhibitor and a shell containing silica can be prepared by contacting the asphaltene inhibitor with a silica precursor. In certain aspects, the asphaltene inhibitor and the silica precursor can be contacted by adding the asphaltene inhibitor and the silica precursor to a solution. The asphaltene inhibitor and the silica precursor can be added to the solution at any suitable order, e.g. separately, or together. In some particular aspects, a solution containing the asphaltene inhibitor can be contacted with the silica precursor. The silica precursor can form silica, such as porous silica, such as open celled porous silica in the solution. In certain aspects, the silica precursor can be a silicon alkoxide and/or an alkyl/aromatic alkoxide. In certain aspects, the silicon alkoxide can be propyl trimethoxysilane. In certain aspects, the solution can contain water. In some particular aspects, the solution can contain water and ethanol at a molar ratio of 7.8:0.1 to 7.8:4, or equal to any one of, at least any one of, or between any two of 7.8:0.1, 7.8:0.5, 7.8:1, 7.8:2, 7.8:3, and 7.8:4. In certain aspects, the solution can be heated to a temperature of 50° C. to 90° C., or equal to any one of, at least any one of, or between any two of 50, 55, 60, 65, 70, 75, 80, 85 and 90° C., before, during and/or after addition of the asphaltene inhibitor and/or the silica precursor. In certain aspects, the method can further include contacting a catalyst with the solution. The catalyst can catalyze formation of the silica from the silica precursor. The catalyst can be contacted with the solution before, during and/or after contacting the silica precursor with the solution. In certain aspects, the catalyst can be triethanolamine and/or ammonium hydroxide, preferably triethanolamine. In certain aspects, the pH of the solution after addition of the catalyst can be 6 to 11 or equal to any one of, or between any two of 6, 7, 8, 9, 10 and 11. In certain aspects, the method can further include adding a surface active agent to the solution. The surface active agent can be contacted with the solution before, during and/or after contacting the silica precursor with the solution. In some aspects, the surface active agent can be a cationic surfactant. In some particular aspects, the cationic surfactant can be a cetyltrimethylammonium halide, such as cetyltrimethylammonium chloride and/or cetyltrimethylammonium bromide, preferably cetyltrimethylammonium bromide. Without wishing to be bound by theory, it is believed that the cationic surfactant can hold the asphaltene inhibitors inside the core and can also help in formation of the mesoporosity in the silica. After formation of the core-shell nanoparticles, large particles can be separated, e.g., filtered from the solution to prevent formation damage. In some aspects, before filtration, a surface modifying agent can be added to the reaction mixture. Without wishing to be bound by theory it is believed that the surface modifying agent can impart some hydrophobicity in the surface of mesoporous silica nanoparticles (e.g., by binding to the surface of the silica nanoparticle surface), which can help in making a stable nanoparticle solution in non-polar solvents. In some particular aspects, the surface modifying agent can be an alkyl siloxane with long alkyl chain. In some particular aspects, the surface modifying agent can be (3-Aminopropyl)triethoxysilane (APTES) and/or Phenyltrimethoxysilane. In some aspects, nanoparticles can be filtered, with a 0.3 to 0.6 μm, such as about 0.45 μm filter. In certain aspects, the method of formation of the core-shell nanoparticles can also (e.g., in addition to the core-shell nanoparticles) form spherical mesoporous silica nanoparticles (e.g., without core-shell structure) containing the asphaltene inhibitors loaded in the pores and/or otherwise complexed with the silica.
The nanoparticles of the present invention can be provided to a treatment site as individual nanoparticles or as a subterranean treatment composition (e.g., a subterranean well treatment composition). By way of example, a subterranean well treatment composition can include a fluid (e.g., an aqueous and/or organic liquid) that contains a plurality of the nanoparticles (e.g., a slurry and/or dispersion) containing the asphaltene inhibitor. The composition can be a controlled—release composition capable of releasing the asphaltene inhibitor over an extended period of time. These compositions can be prepared by mixing the nanoparticles of the invention with a fluid that will be injected into the well. Non-limiting examples of a subterranean treatment composition fluid include water, salt water (KCl) an acidic aqueous solution, low sulfate seawater, an aqueous sodium carbonate solution, a surfactant, or other flush fluid, or can be an organic solvent/fluid (e.g., based on oil, natural gas or petroleum based fluids), or can be a combination of organic and aqueous fluids. In certain aspects, the fluid can contain an organic solvent containing aromatic hydrocarbons, such as C6-C15 aromatic hydrocarbons. In certain aspects, the organic solvent can contain toluene, xylene, C9 aromatic hydrocarbons, C10 aromatic hydrocarbons, or any combinations thereof. Commercially available organic solvent that can be used includes but are not limited to SHELLSOL A150, sold by Shell chemicals.
The nanoparticles or nanoparticle composition (e.g., subterranean treatment composition) of the invention can be delivered to the subterranean formation using a variety of methods, pumping, pressuring injection, or the like. In some embodiments, a squeeze or continuous treatment method is used. In some preferred aspects, a squeeze treatment can be used. A method of treating a subterranean formation, well, or wellbore is depicted in
The present invention will be described in greater detail by way of specific examples. The following examples are offered for illustrative purposes only, and are not intended to limit the invention in any manner. Those of skill in the art will readily recognize a variety of noncritical parameters which can be changed or modified to yield essentially the same results.
Materials: Oxidized PE: EPOLENE E-14 from Westlake Chemicals; Asphaltene inhibitor: CLARIANT RP 19-1301 from Clariant; Anionic Surfactant: Sodium dodecylbenzenesulfonate; Cationic Surfactant: B enzyl dim ethyl hexade cy cl-amm onium chloride.
Methods: Water at 100° C. was added to a mixture containing an oxidized polyethylene, an asphaltene inhibitor, and an anionic surfactant, and having a temperature of 150° C. After addition, the water containing the oxidized polyethylene, asphaltene inhibitor, and surfactant was stirred at 1500 rpm for 10 minutes, and was then sonicated for 30 seconds, to form oil-in-water emulsions containing the oxidized polyethylene and asphaltene inhibitor. The oil-in-water emulsion was then cooled to 4° C. in a refrigerator to form nanoparticles containing the oxidized polyethylene and asphaltene inhibitor. In a similar experiment a cationic surfactant instead of the anionic surfactant was used. Size distributions of the nanoparticles obtained in the experiments are shown in
Cetrimonium bromide was added to a solution containing water and ethanol (at molar ratio 7.8:1) at 70° C. with vigorous stirring. Propyl trimethoxysilane, triethanolamine, and an asphaltene inhibitor (CLARIANT RP 19-1301 from Clariant) were added to the solution with vigorous stirring. The pH of the solution after addition of triethanolamine was 7.5 to 10. After 10-60 minutes of stirring (3-aminopropl)triethoxysilane (APTES) was added to the solution mixture. Nanoparticles having core-shell structure with an asphaltene inhibitor containing core and mesoporous silica containing shell, which are surface functionalized with APTES were formed The synthesized product was filtered using a 0.45 μm filter to prevent formation damage. The method also produces spherical mesoporous silica nanoparticles (e.g. without core-shell structure) containing asphaltene inhibitor loaded into the pores and/or otherwise complexed with the silica.
This application claims the benefit of priority to U.S. Provisional Application 63/411,003 filed Sep. 28, 2022, which is hereby incorporated by reference in its entirety.
| Number | Date | Country | |
|---|---|---|---|
| 63411003 | Sep 2022 | US |
