EP2838633A1 - Composition démulsifiante et son procédé d'utilisation - Google Patents

Composition démulsifiante et son procédé d'utilisation

Info

Publication number
EP2838633A1
EP2838633A1 EP13778640.6A EP13778640A EP2838633A1 EP 2838633 A1 EP2838633 A1 EP 2838633A1 EP 13778640 A EP13778640 A EP 13778640A EP 2838633 A1 EP2838633 A1 EP 2838633A1
Authority
EP
European Patent Office
Prior art keywords
water
microemulsion
oil
demulsifier composition
emulsion
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
EP13778640.6A
Other languages
German (de)
English (en)
Other versions
EP2838633A4 (fr
Inventor
Duy T. Nguyen
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ChampionX LLC
Original Assignee
Nalco Co LLC
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from US13/452,222 external-priority patent/US9353261B2/en
Application filed by Nalco Co LLC filed Critical Nalco Co LLC
Publication of EP2838633A1 publication Critical patent/EP2838633A1/fr
Publication of EP2838633A4 publication Critical patent/EP2838633A4/fr
Pending legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
    • B01D17/02—Separation of non-miscible liquids
    • B01D17/04—Breaking emulsions
    • B01D17/047—Breaking emulsions with separation aids
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
    • C09K8/52—Compositions for preventing, limiting or eliminating depositions, e.g. for cleaning
    • C09K8/524—Compositions for preventing, limiting or eliminating depositions, e.g. for cleaning organic depositions, e.g. paraffins or asphaltenes
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
    • C09K8/60—Compositions for stimulating production by acting on the underground formation
    • C09K8/602—Compositions for stimulating production by acting on the underground formation containing surfactants
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G33/00—Dewatering or demulsification of hydrocarbon oils
    • C10G33/04—Dewatering or demulsification of hydrocarbon oils with chemical means

Definitions

  • This invention relates generally to novel microeraulsion-based demulsifier compositions and methods of resolving emulsions of water and oil. More specifically, this invention concerns microemulsion-based demulsifer compositions comprising the disclosed surfactants and a stabilizing coupling agent. The invention has particular relevance to microemulsion-based demulsifier compositions and methods for resolving oii-in-water, water-in-oil, and complex emulsions of water and oil.
  • Crude oil produced from geological formations can contain various amounts of water.
  • Water and crude oil are naturally non-miscible; however, when naturally occurring interfacial active compounds are present, these compounds can aggregate on the water and oil interface and cause water to form droplets within the bulk oil phase.
  • interfacial active compounds When crude oil lifting through production tubings, the water and oil encounters an increased mixing energy from rapid flow through chokes and bends. This additional mixing energy can emulsify the water and oil.
  • Such an oil external, water internal two-phase system is commonly referred to as a crude oil emulsion, which can be quite stable.
  • the presence of water in crude oil can interfere with refining operations, induce corrosion, increase heat capacity, and result in reduced handling capacity of pipelines and refining equipment. Therefore, the crude oil that is to be shipped out of the oilfield should be practically free of water and usually has a maximum water content limit of about 0.5 to 3% by total weight, depending on the type of crude and oil company.
  • the emulsified water can also contain various amounts of salts. These salts are detrimental to crude oil refining processes due to potential corrosion in the refinery.
  • desalting techniques comprise the deliberate mixing of the incoming crude oil with a fresh "wash water” to extract the water soluble salts and hydrophilic solids from the crude oil.
  • Primary dehydration of the crude oil occurs in oil field water oil separation systems such as "free water knock out” and "phase separators.” Quite often, these systems are not adequate for efficient separation due to factors such as over production, unexpected production changes, and system underdesigns. In these cases, emulsion-breaking chemicals are added to the production processes to assist and promote rapid water oil separations.
  • emulsion-breaking chemicals or deniu!sifiers include alkylphenol formaldehyde resin alkoxylates (AFRA), polyalkylene glycols (PAG), organic sulfonates, and the like. These active ingredients are typically viscous and require a suitable organic solvent to reduce the viscosity of the demulsifier blend. Accordingly, there is an ongoing need for new, economical, environmentally-friendly, and effective chemicals and processes for resolving emulsions into the component parts of water and oil or brine,
  • demulsifier that does not require an organic solvent. It is also desired to have a demulsifier composition capable of resolving water external, water interna!, and complex emulsions while having a broad dosage range.
  • the demulsifier composition includes (i) an oil-like phase comprising at least one nonionic surfactant having a hydropbilic-lipophilic balance (HLB) of less than about 9; (ii) a coupling agent capable of stabilizing the microemulsion-based demulsifier composition; (iii) at ieast one water-soluble or dispersible nonionic surfactant that is different from the at least one nonionic surfactant in the oil-like phase; (iv) at Ieast one additional surfactant selected from anionic, cationic, amphoteric, and combinations thereof; (v) at ieast one nonionic demulsifier; and (vi) water.
  • HLB hydropbilic-lipophilic balance
  • An added advantage of the invention includes wettability alteration, well cieanout, and reduced well damage due to phase trapping.
  • microemulsion deraulsifier contains very small droplets of actives which can be water-insoluble whereby the droplets can deliver actives to the oil/water interface quickly and break the emulsion or prevent the emulsion formation.
  • An additional advantage of the invention is to reduce the viscosity of heavy oil thereby enhancing oil production.
  • Figure 1 shows a particle size distribution spectra obtained for sample VX10540 where a single unimodal size distribution was observed.
  • Figure 2a-2d show the volume percent water drop-out measured over time for all crudes and the two additives tested.
  • the present invention fills an industrial need for improved demulsifiers for use in resolving emulsions of oil and water.
  • the present invention generally relates to a microemulsion-based petroleum demulsifier (also known as emulsion breakers) for resolving or otherwise "breaking" emulsions that typically form during crude petroleum extraction and/or refinement.
  • microemulsion-based petroleum demulsifier also known as emulsion breakers
  • emulsions include water-in-oil emulsions and oil-in-water emulsions as well as complex emulsions.
  • An aspect of the present invention is its usefulness for resolving emulsions by forming a microemulsion thereby reducing or eliminating the need for water-insoluble organic solvents and may also form in situ microemulsions when in contact with crude oil.
  • the invention has usefulness to remove various nonpolar materials, such as oil-based mud, synthetic-based mud, paraffins, asphaltenes, siugs, schmoo, emulsions, and combinations thereof, from subterranean formations. Such removal may act to heal, restore, remediate the formations, and increase water injectivity.
  • microemulsions of the present invention are typically single phase microemulsions but may also be multiphase according to alternative embodiments.
  • the microemulsions are formed prior to pumping to the subterranean reservoir, or the microemulsions may be formed in situ in the subterranean reservoir or an injected microemulsion could form a new microemulsion incorporating non-polar and polar fluids and particles already present in the formation.
  • An in situ microemulsion may be formed when a surfactant (or a plurality of surfactants) and a polar phase (e.g., water or brine) contacts the reservoir formation and solubilizes the nonpolar material encountered in the pores of the formation.
  • a surfactant or a plurality of surfactants
  • a polar phase e.g., water or brine
  • microemulsion-based demulsifiers of this invention are effective for resolving a broad range of hydrocarbon and water emulsions encountered in crude oil production, refining, and chemical processing.
  • Typical hydrocarbons include crude oil, refined oil, bitumen, condensate, slop oil, distillates, fuels, and mixtures thereof.
  • the dernulsifers are also useful for resolving emulsions in butadiene, styrene, acrylic acid, and other hydrocarbon monomer process streams.
  • the microemulsion-based demulsifiers are brought into contact with or caused to act upon the emulsion to be treated in any of the various methods now generally used in the petroleum industry to resolve or break crude petroleum oil emulsions with a chemical agent.
  • the microemulsion-based demulsifiers of the invention are used to demulsify water-in-oil emulsions, oil-in-water emulsions, and complex emulsions in various production and refinery processes.
  • a refinery desalting process the incoming crude is deliberately mixed with wash water to remove dissolved salts and other contaminants.
  • the emulsion is admixed with an effective amount of the demulsifiers.
  • the microemulsion-based demulsifier is introduced into a crude oil emulsion by injecting beneath the surface into the oil well itself, by injecting into the crude oil at the well-head, or by injecting into the crude oil process stream at a point between the well-head and the final oil storage tank.
  • the microemulsion-based demulsifier composition may be injected continuously or in batch fashion. The injecting is preferably accomplished using electric or gas pumps.
  • the treated crude oil emulsion is then allowed to stand in a quiescent state until the desired separation into distinct layers of water and oil results. Once separation into distinct layers of water and oil has been effected, various means known in the art can be utilized for withdrawing the free water and separating the crude oil
  • the microemulsion-based demitisifying formulations of the present invention may be used to prevent, break, or resolve water-in-oil, oil-in-water, and complex type emulsions and crude petroleum oil emulsions in particular.
  • the present microemulsion-based demuisifiers may also be used to break hydrocarbon emulsions derived from refined mineral oil, gasoline, kerosene, etc.
  • the present microemulsion-based demuisifiers may be applied at any point during the petroleum oii extraction and/or production process as is commonly known in the art, For instance, the present microemulsion-based demuisifiers may be introduced at the well head, via downhole injection, either continuously or periodically, or at any point between the wellhead and the final oil storage.
  • microemulsion-based demuisifiers used depends on the particular crude oil emulsion being treated. Bottle tests as described herein may be conducted on site in order to determine the optimum dose and formulation, in general, the effective amount of the microemulsion-based demuisifiers ranges from about 10 ppm to about 5,000 ppm based on the volume of crude production. In embodiments, about 50 ppm to about 500 ppm or from about 25 ppm to about 1,000 ppm may also be used.
  • a reservoir is provided to hold the composition of the invention in either diluted or undiluted form adjacent to the point where the effluent crude petroleum oil leaves the well.
  • the reservoir is connected to a proportioning pump capable of dropwise injecting the microemulsion-based demulsifier of the invention into the fluids leaving the well, which then pass through a flow line into a settling tank.
  • the well fluids pass into the settling tank at the bottom of the tank so that incoming fluids do not disturb stratification of the layers of crude petroleum oil and water which takes place during the course of demulsification.
  • the present invention further contemplates a method for breaking an emulsion comprising oil and water.
  • the method includes contacting the emulsion with any of the microemulsion-based demuisifiers as herein described. Consequently, the method may include contacting an emulsion with a microemulsion-based demulsifier composed of (i) an oil-like phase comprising at least one nonionic surfactant having a hydrophilic-lipophilic balance (HLB) of less than about 9; (ii) a coupling agent capable of stabilizing the microemulsion-based demulsifier composition; (iii) at least one water-soluble or disperslble nonionic surfactant that is different from the at least one nonionic surfactant in the oil-like phase; (iv) at least one additional surfactant selected from anionic, cationic, amphoteric, and combinations thereof; (v) at least one nonionic demulsifier; and (vi) water.
  • HLB hydrophilic-lipophilic balance
  • the microemulsion-based demulsifer composition is used to demulsify water-in-oil emulsions in various production and refinery processes.
  • the incoming crude is deliberately mixed with wash water to remove dissolved salts and other contaminants.
  • the emulsion is admixed with an effective amount of the microemulsion-based demulsifier of this invention.
  • the microemulsion-based demulsifying agent of the invention is brought into contact with or caused to act upon the emulsion to be treated in any of the various methods now generally used in the petroleum industry to resolve or break crude petroleum oil emulsions with a chemical agent,
  • the treated crude oil emulsion is then allowed to stand in a quiescent state until the desired separation into distinct layers of water and oil results.
  • various means known in the art can be utilized for withdrawing the free water and separating crude oil.
  • a reservoir is provided to hold the composition of the invention in either diluted or undiluted form adjacent to the point where the effluent crude petroleum oil leaves the well.
  • the reservoir is connected to a proportioning pump capable of dropwise injecting the microemulsion-based demulsifier of the invention into the fluids leaving the well, which then pass through a flow line into a settling tank.
  • the well fluids pass into the settling tank at the bottom of the tank so that incoming fluids do not disturb stratification of the layers of crude petroleum oil and water which takes place during the course of demulsification.
  • the microemulsion-based demulsifier composition may also include corrosion inhibitors, viscosity reducers, and other chemical treatments used in crude oil production, refining and chemical processing. Additional optional solvents could be added such as: xylene, toluene, light or heavy aromatic naphtha, and the like. Each component contributes to different treating characteristics when added to the crude oil emulsion due to their unique chemical properties.
  • the invention in a preferred embodiment is a microemulsion-based demuisifier composition effective in resolving emulsions of oil and water.
  • the oil may be any type of hydrocarbon encountered in oil and gas operations.
  • the disclosed demuisifier composition includes: (i) an oil-like phase comprising, (ii) at least one coupling agent, (iii) at least one water-soluble or dispersible nonionic surfactant that is different from the at least one nonionic surfactant in the oil-like phase, (iv) at least one additional surfactant, (v) at least one nonionic demuisifier, and (vi) water.
  • the oil-like phase includes at least one nonionic surfactant having a hydrophilic-lipophilic balance (HLB) of less than about 9.
  • the nonionic surfactant having an HLB of less than about 9 is selected from at least one of the following: linear and branched alkoxylated alcohols, alkoxylated alkylphenols, glycerol esters, glycol esters, polyetheyleiieglycol esters, poiygiyeerol esters, sorbitol esters, ethylene oxide/propylene oxide copolymers, and combinations thereof, in embodiments with an alkoxylated alcohol, they may be selected from at least one of the following: ethoxylated and propoxylated C 6 -C 2 o alcohols; and mixtures thereof.
  • HLB hydrophilic-lipophilic balance
  • the ethoxylated and propoxylated & ⁇ €3 ⁇ 4; alcohols preferably have about 1-6 moles of ethylene oxide, or about 1 -6 moles of propylene oxide, or 1 -6 and 3 -6 moles of ethylene oxide and propylene oxide, respectively, per mole of alcohol.
  • the amount of the nonionic surfactant comprising the oil-like phase is preferably in the range of about 0.1% to about 35%, and more preferably, about 2% to 25%, by weight based on the total weight of the microemulsion-based demuisifier composition.
  • the alkoxylated aicohol in the microemulsion-based demuisifier composition comprises about 1-6 moles of alkylene oxide per mole of alcohol
  • from about 0.1% to about 35% of the at least one nonionic surfactant of component (i) is present in the oil-like phase of the microemulsion-based demuisifier composition, based on weight.
  • from about 2% to about 25% of the at least one nonionic surfactant of component (i) is present in the oil-like phase of the microemulsion-based demuisifier composition, wherein, based on weight.
  • the coupling agent is capable of stabilizing the microemulsion-based demulsifier composition.
  • the coupling agent is a water-soluble organic solvent.
  • R epresentative water-soluble organic solvents include, for example, at least one of the following: short chain alcohols with between 1 and 6 carbon atoms; diols with between 1 and 6 carbon atoms; glycerol; alkyl ethers of alkylene glycols with between 1 and 6 carbon atoms; poiyalkylene glycols less than 6 kD; and mixtures thereof.
  • Representative short chain alcohols include, for example, at least one of the following: methanol, ethanol, n-propanol, and combinations thereof.
  • Representative diols include, for example, at least one of the following: methylene glycol, ethylene glycol, propylene glycol, and combinations thereof.
  • Representative alkyl ethers of alkylene glycols include, for example, ethylene glycol mono-n-butyl ether.
  • from about 5% to about 40% of the coupling agent of component (ii) is present in the microemufsion-based demulsifier composition, based on the total weight of the composition.
  • the microemulsion-based demulsifier composition includes at least one water-soluble or dispersible nonionic surfactant that is different from the at least one nonionic surfactant in the oil-like phase
  • the water-soluble or dispersible nonionic surfactant includes, for example, an alkoxylated alcohol, ethylene oxide/propylene oxide copolymers, and/or alkoxylated alkylphenol having an HLB greater than about 10. in another embodiment, from about 2% to about 25% of the water-soluble or dispersible nonionic surfactant is present in the microemulsion-based demulsifier composition, based on total weight.
  • the additional surfactant is selected from anionic surfactants, cationic surfactants, amphoteric surfactants, and combinations thereof.
  • Representative additional surfactants include, for example, at least one of the following: linear alkylbenzene sulfonic acid, alkyl benzene sulfonate, alkane sulfonate, alkyl sulfate, alkyl ether sulfate, alkyl ammonium halides, alkyl aryl ammonium ha! ides, imidazolium, cocoamidopropyl betaine, cocodimethyl betaine, alkyl amine oxide, and combinations thereof exclusive of combinations with both anionic and cationic surfactants.
  • the nonionic demulsifiers in the present invention include, for example, at least one of the following: polyethylenimine alkoxylaies, alkoxylated alkylphenol formaldehyde resins, alkoxylated amine-modified alkylphenol formaldehyde resins, ethylene oxide/propylene oxide copolymers, cross-linked ethylene oxide/propylene oxide copolymers, alkoxylated sorbitan esters, and mixtures thereof.
  • up to about 30% or from about from about 2% to about 30% of the nonionie demulsifier is present in the microemulsion-based demulsifier composition, based on total weight.
  • up to about 25% of the water- soluble or dispersible nonionie surfactant is present in the microemulsion-based demulsifier composition, based on total weight, in an embodiment, from about 5% up to about 25% of the nonionie demulsifier is present in the microemulsion-based demulsifier composition, based on total weight.
  • These microemulsion-based demulsifers can also be used at the well head or be injected downhole to break the emulsion. Since the microemulsion contains very tiny droplets which encapsulate the demulsifier, it then can migrate more quickly to the oil and water interface than a non-microemulsion demulsifier. As a result, the demulsification efficiency is increased.
  • the disclosed microemulsion-based demulsifier composition may further include additional components or adjuncts, such as at least one of oxidizing agents, water-soluble enzymes, precursors to these components, and combinations thereof.
  • the present invention also provides a method of resolvin emulsions of oil and water.
  • the oil phase may be at least one or more hydrocarbons encountered in oil and gas operations.
  • the method includes (i) adding at least one variation of the disclosed microemulsion-based demulsifier composition to the emulsion of oil and water, .
  • the addition may take place at any point, including at the well head, be injected to the reservoir during fracturing process, be injected before the separator, or be injected downhole to break or prevent the emulsion.
  • the method of the invention further includes forming a single phase microemulsion in situ in the subterranean reservoir, where the in situ-formed single phase microemulsion is a thermodynamically stable, macroscopically homogeneous mixture of at least the following components (as described in more detail herein): (i) an oil-like phase comprising at least one nonionie surfactant having a hydrophilic-lipophilic balance (HUB) of less than about 9; (ii) a coupling agent capable of stabilizing the microemulsion flowback aid composition; (iii) at least one water-soluble or dispersible nonionie surfactant that is different from the at least one nonionie surfactant in the oil-like phase; (iv) at least one additional surfactant selected from anionic, cation ic, amphoteric, and combinations thereof; (v) at least one nonionie demulsifier (vi) water; and a nonpolar material derived from the subterranean
  • the microemulsion-based demulsifier of the present invention may aiso be applied in the presence of additional chemicals.
  • additional demulsifiers or in combination with any of a number of additional demulsifiers known in the art including for example, alcohols, fatty acids, tatty amines, glycols, and alkylphenol formaldehyde condensation products.
  • the microemulsio/i-based demulsifiers may also be used m combination with corrosion inhibitors, viscosity reducers, and other chemical treatments used in crude oil production, refining and chemical processing.
  • additional chemicals such as friction reducers, scale inhibitors, clay swelling inhibitors, bioeides, flow back aids, and surfactants may be added on the fly during treatment with the composition of the present invention.
  • Example 1 Preparation of the Microemulsion-Based Demulsifiers This example provides representative formulations for the demulsifiers of the invention.
  • Sample 110-2 3% alcohol ethoxylate (C 12 +3 EO) ; 5.2% EO PO copolymer (water dispersible); 2.7% ethoxylated Cg alcohol; 2.7% EO/PO copolymer (water soluble); 0.1% linear alkylbenzene sulfonic acid; 7% alkoxylated polyethyleneimine (demuisifier); 1.3% polyethylene glycol: 40% propylene glycol; and 38% water.
  • VX10540 3% alcohol ethoxylate (C i2 +3EO); 3% EO/PO copolymer; 2%
  • DOS dioctyisulfosuccinate
  • C i3 + 9EO tridecyi alcohol ethoxylate
  • 9% cross- linked EO/PO block copolymer (demuisifier): 10% glycerin; 30% ⁇ : and 40% water.
  • Example 2 Particle Size Distribution
  • FIG 1 shows the particle size distribution for one embodiment of the microemulsion- based demuisifier of the invention.
  • Sample VX10540 3% alcohol ethoxylate (Cj 2 +3EQ), 3% EO/PO copolymer, 2% dioctyisulfosuccinate (DOS), 3% tridecyi alcohol ethoxylate (Cn+ 9EO), 9% cross-linked EO/PO block copolymer, 10% glycerin, 30% ⁇ , 40% water).
  • the particle size distribution spectra for VX 10540 shows a unimodal particle size distribution with an average droplet size of 0.0776 ⁇ and a median droplet size of 0.0655 ⁇ . This result confirms that VX 10540 is indeed a microemulsion system. Due to the presence of very small droplets (0.01 -0.5 ⁇ ), microemulsions are transparent or translucent.
  • Example 3 Emulsion Prevention Test
  • Table 1 shows the results using commercially available samples along with the results using the sample 1 10-2 from Example 1.
  • the results show the present invention (sample 3 10-2) is superior to currently available commercial samples (Products A and B) with regard to quicker water drop out, sharp interface, clean water, and excellent wettability.
  • Product B is a non-microemulsion commercial product which contains methanol, water, water-soluble nonionic surfactants, and ethoxylated aikylphenol formaldehyde resins.
  • Table 2 shows the results of the overall fluid quality evaluation for all the crudes tested. Each crude was tesied against a blank (no additives, only 4% KCi solution), product A which is a non-microernulsion commercial product which contains methanol, water, water- soluble nonionic surfactants, and ethoxylated aikylphenol formaldehyde resins, (1 gallon per thousand gallons ("gpt") in 4% KCI solution) and VX 10540 (I gallon per thousand gallors in 4% KCi solution). Table 2 shows the overall fluid quality evaluation of untreated crude oils tested. Water quality was observed after the phase separation. The quality should preferably be clear and free of solid particles since the water is often used for re-injection.
  • the preferred interface is at the oil/water boundary ("interface") and should be sharp after the separation or an emulsion layer can build up and cause deposition and/or loss of oil. Wettability is described as how the oil wets the substrate (i.e., glass in this case) where oil sticking to the substrate (i.e., rocky substrate in a formation) is not preferred as a decrease in oil production would occur. Table 2
  • FIGs 2a-2d show the volume percent water drop-out measured over time for ail crudes and the two deniulsifiers tested. In all eases, VX 10540 facilitated a faster breakout time than Product A.
  • FIG 2a shows percent breakout vs. time results for crude oils (A, B. C, D, and E) in a 4% C1 (pH 10,9) aqueous solution (blank). The emulsions formed remained stable even after 72 hours, FiCt 2b shows percent breakout vs. time results for specified crude oils in a 4% C1 (pH 10.9) aqueous solution (blank). The emulsions formed by crude oils G and H remained stable even after 72 hours.
  • FIG 2c shows percent breakout vs. time results for specified crude oils in a 1 gpt Product A - 4% KC! solution.
  • A, B, and D crudes showed a 100% breakout by 2 minutes.
  • C and E crudes needed up to 6 minutes to separate a 300% when using Igpt of product Product A.
  • FIG 2d shows percent breakout vs. time results for specified crude oils in a 1 gpt VXI 0540 - 4% KC1 solution.
  • A, B, C, D, and E crudes showed a 100% breakout by 1.5 minutes when using Igpt of VX10540.
  • microemulsion-based demulsifer VX 10540 exhibited a clear improved performance when compared to the current market product Product A at a 1 gpt dosage in a 4% KG sol tion (pH 10.9).

Abstract

Cette invention concerne une composition démulsifiante à base de micro‑émulsion et un procédé consistant à démulsionner une émulsion comprenant des hydrocarbures et de l'eau. La composition démulsifiante comprend (i) une phase pseudo-huileuse comportant au moins un tensioactif non ionique dont le rapport hydrophile-lipophile (HLB) est inférieur à environ 9 ; (ii) un agent de couplage capable de stabiliser la composition démulsifiante ; (iii) au moins un tensioactif non ionique soluble ou dispersible dans l'eau qui est différent du tensioactif non ionique de la phase pseudo-huileuse ; (iv) au moins un autre tensioactif anionique, cationique, amphotère ou leurs associations ; (v) au moins un démulsifiant non ionique ; et (vi) de l'eau.
EP13778640.6A 2012-04-20 2013-04-19 Composition démulsifiante et son procédé d'utilisation Pending EP2838633A4 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US13/452,222 US9353261B2 (en) 2012-03-27 2012-04-20 Demulsifier composition and method of using same
PCT/US2013/037361 WO2013158989A1 (fr) 2012-04-20 2013-04-19 Composition démulsifiante et son procédé d'utilisation

Publications (2)

Publication Number Publication Date
EP2838633A1 true EP2838633A1 (fr) 2015-02-25
EP2838633A4 EP2838633A4 (fr) 2015-12-16

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Country Status (5)

Country Link
EP (1) EP2838633A4 (fr)
AU (2) AU2013249130B2 (fr)
BR (1) BR112014022515B1 (fr)
CA (1) CA2867595C (fr)
WO (1) WO2013158989A1 (fr)

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RU2549189C1 (ru) * 2013-11-29 2015-04-20 Закрытое акционерное общество "ХИМЕКО-ГАНГ" Состав для разрушения водонефтяных эмульсий и защита промыслового оборудования от коррозии
RU2549534C1 (ru) * 2013-11-29 2015-04-27 Закрытое акционерное общество "ХИМЕКО-ГАНГ" Состав для разрушения водонефтяных эмульсий и защиты нефтепромыслового оборудования от коррозии
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AU2013249130A1 (en) 2014-09-11
BR112014022515B1 (pt) 2021-01-19
AU2016225821A1 (en) 2016-09-22
WO2013158989A1 (fr) 2013-10-24
AU2013249130B2 (en) 2016-06-30
CA2867595A1 (fr) 2013-10-24
EP2838633A4 (fr) 2015-12-16
CA2867595C (fr) 2017-01-10

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