WO2015041819A1 - In situ plasticization of polymers for actuation or mechanical property change - Google Patents
In situ plasticization of polymers for actuation or mechanical property change Download PDFInfo
- Publication number
- WO2015041819A1 WO2015041819A1 PCT/US2014/052940 US2014052940W WO2015041819A1 WO 2015041819 A1 WO2015041819 A1 WO 2015041819A1 US 2014052940 W US2014052940 W US 2014052940W WO 2015041819 A1 WO2015041819 A1 WO 2015041819A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- shape memory
- memory polymer
- glass transition
- transition temperature
- shape
- Prior art date
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Classifications
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- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J3/00—Processes of treating or compounding macromolecular substances
- C08J3/18—Plasticising macromolecular compounds
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/42—Polycondensates having carboxylic or carbonic ester groups in the main chain
- C08G18/44—Polycarbonates
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/0004—Use of compounding ingredients, the chemical constitution of which is unknown, broadly defined, or irrelevant
- C08J9/0009—Phase change materials
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/02—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by the reacting monomers or modifying agents during the preparation or modification of macromolecules
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/04—Oxygen-containing compounds
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L101/00—Compositions of unspecified macromolecular compounds
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G2101/00—Manufacture of cellular products
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G2110/00—Foam properties
- C08G2110/0008—Foam properties flexible
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2205/00—Foams characterised by their properties
- C08J2205/04—Foams characterised by their properties characterised by the foam pores
- C08J2205/05—Open cells, i.e. more than 50% of the pores are open
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2207/00—Foams characterised by their intended use
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2300/00—Characterised by the use of unspecified polymers
- C08J2300/22—Thermoplastic resins
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2375/00—Characterised by the use of polyureas or polyurethanes; Derivatives of such polymers
- C08J2375/04—Polyurethanes
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/04—Oxygen-containing compounds
- C08K5/07—Aldehydes; Ketones
Definitions
- the present invention relates to methods and compositions used in oil and gas wellbores for employing shape-memory materials, and more particularly relates to methods and compositions for changing the glass transition temperature of shape-memory materials using an activation fluid.
- SMPs Shape memory polymers
- Tg glass transition temperature
- Articles are formed from shape memory polymer by first heating above the glass transition temperature and then shaping the polymer, then subsequently fixing the shape by cooling to below the glass transition temperature. During deployment, the shaped article is heated above the glass transition temperature to allow recovery of the first molded shape.
- SMPs shape memory polymers
- downhole environments e.g., oil and natural gas production
- Tg glass transition temperature
- heated downhole fluids are used to increase the temperature of the SMP to greater than its Tg.
- a method for deploying a shape memory polymer comprising disposing a shape memory polymer having a deformed shape in an environment at a first temperature, the shape memory polymer having a first glass transition temperature which is greater than the first temperature.
- the method also comprises decreasing the glass transition temperature of shape memory polymer from the first glass transition temperature to a second glass transition temperature which is less than or equal to the first temperature comprising contacting the shape memory polymer with an activation fluid which may include, but is not necessarily limited to, water, alcohols, aldehydes, amides, amines, carboxylic acids, esters, ethers, ketones, dicarbonates, tricarbonates, and combinations thereof.
- the method additionally comprises expanding the shape memory polymer to deploy the shape memory polymer in a deployed shape.
- a method for deploying a shape memory polymer in a downhole environment comprising disposing a shape memory polymer having a deformed shape in the downhole environment which is at a first temperature.
- the method also comprises contacting the shape memory polymer with an activation fluid to decrease the glass transition temperature of the shape memory polymer below the first temperature, where the activation fluid includes but is not necessarily limited to water, alcohols, glycols, aldehydes, amides, amines, carboxylic acids, esters, ethers, ketones, dicarbonates, tricarbonates, and combinations thereof.
- the method comprises expanding the shape memory polymer to a deployed shape and displacing the activation fluid to increase the glass transition temperature to greater than the first temperature and to maintain the shape memory polymer in the deployed shape.
- a system for deploying a shape memory polymer comprising an activation fluid selected from the group consisting of water, alcohols, glycols, aldehydes, amides, amines, carboxylic acids, esters, ethers, ketones, dicarbonates, tricarbonates, and combinations thereof, and a shape memory polymer which is deployed by a decrease in its glass transition temperature in response to contact with the activation fluid.
- an activation fluid selected from the group consisting of water, alcohols, glycols, aldehydes, amides, amines, carboxylic acids, esters, ethers, ketones, dicarbonates, tricarbonates, and combinations thereof
- FIG. 1 is a graph showing glass transition temperature variation over time for a shape memory polymer
- FIG. 2 is a graph showing a diameter size change of a shape memory polymer with respect to a change in its glass transition temperature
- FIG. 3 is a graph of size versus time for a shape memory polymer in contact with an activation fluid at 105°F. (40.5°C);
- FIG. 4 is a graph of size versus time for a shape memory polymer in contact with an activation fluid at 1 10°F. (43.3°C);
- FIG. 5 is a graph of size versus time for a shape memory polymer in contact with an activation fluid at 1 15°F. (46.1 °C);
- FIG. 6 is a graph of the outer diameter of a high Tg shape memory polymer over time for an activation fluid
- FIG. 7 is a graph of the outer diameter of a low Tg shape memory polymer over time for an activation fluid.
- FIG. 8 is a graph of the outer diameter of a low Tg shape memory polymer over time for an activation fluid.
- a shape memory polymer can be deployed (without increasing the temperature of its environment) by decreasing the glass transition temperature (Tg) of the shape memory polymer below the environment's temperature.
- Tg glass transition temperature
- rapid and selective deployment of a downhole article that includes a shape memory polymer occurs by contact of such an article with an activation fluid to lower the Tg of the downhole article below the surrounding downhole temperature.
- a mechanical property of the shape memory polymer may be alternatively or simultaneously changed when the shape memory polymer is contacted with an activation fluid. The property changed includes, but is not necessarily limited to, a lower Young's modulus and/or increased toughness.
- a shape memory polymer may be deployed from a deformed shape or compressed shape to an original shape by shape memory recovery due to contacting the shape memory polymer with an activation fluid that lowers the Tg of the shape memory polymer.
- the shape memory polymer may include, but is not necessarily limited to, a polyurethane, a polyurethane made by reacting a polycarbonate polyol with a polyisocyanate, a polystyrene, a polyethylene, an epoxy, a rubber, a fluoroelastomers, a nitrile, a polymer made from ethylene propylene diene monomers (EPDM), a polyamide, a polyurea, a polyvinyl alcohol, a vinyl alcohol-vinyl ester copolymer, a phenolic polymer, a polybenzimidazole, a polyethylene oxide/acrylic acid/methacrylic acid copolymer crosslinked with N,N'-methylene-bis-acrylamide, a polyethylene oxide/methacrylic acid/N-vinyl-2-pyrrolidone copolymer crosslinked with ethylene glycol dimethacrylate, a polyethylene oxide/pol
- a polyurethane made by reacting
- a shape memory polymer includes a base polymer, for example polyurethane.
- the shape memory polymer can be an open cell foam or a solid, where the polymer is polyurethane. Unlike the open cell foam, the solid is substantially void-free and/or substantially devoid of interconnected structures that allow fluid communication through the solid.
- Polyurethane in general is a condensation product of a di- or polyisocyanate and a di- or polyhydroxy compound (also referred to as diol or polyol herein).
- a chain extender e.g., chain extenders based on di- or polyamines
- diols may be included in place of part of the diol charge to form the polyurethane.
- the diol, polyol, diisocyanate, polyisocyante, chain extender, and other compounds that react to form the polyurethane are referred to collectively as reactive monomers.
- Di- and polyhydroxy compounds may include, for example, diols and polyols having from 2 to 30 carbon atoms.
- Useful diols include, but are not necessarily limited to, glycols including oligomeric glycols having repeating alkyleneoxy units including di-, tri- and higher glycols, or polyglycols.
- Exemplary diols may include, but are not necessarily limited to, ethylene glycol, propylene glycol, trimethylene glycol, 1 ,3-butanediol, 1 ,4-butanediol, bishydroxymethyl cyclohexane, neopentylglycol, diethylene glycol, hexanediol, dipropylene glycol, tripropylene glycol, polypropylene glycol, triethylene glycol, polyethylene glycol, tetraethylene glycol, oligomeric and polymeric glycols such as polyethylene glycols, polypropylene glycols, polybutylene glycols, poly(ethylene-propylene) glycols, and the like. Combinations comprising at least one of the foregoing dihydroxy compounds can be used.
- Exemplary suitable polyols include, but are not necessarily limited to, triols, for example glycerol, trimethylol propane, pentaerythritol, tris(2- hydroxyethyl) isocyanurate, and the like; tetrols such as dipentaerythritol; and other sugar alcohols such as inositol, myoinositol, sorbitol, and the like. Combinations comprising at least one of the foregoing polyhydroxy compounds may be used.
- triols for example glycerol, trimethylol propane, pentaerythritol, tris(2- hydroxyethyl) isocyanurate, and the like
- tetrols such as dipentaerythritol
- other sugar alcohols such as inositol, myoinositol, sorbitol, and the like.
- Polyurethanes may be typically prepared by the condensation of a diisocyanate with a diol.
- Aliphatic polyurethanes having at least two urethane moieties per repeating unit are useful, wherein the diisocyanate and diol used to prepare the polyurethane comprise divalent aliphatic groups that may be the same or different.
- the divalent aliphatic units may be C2 to C30, specifically C3 to C25, more specifically C4 to C20 alkylene groups, including straight chain alkylene, branched chain alkylene, cycloalkylene, heteroalkylene such as oxy- alkylene (including polyetheralkylene), and the like.
- Exemplary aliphatic diradi- cal groups include but are not limited to ethylene; 1 ,2- and 1 ,3-propylene; 1 ,2-, 1 ,3-, and 1 ,4-butylene; 1 ,5-pentamethylene; 1 ,3-(2,2-dimethyl)propylene; 1 ,6- hexamethylene; 1 ,8-octamethylene; 1 ,5-(2,2,4-trimethyl)pentylene, 1 ,9-nona- methylene; 1 ,6-(2,2,4-trimethyl)hexylene; 1 ,2-, 1 ,3-, and 1 ,4-cyclohexylene; 1 ,4- dimethylene cyclohexane; 1 , 1 1-undecamethylene; 1 , 12-dodecamethylene, and the like.
- Monomeric diisocyanates may be used to prepare the polyurethane.
- the diisocyanate component may be a monomeric C4-20 aliphatic or C4-20 aromatic diisocyanate.
- Exemplary aliphatic diisocyanates include isophorone diisocyanate; dicyclohexylmethane-4,4'-diisocyanate; 1 ,4-tetra- methylene diisocyanate; 1 ,5-pentamethylene diisocyanate; 1 ,6-hexamethylene diisocyanate; 1 ,7-heptamethylene diisocyanate; 1 ,8-octamethylene diisocyanate; 1 ,9-nonamethylene diisocyanate; 1 , 10-decamethylene diisocyanate; 2,2,4-trimethyl-1 ,5-pentamethylene diisocyanate; 2,2'-dimethyl-1 ,5-pentameth- ylene diisocyanate; 3-me
- Exemplary aromatic polyisocyanates include, but are not necessarily limited to, toluene diisocyanate, methylene bis-phenylisocyanate (diphe- nylmethane diisocyanate), methylene bis-cyclohexylisocyanate (hydrogenated MDI), naphthalene diisocyanate, and the like.
- Polymeric or oligomeric diisocyanates may also or alternatively be used to prepare a polyurethane or a urethane- or urea-linked copolymer.
- Exemplary oligomeric or polymeric chains for the polymeric diisocyanates include, but are not necessarily limited to, polyurethanes, polyethers, polyester, polycarbonate, polyestercarbonates, and the like.
- the polyisocyanate is a polymeric polyisocyanate, such as a polymer chain with terminal isocyanate groups.
- Useful polyisocyanates include, but are not necessarily limited to, those based on polyesters such as polyaliphatic esters including polylactones, polyarylate esters including copolymers of phthalates with phenols such as bisphenol A, dihydroxybenzenes, and the like; and poly(ali- phatic-aromatic) esters such as ethylene terephthalate, butylene terephthalate, and the like.
- a useful class of polyaliphatic ester-based diisocyanates is based on polylactones such as polybutyrolactones, polycaprolactones, and the like.
- Exemplary polyester-diisocyanates based on these polyesters include, but are not necessarily limited to, ADIPRENE ® LFP 2950A and PP 1096, available from Chemtura, which are p-phenylene diisocyanate (PPDI)-terminated poly- caprolactone prepolymers.
- the diisocyanate may be condensed with a diamine, sometimes referred to as a chain extender.
- a diamine sometimes referred to as a chain extender.
- chain extenders include, but are not necessarily limited to, C4-30 diamines.
- the diamines may be aliphatic or aromatic.
- useful diamines include aromatic diamines including, but not necessarily limited to, 4,4'-bis(aminophenyl)methane, 3,3'- dichloro-4,4'-diaminodiphenyl methane (also referred to as 4,4'-methylene- bis(o-chloroaniline), abbreviated MOCA), dimethylsulfidetoluene diamine (DADMT), and the like.
- aromatic diamines including, but not necessarily limited to, 4,4'-bis(aminophenyl)methane, 3,3'- dichloro-4,4'-diaminodiphenyl methane (also referred to as 4,4'-methylene- bis(o-chloroaniline), abbreviated MOCA), dimethylsulfidetoluene diamine (DADMT), and the like.
- an open cell foam having a base polymer of polyurethane is formed by combining, for example, a diisocyanate and diol described herein.
- a blowing agent may be included to produce the pores for the open cell foam.
- a blowing agent such as water is included with the diol to provide a foam structure due to generation of carbon dioxide from the reaction between diisocyanate and water when the diisocyanate is combined with the water and diol.
- the foam can be formed by other chemical or physical blowing agents.
- blowing agent examples include, but are not necessarily limited to, hydrochlorofluorocarbons (e.g., methylene chloride, tetrafluoroethylene, pentafluoropropane, heptafluoro- propane, pentafluorobutane, hexafluorobutane, and dichloromonofluoroeth- ane), hydrocarbons (for example, pentane, isopentane, and cyclopeantane), carbon dioxide, acetone, and water.
- hydrochlorofluorocarbons e.g., methylene chloride, tetrafluoroethylene, pentafluoropropane, heptafluoro- propane, pentafluorobutane, hexafluorobutane, and dichloromonofluoroeth- ane
- hydrocarbons for example, pentane, isopentane, and cyclopeantane
- carbon dioxide
- the pores for the open cell foam can be produced by placing the above components in a vacuum chamber and decreasing the pressure below the internal pressure of the forming polyurethane to cause out-gassing of the polymer material.
- the density of the foam may be controlled by the amount of water or blowing agent added.
- the amount of water can be about 0.5 weight percent (wt%) independently to about 5.0 wt%, alternatively about 0.5 wt% independently to about 4.0 wt%, and more in another non-limiting version from about 0.5 wt% independently to about 3.0 wt %, based on the weight of the diol (or polyol). It will be appreciated that the use of the word "independently" with respect to a range herein means that any suitable lower threshold may be used together with any upper threshold to form another suitable, alternative range.
- physical blowing agents can be used in amount about 0.5 wt % independently to about 15 wt %, and alternatively about 0.5 wt % independently to about 10 wt %, based on the combined weight of the diol (or polyol) and diisocyanate (or polyisocyanate).
- physical blowing agents such as carbon dioxide, can be used in combination with water as a blowing agent.
- the composition containing the reactive monomers may be mixed for a time (e.g., about 20 seconds) and then disposed in a mold, which may be immediately closed by placing a top metal plate on the mold. Due to the significant amount of pressure generated by the foam-forming process, a clamp may be used to hold the top metal plate and mold together to prevent leakage of the foam material from the mold. After about 2 hours, the polyurethane foam material is sufficiently cured such that it can be removed from the mold, i.e., de-molded. Before de-molding, the mold may be cooled below the glass transition temperature of the polymer to fix the shape.
- the polyurethane foam material may be post-cure treated at a temperature of about 100°C for about 6 hours so that the polyurethane foam material reaches its full strength.
- the material is a shape memory polymer in an original shape.
- the polyurethane foam material may have a layer of "skin" on the outside surface of the polyurethane.
- the skin is a layer of solid polyurethane formed when the mixture containing reactive monomers contacts the mold surface.
- the thickness of the skin can depend on the concentration of water added to the mixture. Excess water content decreases the thickness of the skin, and insufficient water content increases the thickness of the skin.
- the formation of the skin is believed to be due to the reaction between the isocya- nate in the mixture and the moisture on the mold surface. Therefore, additional mechanical conversion processes may be used to remove the skin. Tools such as band saws, miter saws, hack saws, and hot filament wire saws can be used to remove the skin.
- the mold can be sufficiently sized to take into account material loss due to removal of the skin.
- the polyurethane may be a solid without the interconnecting pores characteristic of an open cell foam.
- the reactive monomers may be combined without addition of a blowing agent, and the components are molded and then de-molded as described above to produce a shape memory polymer in an original shape that is solid.
- the shape memory polymer after de-molding has not only an original shape but an original glass transition temperature (Tg), which is a physical characteristic of the material.
- Tg glass transition temperature
- the shape memory polymer may be heated to a temperature greater than or close to its Tg and a deformation or compression stress may be applied to the shape memory polymer to reshape the shape memory polymer into a deformed or compressed shape.
- the shape memory polymer may then be cooled below its Tg with the deformation stress still applied to the shape memory polymer.
- the shape memory polymer Upon cooling below the Tg of the shape memory polymer, the shape memory polymer is fixed in the deformed shape even with removal of the deformation stress.
- the shape memory polymer may again be heated to a temperature greater than or close to its Tg.
- a method for deploying the shape memory polymer includes disposing a shape memory polymer having a deformed shape in an environment at a first temperature (the shape memory polymer has a first glass transition temperature which is greater than the first temperature); decreasing the glass transition temperature of shape memory polymer from the first glass transition temperature to a second glass transition temperature that is less than or equal to the first temperature; and expanding the shape memory polymer to deploy the shape memory polymer in a deployed shape.
- the shape memory polymer may be a polyurethane.
- the shape memory polymer may be an open cell foam or a solid. Decreasing the glass transition temperature of the shape memory polymer includes contacting the shape memory polymer with an activation fluid.
- the glass transition temperature is a physical property of the shape memory polymer and depends in part on the interaction of the component polyurethane chains. Strong interactions among the polyurethane polymer chains lead to a greater glass transition temperature. In contrast, weaker interactions among the polyurethane polymer chains produce a smaller value for the glass transition temperature. It should be recognized that the aggregate strength of the interactions provides the glass transition temperature of the polyurethane. Thus, selection of the reactive monomers influences the glass transition temperature since the reactive monomers become part of the polymer matrix.
- the glass transition temperature of the polyurethane is about 90°C independently to about 170°C, alternatively about 95°C independently to about 160°C, and in another non-limiting embodiment from about 100°C independently to about 150°C.
- the glass transition temperature of the polyurethane may be decreased by contact with the activation fluid so that the transition glass temperature decreases by about 5°C independently to about 70°C, alternatively by about 10°C independently to about 60°C.
- the depression of the glass transition temperature may be temporary and last for as long as the activation fluid is present among the polyurethane chains.
- a shape memory polymer made of polyurethane will have substantially the same glass temperature and decreased glass temperature as the polyurethane.
- the shape memory polymer may be contacted with an activation fluid to lower the glass transition temperature of the shape memory polymer.
- the activation fluid may include brine, solvent, and alcohol. Additionally, the activation fluid may optionally include a surfactant.
- the activation fluid may include, but is not necessarily limited to, water, alcohols, glycols, aldehydes, amides, amines, carboxylic acids, esters, ethers, ketones, dicarbonates, tricarbonates, and combinations thereof. Any of one these components may be used by themselves. That is, while it is permissible that the activation fluid includes all of brine, an activation fluid as listed herein, or a solvent (100%), it is not necessary that all three components be included.
- water may include brine.
- Water or brine may be used by themselves.
- Brine can be included in the foregoing compositions to modify the density of the activation fluid as well as moderate the diffusion rate of the activation fluid in the shape memory polymer.
- the brine may be, for example, seawater, produced water, completion brine, or a combination thereof.
- the properties of the brine can depend on the identity and components of the brine.
- Seawater as an example, contains numerous constituents such as sulfate, bromine, and trace metals, in addition to halide-containing salts.
- produced water may be water extracted from a production reservoir (e.g., hydrocarbon reservoir), produced from the ground.
- Produced water is also referred to as reservoir brine and often contains many components such as barium, strontium, and heavy metals as well as halide salts.
- completion brine may be synthesized from fresh water by addition of various salts such as NaCI, CaCl 2 , or KCI to increase the density of the brine to a value such as 10.6 pounds per gallon of CaCl 2 brine.
- Completion brines can provide a hydrostatic pressure optimized to counter the reservoir pressure downhole.
- the above brines may be modified to include an additional salt.
- the additional salt included in the brine is NaCI, KCI, NaBr, MgCI 2 , CaCI 2 , CaBr 2 , ZnBr 2 , NH 4 CI, sodium formate, potassium formate, cesium formate, and the like.
- the salt may be present in the brine in an amount from about 0.5 wt.% independently to about 50 wt.%, alternatively about 1 wt.% independently to about 40 wt. %, and in another non-limiting embodiment from about 1 wt.% independently to about 25 wt.%, based on the weight of the brine.
- Brine is generally added to either increase the density of the fluid or lower the concentration of the chemical so that it does not damage the shape memory polymer.
- the activation fluid may alternatively or additionally contain solvent, which is also referred to as a mutual solvent because the solvent is miscible with more than one class of liquids.
- a mutual solvent can be soluble in hydrophobic and hydrophilic liquids, for example, hydrocarbon fluids and aqueous solutions.
- suitable ketones include, but are not limited to, 2-butanone, 2-pentanone, 3-pentanone, acetone, hydroxyacetone, 4-hydroxy- 2-butanone, 1-hydroxy-2-butanone, acetylacetone, methyl ethyl ketone, and combinations thereof.
- Suitable carboxylic acids include, but are not necessarily limited to, dicarboxylic acids and/or tricarboxylic acids.
- Suitable dicarboxylic acids include, but are not necessarily limited to, oxalic acid, malonic acid, succinic acid, glutaric acid, adipic acid, pimelic acid, suberic acid, azelaic acid, and/or sebacic acid.
- Suitable mutual solvents include but are not necessarily limited to substituted and unsubstituted glycols of the formula R 1 0(CH 2 CHR 2 0) n R 3 , wherein R 1 , R 2 , and R 3 are independently hydrogen, alkyl group, aryl group, and acetyl group, and n is about 1 to about 10.
- the alkyl group, aryl group, and acetyl group may have 1 to about 6 carbon atoms, alternatively 1 to about 4 carbon atoms; and in a different non- restrictive version 1 to about 2 carbon atoms; n is 1 to about 10, alternatively 1 to about 6, and in another non-limiting embodiment 1 to about 3.
- substituted and unsubstituted glycols include, but are not necessarily limited to, glycols such as ethylene glycol, propylene glycol, butylene glycol, hexylene glycol, di-propylene glycol, diethylene glycol, tripropyl- ene glycol, triethylene glycol, and poly glycols; glycol ethers such as ethylene glycol monomethyl ether (EGMME), ethylene glycol monoethyl ether (EGMEE), ethylene glycol monopropyl ether (EGMPE), ethylene glycol monoisopropyl ether, ethylene glycol monobutyl ether (EGMBE), ethylene glycol monophenyl ether, ethylene glycol monobenzyl ether, diethylene glycol monomethyl ether (DEGMME), diethylene glycol monoethyl ether (DEGMEE), diethylene glycol mono-n-butyl ether (DEGMBE), and dipropylene glycol monomethyl ether (DPGMEE
- the solvent may be a glycol ether wherein R 1 and R 2 are both hydrogen; R 3 is an alkyl group including methyl, ethyl, propyl, isopropyl, and butyl groups; and n is 1.
- the solvent may be ethylene glycol monomethyl ether (EGMME), and may alternatively be ethylene glycol monobutyl ether (EGMBE).
- ECMME ethylene glycol monomethyl ether
- EGMBE ethylene glycol monobutyl ether
- Suitable solvents include, but are not necessarily limited to, amides of the formula R 4 CONR 5 R 6 , wherein R 4 , R 5 , and R 6 are independently a C1 -C5 alkyl group or C1-C5 alkenyl group, and any two of R 4 -R 6 can cyclize together to form a cycle as in 1-methyl-2-pyrrolidinone.
- amide solvents include but are not limited to ⁇ , ⁇ -dimethylformamide, N,N-diethylfor- mamide, N,N-dimethylacetamide, ⁇ , ⁇ -diethylacetamide, N, N-dimethylpropio- namide, ⁇ , ⁇ -dimethylbutyramide, 1-methyl-2-pyrrolidinone, and 1 -ethyl-2- pyrrolidinone.
- Such amides are commercially available from, for example, Sigma-Aldrich.
- the solvent is not particularly limited and can be any one or a combination comprising at least one of the foregoing solvents as long as the alcohol and brine are miscible therein to an appreciable extent.
- the activation fluid may also additionally or alternatively contain an alcohol.
- the alcohol may be linear or branched.
- the alcohol is a C1-C10 alcohol, including monohydric and polyhydric alcohols.
- the monohydric alcohol include, but are not necessarily limited to, methanol, ethanol, n-propanol, isopropanol, n-butanol, 2-butanol, isobutanol, tert-butanol, n-pentanol, isopentanol, 2-pentanol, hexanol, octanol, isooctanol, cyclohexanol, 2-methyl-1-butanol, 2-methyl-1-pentanol, 3-methyl-2-butanol, 2- ethylhexanol and combinations of these.
- alcohols include, but are not necessarily limited to, polyhydric alcohols such as diols, triols, and polyols, including ethylene glycol, propylene glycol, 1 ,3-propanediol, 1 ,4-butanediol, 1 ,2,4-butanetriol, glycerin, erythritol, and the like. Combinations of the foregoing may be used.
- the amount of the brine, solvent, and/or alcohol in the activation fluid depends on the conditions and characteristics of the downhole environment as well as the desired amount and/or rate of expansion of the shape memory polymer.
- the alcohol may be present in the activation fluid in an amount of about 2 weight percent (wt%) independently to about 98 wt%, alternatively about 10 wt% to about 90 wt%, and in one non-limiting embodiment from about 30 wt% independently to about 70 wt %, based on the weight of the activation fluid.
- the solvent may be present in the composition in an amount from about 0.05 wt.% independently to about 90 wt.%, alternatively from about 0.1 wt.% independently to about 50 wt.%, and in another non- limiting embodiment from about 1 wt.% independently to about 20 wt.%, based on the weight of the activation fluid.
- the activation fluid may be pure or 100% of the noted possibilities, or alternatively may only be diluted with water or brine, or an oil, and oil-based mud, a water- based mud or an emulsion-based mud.
- the brine may be present in the activation fluid in an amount of about 20 wt.% independently to about 99 wt.%, alternatively from about 30 wt% independently to about 90 wt.%, and in a different non-limiting embodiment from about 40 wt.% independently to about 80 wt %, based on the weight of the activation fluid.
- diluents may include, but are not necessarily limited to, water-based muds, oils, oil-based muds, emulsion-based muds.
- Suitable oils may include, but are not necessarily limited to diesel, and LVT 200, diesel oil, LVT-200 oil, poly-olefin oils, synthetic as well as natural paraffin oils, and the like.
- the solvent is different than the alcohol in the activation fluid.
- the solvent and the alcohol are the same in the activation fluid.
- the activation fluid includes brine, EGMBE, and/or methanol. More particularly, the activation fluid may contain about 50 volume percent (vol%) to about 99 vol% brine, about 1 vol% to about 50 vol% EGMBE, and about 1 vol% to about 25 vol% methanol, based on the density of the activation fluid.
- the brine, solvent, and/or alcohol may be combined together as a composition, or the individual components can be used separately as the activation fluid. Alternatively, two of the components can be combined while the third is combined to the two-component composition at a later time, such as upon introduction of the activation fluid downhole.
- the density of the activation fluid is about 8 pounds per gallon (ppg) independently to about 20 ppg (about 0.96 to about 2.4 kg/L), alternatively about 9 ppg independently to about 16 ppg (about 1 .1 to about 1.9 kg/L), and in another non-limiting embodiment about 10 ppg independently to about 15 ppg (about 1.2 to about 1 .8 kg/L).
- the activation fluid lowers the (original) glass transition temperature of the shape memory polymer through a plasticization process.
- the activation fluid includes low molecular weight compounds that are smaller than the polyurethane chains of the shape memory polymer; thus, the constituents of the activation fluid can penetrate and interact with the polyurethane polymer chain molecules, which may reduce the cohesive forces between the polymer chains. Consequently, the glass transition temperature is decreased from its original value due to an increase in the chain segment mobility.
- the Tg of the shape memory polymer increase towards its original value prior to contact with the activation fluid.
- the effect of the activation fluid on the Tg of the shape memory polymer may be temporary.
- the glass transition temperature may not fully recover to its original value (before contact with activation fluid) but may instead be slightly lower than the original value of the glass transition temperature.
- FIG. 1 shows variation of the glass transition temperature over time for a shape memory polymer.
- the shape memory polymer is initially in an environment at a first temperature Td, has a deformed shape at time tO, and has first glass transition temperature Tg1.
- the first glass transition temperature Tg1 is greater than the first temperature Td, i.e., Td ⁇ Tg1. It should be noted that with respect to FIG. 1 , the first temperature Td is not changed although slight variations in Td can be expected.
- an activation fluid contacts the shape memory polymer, and the glass transition temperature begins to decrease from the first glass transition temperature Tg1 until the shape memory polymer attains a second glass transition temperature Tg2 (at time t2), with Tg2 ⁇ Td ⁇ Tg3.
- Tg2 glass transition temperature
- Tg3 glass transition temperature
- the activation fluid is displaced from the shape memory polymer, and the glass transition temperature begins to increase from the second glass transition temperature Tg2 to the third glass transition temperature T3.
- the original shape becomes fixed again in the shape memory polymer.
- the shape memory polymer reaches its third glass transition temperature Tg3 and remains in the fixed original shape.
- the third glass transition temperature Tg3 may be less than the first glass transition temperature Tg1.
- the third glass transition temperature Tg3 is less than or equal to the first glass transition temperature Tg1.
- the polyurethane shape memory polymer can recover its original shape upon contact with the activation fluid by virtue of a decrease in its transition glass temperature. Therefore, thermal activation of the shape memory effect can be avoided.
- Shape recovery by activation fluid described herein can significantly decrease the glass transition temperature of the polyurethane shape memory polymer. Instead of heating the shape memory polymer to a temperature greater than or about equal to its original Tg to actuate from the deformed shape to the original shape, shape recovery to the original shape can occur by contact with activation fluid to decrease the Tg of the polyurethane.
- the first glass transition temperature of the shape memory polymer may be from about 80°C independently to about 160°C, alternatively about 90°C to about 150°C, and in another non-limiting embodiment about 100°C independently to about 150°C.
- the second glass transition temperature may be about 30°C independently to about 120°C, alternatively about 35°C independently to about 1 10°C, and in another non- limiting embodiment about 40°C independently to about 100°C.
- the second glass transition temperature may be from about 5°C independently to about 80°C, alternatively about 10°C independently to about 70°C, and in another non-limiting embodiment from about 10°C independently to about 60°C less than the first glass transition temperature.
- the third glass transition temperature may be from about 60°C independently to about 160°C, alternatively about 70°C independently to about 165°C, and in a different non-limiting embodiment about 80°. independently to about 150°C. Additionally, the first temperature (i.e., the temperature of the environment that the shape memory polymer is in) may be about 35°C independently to about 1 10°C.
- the shape memory polymers described herein can be used in diverse applications and are well-suited for downhole applications.
- the shape memory polymers may be initially molded into an original shape for use as, for example, a packer, a sandscreen, a blowout preventer element, a submersible pump motor protector bag, a sensor protector, a sucker rod, an O-ring, a T-ring, a gasket, a sucker rod seal, a pump shaft seal, a tube seal, a valve seal, a seal for an electrical component, an insulator for an electrical component, a seal for a drilling motor, a seal for a drilling bit, or other downhole elements.
- the article Before running the article downhole, the article is deformed above the Tg of the shape memory polymer, and fixed into the deformed shape upon cooling below the
- a method for deploying a shape memory polymer in a downhole environment includes disposing the shape memory polymer having a deformed shape in the downhole environment that is at a first temperature.
- the shape memory polymer can be a downhole element, e.g., a packer or sandscreen.
- the method further includes contacting the shape memory polymer with an activation fluid to decrease the glass transition temperature of the shape memory polymer below the first temperature; expanding the shape memory polymer to a deployed shape; and displacing the activation fluid to increase the glass transition temperature to greater than the first temperature and to maintain the shape memory polymer in the deployed shape.
- displacing the activation fluid includes replacing the activation fluid with a production fluid, which can be a fluid produced from the downhole environment such as a hydrocarbon, hydrocarbon-containing fluid, aqueous fluid, or a combination comprising at least one of the foregoing.
- a production fluid which can be a fluid produced from the downhole environment such as a hydrocarbon, hydrocarbon-containing fluid, aqueous fluid, or a combination comprising at least one of the foregoing.
- FIG. 2 shows the progression of downhole deployment of a shape memory polymer (SMP), e.g., a packer.
- the downhole environment e.g., a borehole
- the SMP in a deformed shape (with outer diameter D2) is disposed in the downhole environment at time tO.
- the SMP has a first glass transition temperature Tg1 > Td.
- the activation fluid contacts the SMP, and the glass transition temperature begins to decrease from Tg1 .
- the glass transition temperature of the SMP is about equal to Td so that the SMP begins to expand from the deformed shape, i. e., the diameter increases to values greater than D2.
- the glass transition temperature has decreased from the first glass transition temperature Tg1 , to the second glass transition temperature Tg2, and the SMP continues to expand.
- downhole fluids e.g., hydrocarbons
- the activation fluid is displaced (or decreased) from the SMP so that the glass transition temperature begins to increase from Tg2 while expansion of the SMP continues (unless it has reached its original shape or has contacted the borehole wall or casing in the borehole).
- the glass transition temperature of the SMP is about equal to Td, and expansion (if still occurring) of the SMP begins to decrease.
- the SMP reaches its third glass transition temperature Tg3, and the SMP is fixed in the original shape, sealing the borehole if used a packer. By time t6, the SMP is deployed in the downhole environment.
- the first glass transition temperature Tg1 may be equal to or greater than the third glass transition temperature Tg3.
- the final glass transition temperature can be less than or equal to the original glass transition temperature
- the intermediate glass transition temperature (Tg2 in FIG. 2) is less than both the original and final glass transition temperatures of the SMP. It will be appreciated that the glass transition temperature of the SMP is temporarily decreased below Td by the presence of the activation fluid, and the decrease of the glass transition temperature to the intermediate value (Tg2 in FIG. 2) is not permanent.
- the shape memory packer is deformed or compressed (for disposal and location downhole) to have a volume that is about 60% independently to about 5%, alternatively about 50% independently to about 10%, and in another non-restrictive version to about 40% independently " to about 20% less than the volume of the original shape.
- the shape memory packer may be compressed or deformed to have an outer diameter that is about 50% independently to about 5%, alternatively about 40% independently to about 5%, and in another non-limiting embodiment about 30% independently to about 5% less than outer diameter of the original shape.
- the shape memory polymer recovers at least about 80% of its original size, alternatively at least about 90%, and in another non-limiting embodiment at least about 99% of its original size.
- size of the shape memory polymer refers to a linear dimension of a working portion of the shape memory polymer. That is, if the shape memory polymer is used as a packer to seal a borehole, then the outer diameter is the working portion of the shape memory polymer, and the outer diameter (OD) would recover at least about 80% of its original size, alternatively at least about 90%, and more in another non-limiting embodiment at least about 99% of its original size.
- the rate of expansion of the shape memory polymer from the deformed shape to the original shape is at least about 0.3 millimeters per hour (mm/hr) independently to about 12 mm/hr, alternatively about 0.4 mm/hr independently to about 10 mm/hr, and in a different non-limiting embodiment about 0.4 mm/hr independently to about 8 mm/hr.
- the amount of the activation fluid used to lower the glass transition temperature below the downhole temperature depends on a number of factors such as the density and porosity of the shape memory polymer and downhole properties such as temperature and pressure. Therefore, the activation fluid is present in an amount effective to lower the transition glass temperature of the shape memory polymer below the downhole temperature.
- the amount of activation fluid ranges from about 0.5 independently to about 100 vol% of the shape memory polymer, alternatively from about 0.5 independently to about 20 vol%, in a different non- restrictive version from about 1 independently to about 10 vol%, and in another non-limiting embodiment from about 3 independently to about 8 vol%.
- the volume ratio of activation fluid to shape memory polymer ranges from about 1000: 1 to about 75: 1 , alternatively from about 4: 1 to about 0.01 : 1 , or in another non-limiting embodiment from about 1000: 1 to about 0.01 : 1 .
- the activation fluid may be in steam or vapor form, and thus there is much less activation fluid compared to the shape memory polymer.
- the activation fluid is pumped from the surface into the target zone to temporarily lower the transition glass temperature of the shape memory polymer to deploy the shape memory polymer to its original shape.
- the exposure time of the shape memory polymer may range from about instantaneously independently to about one year, alternatively from about 1 hour independently to about 14 days, and in another non-limiting embodiment from about 6 hours independently to about 5 days.
- a system for deploying a shape memory polymer may include an activation fluid comprising a brine, solvent, and/or other activation fluid noted elsewhere, and a shape memory polymer which is deployed by a decrease in its glass transition temperature in response to contact with the activation fluid.
- the shape memory polymer may be an open cell foam including polyurethane, and the shape memory polymer actuates from a deformed shape to a deployed shape.
- the shape memory polymer may be a solid including polyurethane and actuates from a deformed shape to a deployed shape.
- the activation fluid may also change a mechanical property of the shape memory polymer.
- the changed property includes, but is not necessarily limited to, lowering Young's modulus, increasing toughness, and both simultaneously.
- a shape memory polymer (SMP) having open cell polyurethane foam was fabricated by combining MDI (isocyanate), polycarbonate polyol, and water in a mold and held at a temperature above the Tg for 18 hours.
- the mold was cooled to room temperature, and the SMP was de-molded in an original shape.
- the SMP was placed in a cylinder and heated to a temperature above or close to the Tg of the SMP).
- the SMP was deformed by compressing the SMP between two plates in the cylinder to obtain a deformed shape having 25% of the volume of the original shape.
- the cylinder was cooled to room temperature, and the SMP removed from the cylinder to produce the SMP in the deformed shape.
- the SMP in the deformed shape was placed in a container, and the container was filled with an activation fluid.
- Data for the expansion of the SMP were acquired at the indicated temperatures by placing a linear potentiometer on the top surface of the SMP and recording the expansion of the SMP by the displacement of the linear potentiometer as a function of time.
- the activation fluid included 65 volume percent (vol %) sodium bromide, 25 vol % methanol, and 10 vol % ethylene glycol mono- butyl ether (EGMBE).
- the density of the activation fluid was 10.7 pounds per gallon (ppg) (1.28 kg/L).
- Data for the expansion of the SMP were acquired at temperatures of 105°F (40.6°C), 1 10°F (43.3°C), and 1 15°F (46.1 °C).
- FIG. 3 displays displacement data for an SMP at 105°F (40.6°C).
- the height of the SMP versus the time is graphed, and the expansion of the SMP increases for greater than 1 15 hours.
- the expansion of three separate SMP samples was tested, and the data indicates that the measurements are highly reproducible. Therefore, the expansion of the SMP is well-defined and can be controlled.
- FIG. 4 shows data for SMP samples at a temperature of 1 10°F (43.3°C)
- FIG. 5 shows data for SMP samples at a temperature of 1 15°F (46.1 °C).
- FIG. 6 displays displacement data for an SMP at 185°F (85°C).
- the activation fluid was an oil based mud (OBM; solids-free OMNIFLOW available from Baker Hughes) mixed with 6 vol% methyl ethyl ketone (MEK).
- OBM oil based mud
- MEK 6 vol% methyl ethyl ketone
- the dry Tg of the SMP ranged from 142-148°C (high Tg or HiTg).
- the outer diameter (OD) of the SMP versus the time is graphed, and the expansion of the SMP increases for 40 hours.
- FIG. 7 displays displacement data for an SMP prepared as described above, at 50°F (10°C) where the activation fluid was 50 vol% acetone in water) as graph of the outer diameter of a low Tg shape memory polymer over 70 hours.
- the dry Tg for this SMP was 98-105 °C (low Tg or LoTg).
- FIG. 8 displays displacement data for an SMP prepared as described above, at 128°F (53°C) where the activation fluid was 9.6 ppg KCI (1 .2 kg/L) with 6 vol% acetyl acetone as graph of the outer diameter of a low Tg shape memory polymer over 70 hours. Again, the dry Tg for this SMP was 98- 105 °C (low Tg or LoTg).
- FIGS. 3-8 show that the expansion of the SMP is well- defined and can be controlled.
- the present invention may suitably comprise, consist or consist essentially of the elements disclosed and may be practiced in the absence of an element not disclosed.
- a method for deploying a shape memory polymer consisting essentially of or consisting of disposing a shape memory polymer having a deformed shape in an environment at a first temperature, the shape memory polymer having a first glass transition temperature which is greater than the first temperature; decreasing the glass transition temperature of shape memory polymer from the first glass transition temperature to a second glass transition temperature which is less than or equal to the first temperature comprising contacting the shape memory polymer with an activation fluid selected from the group consisting of water, alcohols, glycols, aldehydes, amides, amines, carboxylic acids, esters, ethers, ketones, dicarbonates, tricarbonates, water-based muds, oils, oil-based muds, emulsion-based muds, and combinations thereof; and expanding the shape memory polymer to deploy the shape memory polymer in a deployed
- a method for deploying a shape memory polymer in a downhole environment consisting essentially of or consisting of disposing a shape memory polymer having a deformed shape in the downhole environment which is at a first temperature; contacting the shape memory polymer with an activation fluid to decrease the glass transition temperature of the shape memory polymer below the first temperature, where the activation fluid is selected from the group consisting of water, alcohols, glycols, aldehydes, amides, amines, carboxylic acids, esters, ethers, ketones, dicarbonates, tricarbonates, and combinations thereof; expanding the shape memory polymer to a deployed shape; and displacing the activation fluid to increase the glass transition temperature to greater than the first temperature and to maintain the shape memory polymer in the deployed shape.
- a system for deploying a shape memory polymer consisting essentially of or consisting of an activation fluid selected from the group consisting of water, alcohols, glycols, aldehydes, amides, amines, carboxylic acids, esters, ethers, ketones, dicarbonates, tricarbonates, and combinations thereof; and a shape memory polymer which is deployed by a decrease in its glass transition temperature in response to contact with the activation fluid.
- an activation fluid selected from the group consisting of water, alcohols, glycols, aldehydes, amides, amines, carboxylic acids, esters, ethers, ketones, dicarbonates, tricarbonates, and combinations thereof.
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- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- General Chemical & Material Sciences (AREA)
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
- Treatments Of Macromolecular Shaped Articles (AREA)
- Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
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- Casting Or Compression Moulding Of Plastics Or The Like (AREA)
Abstract
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GB1602134.7A GB2533496A (en) | 2013-09-20 | 2014-08-27 | In situ plasticization of polymers for actuation or mechanical property change |
JP2016544341A JP2017500234A (en) | 2013-09-20 | 2014-08-27 | In-situ plasticization of polymers for shape change or mechanical property change |
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US14/033,178 US20140020910A1 (en) | 2011-12-22 | 2013-09-20 | In Situ Plasticization of Polymers For Actuation or Mechanical Property Change |
US14/033,178 | 2013-09-20 |
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Cited By (3)
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WO2017172432A3 (en) * | 2016-03-28 | 2018-08-23 | Baker Hughes, A Ge Company, Llc | High flash point fluids for in situ plasticization of polymers |
US11927082B2 (en) | 2019-02-20 | 2024-03-12 | Schlumberger Technology Corporation | Non-metallic compliant sand control screen |
US12078035B2 (en) | 2020-10-13 | 2024-09-03 | Schlumberger Technology Corporation | Elastomer alloy for intelligent sand management |
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US20090101354A1 (en) * | 2007-10-19 | 2009-04-23 | Baker Hughes Incorporated | Water Sensing Devices and Methods Utilizing Same to Control Flow of Subsurface Fluids |
US20100089565A1 (en) * | 2008-10-13 | 2010-04-15 | Baker Hughes Incorporated | Shape Memory Polyurethane Foam for Downhole Sand Control Filtration Devices |
US20110232901A1 (en) * | 2010-03-26 | 2011-09-29 | Baker Hughes Incorporated | VARIABLE Tg SHAPE MEMORY POLYURETHANE FOR WELLBORE DEVICES |
US20110252781A1 (en) * | 2010-04-20 | 2011-10-20 | Baker Hughes Incorporated | Prevention, Actuation and Control of Deployment of Memory-Shape Polymer Foam-Based Expandables |
US20130161026A1 (en) * | 2011-12-22 | 2013-06-27 | Baker Hughes Incorporated | Chemical glass transition temperature reducer |
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2014
- 2014-08-27 WO PCT/US2014/052940 patent/WO2015041819A1/en active Application Filing
- 2014-08-27 JP JP2016544341A patent/JP2017500234A/en active Pending
- 2014-08-27 GB GB1602134.7A patent/GB2533496A/en not_active Withdrawn
Patent Citations (5)
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US20090101354A1 (en) * | 2007-10-19 | 2009-04-23 | Baker Hughes Incorporated | Water Sensing Devices and Methods Utilizing Same to Control Flow of Subsurface Fluids |
US20100089565A1 (en) * | 2008-10-13 | 2010-04-15 | Baker Hughes Incorporated | Shape Memory Polyurethane Foam for Downhole Sand Control Filtration Devices |
US20110232901A1 (en) * | 2010-03-26 | 2011-09-29 | Baker Hughes Incorporated | VARIABLE Tg SHAPE MEMORY POLYURETHANE FOR WELLBORE DEVICES |
US20110252781A1 (en) * | 2010-04-20 | 2011-10-20 | Baker Hughes Incorporated | Prevention, Actuation and Control of Deployment of Memory-Shape Polymer Foam-Based Expandables |
US20130161026A1 (en) * | 2011-12-22 | 2013-06-27 | Baker Hughes Incorporated | Chemical glass transition temperature reducer |
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Publication number | Priority date | Publication date | Assignee | Title |
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WO2017172432A3 (en) * | 2016-03-28 | 2018-08-23 | Baker Hughes, A Ge Company, Llc | High flash point fluids for in situ plasticization of polymers |
GB2565459A (en) * | 2016-03-28 | 2019-02-13 | Baker Hughes A Ge Co Llc | High flash point fluids for in situ plasticization of polymers |
GB2565459B (en) * | 2016-03-28 | 2021-02-03 | Baker Hughes A Ge Co Llc | High flash point fluids for in situ plasticization of polymers |
US11927082B2 (en) | 2019-02-20 | 2024-03-12 | Schlumberger Technology Corporation | Non-metallic compliant sand control screen |
US12078035B2 (en) | 2020-10-13 | 2024-09-03 | Schlumberger Technology Corporation | Elastomer alloy for intelligent sand management |
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Publication number | Publication date |
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JP2017500234A (en) | 2017-01-05 |
GB2533496A (en) | 2016-06-22 |
GB201602134D0 (en) | 2016-03-23 |
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