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Well Barriers For Subterranean Storage Of Carbon Dioxide

Abstract: A method may include: introducing a resin modified cement slurry into a wellbore penetrating a subterranean formation, the subterranean formation comprising a caprock and a carbon dioxide injection zone, the resin modified cement slurry comprising: a resin; a hardener; a hydraulic cement; and water; and setting the resin modified cement slurry to form a set cement wherein the set cement forms a carbonation-resistant barrier in the carbon dioxide injection zone in the subterranean formation.

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Patent Information

Application #
Filing Date
19 December 2024
Publication Number
04/2025
Publication Type
INA
Invention Field
CIVIL
Status
Email
Parent Application

Applicants

HALLIBURTON ENERGY SERVICES, INC.
3000 N. Sam Houston Parkway E. Houston, Texas 77032-3219

Inventors

1. LEWIS, Samuel J.
3000 N. Sam Houston Parkway E. Houston, Texas 77032-3219
2. JONES, Paul J.
3000 N. Sam Houston Parkway E. Houston, Texas 77032-3219

Specification

WELL BARRIERS FOR SUBTERRANEAN STORAGE OF CARBON DIOXIDE

BACKGROUND

[0001] Methods of constructing and remediating carbon capture underground storage (CCUS) wells utilize Portland cement compositions that include Portland cement and water. CCUS well barriers constructed using Portland cement compositions may be subjected over time to degradation, increased porosity, and reduced mechanical strength and barrier integrity from prolonged contact with carbon dioxide.

BRIEF DESCRIPTION OF THE DRAWINGS

[0002] These drawings illustrate certain aspects of some of the embodiments of the present disclosure and should not be used to limit or define the disclosure.

[0003] FIG. 1 illustrates a system for the preparation and delivery of a resin modified cement slurry to a wellbore in accordance with certain embodiments.

[0004] FIG. 2 illustrates surface equipment that may be used in the placement of a resin modified cement slurry in a wellbore in accordance with certain embodiments.

[0005] FIG. 3 illustrates the placement of a resin modified cement slurry into a wellbore annulus in accordance with certain embodiments.

[0006] FIG. 4 is a schematic illustration showing the presence of a small perforation in a casing and protective sheath in a wellbore.

[0007] FIG. 5 is a schematic illustration of an example in which a resin modified cement slurry is used in a remedial application.

[0008] FIG 6 is another schematic illustration of an example in which a resin modified cement slurry is used in a remedial application.

[0009] FIG 7 illustrates injection of carbon dioxide into a carbon dioxide injection zone of a in accordance with certain embodiments.

[0010] FIG. 8A is a picture of neat cement exposed to one week of saturated carbon dioxide.

[0011] FIG. 8B is a picture of neat cement exposed to one week of saturated carbon dioxide.

[0012] FIG. 8C is a picture of water extended cement exposed to one week of saturated carbon dioxide.

[0013] FIG. 8D is a picture of water extended cement exposed to one week of saturated carbon dioxide.

[0014] FIG. 8E is a picture of reduced Portland cement exposed to one week of saturated carbon dioxide.

[0015] FIG. 8F is a picture of reduced Portland cement exposed to one week of saturated carbon dioxide.

[0016] FIG. 8G is a picture of resin modified Portland cement exposed to one week of saturated carbon dioxide.

[0017] FIG. 8H is a picture of resin modified Portland cement exposed to one week of saturated carbon dioxide.

[0018] FIG. 9A is a picture of neat cement exposed to one month of saturated carbon dioxide.

[0019] FIG. 9B is a picture of neat cement exposed to one month of saturated carbon dioxide.

[0020] FIG. 9C is a picture of water extended cement exposed to one month of saturated carbon dioxide.

[0021] FIG. 9D is a picture of water extended cement exposed to one month of saturated carbon dioxide.

[0022] FIG. 9E is a picture of reduced Portland cement exposed to one month of saturated carbon dioxide.

[0023] FIG. 9F is a picture of reduced Portland cement exposed to one month of saturated carbon dioxide.

[0024] FIG. 9G is a picture of resin modified Portland cement exposed to one month of saturated carbon dioxide.

[0025] FIG. 9H is a picture of resin modified Portland cement exposed to one month of saturated carbon dioxide.

DETAILED DESCRIPTION

[0026] The present disclosure relates to systems and methods of cementing carbon capture underground storage (CCUS) wells and methods of using carbon capture underground storage well barriers to store carbon dioxide. More particularly, certain embodiments of the present disclosure are directed to systems and methods of using a resin modified cement slurry comprising a hydraulic cement, a resin, a hardener, and water, in construction and remediation of subterranean and subsea carbon capture underground storage wells to mitigate carbonation of cement therein.

[0027] In some examples, the hydraulic cement may include a Portland cement. In some examples, the Portland cements may include Portland cements that are classified as Class A, B, C, D, E, F, G, H, K and L cements according to American Petroleum Institute, API Specification for Materials and Testing for Well Cements, API Specification 10A, Twenty-Fifth Ed., March 2019. In some examples, resin modified cement slurries may include cements classified by American Society for Testing and Materials (ASTM) in C150 (Standard Specification for Portland Cement), C595 (Standard Specification for Blended Resin modified cement slurry) or Cl 157 (Performance Specification for Resin modified cement slurries) such as those cements classified as ASTM Type I, II, or III. Cementitious materials may be combined with the aqueous base fluids to form a cement slurry which may be introduced into a wellbore penetrating a subterranean formation. The cement may be included in the resin modified cement slurry in any suitable amount, including, but not limited to, about 20% to about 99% by weight of the resin modified cement slurry. Alternatively, the cement may be included in the resin modified cement slurry in a range of about 50% to about 75% by weight, about 55% to about 75% by weight, about 60% to about 70% by weight, about 60% to about 75% by weight, about 45% to about 80% by weight. Suitable amounts may include, but are not limited to, 20%, 30%, 40%, 50%, 60%, 70%, 80%, 90%, or 99% by weight of the resin modified cement slurry.

[0028] As used herein, the term “resin” may refer to any of a number of physically similar polymerized synthetics or chemically modified natural resins including thermoplastic materials and thermosetting materials. In some examples, resins may be liquid curable resins which may include, but are not limited to, epoxy-based resins, cyclic olefins, novolak resins, polyepoxide resins, phenol-aldehyde resins, urea-aldehyde resins, urethane resins, phenolic resins, furan resins, furan and furfuryl alcohol resins, phenolic/latex resins, phenol formaldehyde resins, bisphenol A diglycidyl ether resins, butoxymethyl butyl glycidyl ether resins, bisphenol A-epichlorohydrin resins, bisphenol F resins, diglycidyl ether bisphenol F resin, cyclohexane dimethanol diglycidyl ether, glycidyl ether resins, polyester resins and hybrids and copolymers thereof, polyurethane resins and hybrids and copolymers thereof, acrylate resins, and mixtures thereof. Some suitable resins, such as epoxy resins, may be cured with an internal catalyst or activator so that when pumped downhole, they may be cured using only time and temperature. Other suitable resins, such as furan resins generally require a time-delayed catalyst or an external catalyst to help activate the polymerization of the resins if the cure temperature is low (i.e., less than 250 °F (121 °C), but will cure under the effect of time and temperature if the formation temperature is above about 250°F.

[0029] Selection of a particular resin may be affected by the temperature of the subterranean formation to which the resin modified cement slurry will be introduced. By way of example, for subterranean formations having a bottom hole static temperature (“BHST”) ranging from about 60°F (15.5 °C) to about 400°F (204 °C), two-component resins may be used. Generally, a resin may be included in the resin modified cement slurry in an amount in a range of from about 2% to about 60% by volume of the resin modified cement slurry. Alternatively, a resin may be included in the resin modified cement slurry in an amount in a range of from about 1% to about 60% by weight of the resin modified cement slurry. Alternatively, from about 1% to about 5% by weight, from about 1% to about 10% by weight, from about 1% to about 15% by weight, from about 1% to about 25% by weight, from about 1% to about 35% by weight, from about 1% to about 45% by weight, from about 1% to about 55% by weight, from about 5% to about 10% by weight, from about 5% to about 15% by weight, from about 5% to about 20% by weight, from about 15% to about 30% by weight, from about 30% to about 45% by weight, from about 45% to about 60% by weight, or any ranges therebetween.

[0030] As used herein, the term “hardener” or “hardening agent” may refer to any substance capable of transforming a resin into a hardened, consolidated mass. Examples of suitable hardening agents may include, but are not limited to, aliphatic amines, aliphatic tertiary amines, aromatic amines, transition metal catalysts, cycloaliphatic amines, heterocyclic amines, amido amines, polyamides, polyethyl amines, polyether amines, polyoxyalkylene amines, carboxylic anhydrides, triethylenetetraamine, ethylene diamine, N-cocoalkyltrimethylene, isophorone diamine, N-aminophenyl piperazine, imidazoline, 1,2-diaminocyclohexane, polyetheramine, diethyltoluenediamine, 4,4'-diaminodiphenyl methane, methyltetrahydrophthalic anhydride, hexahydrophthalic anhydride, maleic anhydride, polyazelaic polyanhydride, phthalic anhydride, and combinations thereof. Examples of commercially available hardening agents may include, but are not limited to, combinations of hardeners such as 75%-81% 3,5-diethyltoluene-2,4-diamine, 18%-20% 3,5-diethyltoluene-2,6-diamine, and 0.5%-3% dialkylated phenylenediamines. In some embodiments the hardening agent may comprise a mixture of hardening agents selected to impart particular qualities to the resin modified cement slurry. In some embodiments, the hardening agents may be included in the resin modified cement slurry at a point in a range of from about 0.05% to about 50% by volume of the resin modified cement slurry. Alternatively, from about 1% to about 10% by volume, from about 1% to about 5% by volume, about 10% to about 20% by volume, about 20% to about 30% by volume, about 4% to about 50% by volume, or any ranges therebetween. Alternatively, from about 0.05% to about 5% by weight of the slurry, 0.05% to about 10% by weight of the slurry, from about 0.05% to about 15% by weight of the slurry, about 10% to about 20% by weight of the slurry, about 20% to about 30% by weight of the slurry, about 4% to about 50% by weight of the slurry, or any ranges therebetween. In some embodiments, the resin modified cement slurry may be free of poly amine.

[0031] Resin modified cement slurries may include a resin that can undergo a ring-opening metathesis polymerization (ROMP) reaction. Resin molecules that undergo ROMP may

polymerize by forming new carbon-carbon bonds between molecules. Once the polymerization reaction is initiated, the reaction may proceed rapidly to transform the resin modified cement slurry from a liquid to a solid. During the reaction, heat may be released, which may raise the temperature of the resin modified cement slurry, however, the heat generated may not be sufficient to char or degrade the final hardened mass. The resin in the resin modified cement slurry may be pumpable below 38 °C (100 °F) without additional solvents present. Further, the resin may have a density greater than water and a viscosity that may be ideal for deep penetration into channels and efficient squeezes for defects such as gas migration or casing leaks.

[0032] A resin included in the resin modified cement slurry may include a cycloalkene, which may be a cycloalkadiene, that may undergo a ring-opening metathesis polymerization reaction transforming the resin modified cement slurry into a hardened mass. The cycloalkene may have no aromatic character. The cycloalkene may include, but is not limited to, cyclopentadiene, dicyclopentadiene, tricyclopentadiene, cyclobutadiene, cyclohexadiene, terpinene, norbomadiene, isomers thereof, and combinations thereof. The cycloalkene may also be substituted or unsubstituted cycloalkadienes. Substituted cycloalkadienes may be substituted with a hydrocarbyl group or any other suitable organic functional group.

[0033] A resin included in the resin modified cement slurry may include an olefin. The olefin may comprise a cyclic olefin. The cyclic olefin may be present in the resin modified cement slurry in any suitable amount, including but not limited to a range of about 1% to about 60% by weight of the resin modified cement slurry. Alternatively, the cyclic olefin may be present in a range of about 1% to about 10% by weight, about 1% to about 15% by weight, about 1% to about 20% by weight, 1% to about 25% by weight, about 5% to about 20% by weight, about 20% to about 30% by weight, about 30% to about 40% by weight, about 40% to about 50% by weight, about 50% to about 60% by weight.

[0034] In some embodiments, the hardener may comprise a transition metal catalyst. The transition metal catalyst may be present in the resin modified cement slurry in any suitable amount, including but not limited to a range of about 0.0001% to about 5% by weight of the resin modified cement slurry. Alternatively, the transition metal catalyst may be present in a range of about 0.0001% to 0.001% by weight, about 0.001% to about 0.01% by weight, about 0.01% to about 0.1% by weight, about 0.1% by weight to about 1% by weight, about 1% to about 2% by weight, about 2% to about 3% by weight, about 3% to about 4% by weight, about 4% to about 5% by weight. Alternatively, the transition metal catalyst may be present in a range of about 0.0001% to0.001% by volume, about 0.001% to about 0.01% by volume, about 0.01% to about 0.1% by volume, about 0.1% by weight to about 1% by volume, about 1% to about 2% by volume, about

2% to about 3% by volume, about 3% to about 4% by volume, about 4% to about 5% by volume. Alternatively, the transition metal catalyst may be present in an amount less than 10% by weight, less than 20% by weight, less than 30% by weight, less than 40% by weight, or less than 50% by weight.

[0035] In embodiments wherein the hardener comprises a transition metal catalyst, the transition metal catalyst may comprise a transition metal compound catalyst which may include a substituted or unsubstituted metal carbene compound comprising a transition metal and an organic backbone. Some non-limiting examples of the transition metal compound catalyst may include, but not are limited to a Grubbs Catalyst® and Schrock catalysts. The Grubbs Catalyst® may include ruthenium alkylidene or osmium alkylidene and Schrock catalyst may include molybdenum. Selection of a transition metal compound catalyst may affect a polymerization rate of the resin in the resin modified cement slurry. The transition metal compound catalyst may be present in the resin modified cement slurry at a point in a range of about 0.0001 wt. % to about 20 wt.%. Alternatively, the transition metal compound catalyst may be present at a point in a range of about 0.0001 wt.% to about 0.001 wt.%, at a point in a range of about 0.001 wt.% to about 0.01 wt.%, at a point in a range of about 0.01 wt.% to about 0. 1 wt.%, at a point in a range of about 0. 1 wt.% to about 1 wt.%, at a point in a range of about 1 wt.% to about 5 wt.%, at a point in a range of about 5 wt.% to about 10 wt.%, at a point in a range of about 10 wt.% to about 15 wt.%, at a point in a range of about 15 wt.% to about 20 wt.%, or any ranges therebetween. Alternatively, the resin and the transition metal compound catalyst concentrations may be expressed as relative mass ratios. For example, the resin and the transition metal compound catalyst may be present in the resin modified cement slurry in a mass ratio of about 50: 1 to about 10000: 1 resin to transition metal compound catalyst. Alternatively, the resin and transition metal compound catalyst may also be present in mass ratios of about 50: 1 to about 100: 1, about 100:1 to about 500: 1, about 500: 1 to about 1000: 1, about 1000: 1 to about 2000: 1, about to 2000: 1 to about 3000: 1, about 3000: 1 to about 4000: 1, about 4000: 1 to about 5000: 1, about 5000: 1 to about 6000: 1, about 6000: 1 to about 7000: 1, about 7000: 1 to about 8000: 1, about 8000: 1 to about 9000: 1, about 9000: 1 to about 10000: 1 or any mass ratios therebetween of the resin to the transition metal compound catalyst. Alternatively, the transition metal compound catalyst may be suspended in a mineral oil suspension, or any suitable suspension medium. For example, the suspension medium may be present in the transition metal compound catalyst suspension in an amount of about 90% to 99% of the transition metal compound catalyst suspension. Alternatively, the suspension medium may be present in amount of about 90% to about 92%, about 93% to about 95%, and about 96% to about 99%. The resin and the transition metal compound catalyst suspension concentrations may

be expressed as relative mass ratios. For example, the resin and the transition metal compound catalyst suspension may be present in the resin modified cement slurry in a mass ratio of about 50: 1 resin to transition metal compound catalyst suspension. Alternatively, the resin and transition metal compound catalyst suspension may also be present in mass ratios of about 20: 1, about 30: 1, about 40:1, about 60:1, about 70:1, or about 80:1, or any mass ratios therebetween of the resin to the transition metal compound catalyst suspension. Specific examples of suitable transition metal compound catalysts will be described in detail below.

[0036] The transition metal compound catalyst may have the general chemical structure depicted in Structure 1. M may be either ruthenium or osmium. R and R1 may be independently selected from hydrogen, C2-C20 alkenyl, C2-C20 alkynyl, C2-C20 alkyl, aryl, C1-C20 carboxylate, C1-C20 alkoxy, C2-C20 alkenyloxy, C2-C20 alkynyloxy, aryloxy, C2-C20 alkoxy carbonyl, C1-C20 alkylthio, C1-C20 alkylsulfonyl or C1-C20 alkyl sulfinyl. The selected R and R1 may be optionally substituted with C 1 -C5 alkyl, halogen, C 1 -C5 alkoxy or with a phenyl group further optionally substituted with halogen, C1-C5 alkyl or C1-C5 alkoxy. X and XI may be the same or different and may be any suitable anionic ligand. L and LI may any suitable neutral electron donor.

Structure 1

[0037] The transition metal compound catalyst may also have the general chemical structure depicted in Structure 2. M may be either ruthenium or osmium. R and R1 may be independently selected from hydrogen, C2-C20 alkenyl, C2-C20 alkynyl, C2-C20 alkyl, aryl, Cl-C20 carboxylate, C1-C20 alkoxy, C2-C20 alkenyloxy, C2-C20 alkynyloxy, aryloxy, C2-C20 alkoxy carbonyl, C1-C20 alkylthio, C1-C20 alkylsulfonyl or C1-C20 alkyl sulfinyl. The selected R and R1 may optionally be substituted with C 1 -C5 alkyl, halogen, C 1 -C5 alkoxy or with a phenyl group further optionally substituted with halogen, C1-C5 alkyl or C1-C5 alkoxy. X and XI groups may be the same or different and may be any suitable anionic ligand. L2, L3, and L4 may be the same or different, and may be any suitable neutral electron donor ligand, wherein at least one L2, L3, and L4 may be an N-heterocyclic (NHC) carbene ligand as described below.

Structure 2

[0038] The transition metal compound catalyst may also have the general chemical structure depicted in Structure 3. M may be either ruthenium or osmium. R and R1 may be independently selected from hydrogen, C2-C20 alkenyl, C2-C20 alkynyl, C2-C20 alkyl, aryl, Cl-C20 carboxylate, C1-C20 alkoxy, C2-C20 alkenyloxy, C2-C20 alkynyloxy, aryloxy, C2-C20 alkoxy carbonyl, C1-C20 alkylthio, C1-C20 alkylsulfonyl or C1-C20 alkyl sulfinyl. The selected R and R1 may optionally be substituted with C 1 -C5 alkyl, halogen, C 1 -C5 alkoxy or with a phenyl group further optionally substituted with halogen, C1-C5 alkyl or C1-C5 alkoxy. X and XI may be the same or different and may be any suitable anionic ligand. NHC may be any N-heterocyclic carbene (NHC) ligand as described below.

Structure 3

[0039] The transition metal compound catalyst may also have the general chemical structure depicted in Structure 4. M may be either ruthenium or osmium. R and R1 may be independently selected from hydrogen, C2-C20 alkenyl, C2-C20 alkynyl, C2-C20 alkyl, aryl, Cl-C20 carboxylate, C1-C20 alkoxy, C2-C20 alkenyloxy, C2-C20 alkynyloxy, aryloxy, C2-C20 alkoxy carbonyl, C1-C20 alkylthio, C1-C20 alkylsulfonyl or C1-C20 alkyl sulfinyl. The selected R and R1 may optionally be substituted with C 1 -C5 alkyl, halogen, C 1 -C5 alkoxy or with a phenyl group further optionally substituted with halogen, C1-C5 alkyl or C1-C5 alkoxy. X and XI may be the same or different and may be any suitable anionic ligand. NHC may be any N-heterocyclic carbene (NHC) ligand as described below.

Structure 4

[0040] The transition metal compound catalysts of Structures 2-4 may further include an N-heterocyclic carbene (NHC) ligand. The NHC ligands may include 4-membered NHC and 5-membered NHC where the NHC ligand may attach to one coordination site of the transition metal compound catalyst. Structures 5-9 are exemplary structures of NHC ligands.

[0041] The NHC ligand may be a 4-membered N-heterocyclic carbene ligand. An exemplary structure of 4-membered carbene ligand is depicted in Structure 5. In the following structure, iPr is an isopropyl group.

Structure 5

[0042] The NHC ligand may also be a 5-membered N-heterocyclic carbene ligand. An exemplary structure of 5 -membered carbene ligands is depicted in Structure 6 and Structure 7. R1 and R2 may be independently selected from 2,4,6-(Me)3C6H2, 2,6-(iPr)2C6H3, cyclohexyl, tertbutyl, 1-adamantyl.

Structure 7

[0043] The NHC ligand may be a 5-membered N-heterocyclic carbene ligand. Another exemplary structure of a 5-membered carbene ligand is depicted in Structure 8. R1 and R2 may be equivalent groups and may be selected from (CH2)n where n may be 4-7 and 12.

Structure 8

[0044] The NHC ligand may be a 5-membered N-heterocyclic carbene ligand. An exemplary structure of 5-membered carbene ligand is depicted in Structure 9. R may be selected between hydrogen and tert-butyl.

Structure 9

[0045] In embodiments, the resin and hardener together may be present in the resin modified cement slurry in an amount of 40% by volume to 99% by volume. Alternatively, from about 40% by volume to 50% by volume, from about 50% by volume to 60% by volume, from about 60% by volume to 70% by volume, from about 70% by volume to 80% by volume, from about 80% by volume to 90% by volume, from about 90% by volume to 99% by volume, or any ranges therebetween. In embodiments, the resin and hardener together may be present in the resin modified cement slurry in an amount of at least 40% by volume of the resin modified cement slurry. Alternatively, in an amount of at least 50% by volume of the resin modified cement slurry, in an amount of at least 60% by volume of the resin modified cement slurry, in an amount of at least 70% by volume of the resin modified cement slurry, in an amount of at least 80% by volume of the resin modified cement slurry, in an amount of at least 90% by volume of the resin modified cement slurry, or in an amount of at least 99% by volume of the resin modified cement slurry.

[0046] In some embodiments, the resin modified cement slurry may be free of epoxy phenol novolak resins. In some embodiments, the resin modified cement slurry may be free of bisphenol A diglycidyl ether resins. In some embodiments, the resin modified cement slurry may be free of napthol-based epoxy resins. In some embodiments, the resin modified cement slurry may be free of naphthalene. In some embodiments, the resin modified cement slurry may be free of epoxy-based resins. In some embodiments, the resin modified cement slurry may be free of bisphenol. In some embodiments, the resin modified cement slurry may be free of novolak resins.

[0047] The water may be from any source provided that it does not contain an excess of compounds that may undesirably affect other components in the resin modified cement slurries. For example, a resin modified cement slurry may include fresh water or saltwater. Saltwater generally may include one or more dissolved salts therein and may be saturated or unsaturated as desired for a particular application. Seawater or brines may be suitable for use in some examples. Further, the water may be present in an amount sufficient to form a pumpable slurry. In certain examples, the water may be present in the resin modified cement slurry in an amount in the range from about 33% to about 200% by weight of the cementitious materials. For example, the water may be present in an amount ranging between any of and/or including any of about 33%, about 50%, about 75%, about 100%, about 125%, about 150%, about 175%, or about 200% by weight of the hydraulic cement or by weight of a dry blend of cementitious materials. The cementitious materials referenced may include all components which contribute to the compressive strength of the resin modified cement slurry such as the hydraulic cement, resin, and supplementary cementitious materials, for example.

[0048] The supplementary cementitious material may be any material that contributes to the compressive strength of the resin modified cement slurry. Some supplementary cementitious materials may include, without limitation, fly ash, blast furnace slag, natural glass, shale, or metakaolin, silica fume, pozzolans, kiln dust, and clays, Portland cements, pozzolana cements, gypsum cements, high alumina content cements, slag cements, high magnesia content cements, shale cements, acid/base cements, fly ash cements, zeolite cement systems, kiln dust cement systems, microfine cements, metakaolin cements, pumice/lime cements, silica cements, and any combination thereof.

[0049] “Fly ash” may be of any grade including those classified as Class C, Class F, or Class N fly ash according to American Petroleum Institute, API Specification for Materials and Testing for Well Cements, API Specification 10, Fifth Ed., July 1, 1990.

[0050] “Kiln dust,” as that term is used herein, refers to a solid material generated as a byproduct of the heating of certain materials in kilns. The term “kiln dust” as used herein is intended to include kiln dust made as described herein and equivalent forms of kiln dust. Depending on its source, kiln dust may exhibit cementitious properties in that it can set and harden in the presence of water. Examples of suitable kiln dusts include cement kiln dust, lime kiln dust, and combinations thereof. Cement kiln dust may be generated as a by-product of cement production

that is removed from the gas stream and collected, for example, in a dust collector. Usually, large quantities of cement kiln dust are collected in the production of cement that are commonly disposed of as waste. The chemical analysis of the cement kiln dust from various cement manufactures varies depending on a number of factors, including the particular kiln feed, the efficiencies of the cement production operation, and the associated dust collection systems. Cement kiln dust generally may include a variety of oxides, such as SiCh, AI2O3, Fe2C>3, CaO, MgO, SO3, Na20, and K2O. The chemical analysis of lime kiln dust from various lime manufacturers varies depending on several factors, including the particular limestone or dolomitic limestone feed, the type of kiln, the mode of operation of the kiln, the efficiencies of the lime production operation, and the associated dust collection systems. Lime kiln dust generally may include varying amounts of free lime and free magnesium, limestone, and/or dolomitic limestone and a variety of oxides, such as SiCh, AI2O3, Fe2C>3, CaO, MgO, SO3, Na20, and K2O, and other components, such as chlorides. Cement kiln dust may include a partially calcined kiln feed which is removed from the gas stream and collected in a dust collector during the manufacture of cement. The chemical analysis of CKD from various cement manufactures varies depending on a number of factors, including the particular kiln feed, the efficiencies of the cement production operation, and the associated dust collection systems. CKD generally may comprise a variety of oxides, such as SiCh, AI2O3, Fe2C>3, CaO, MgO, SO3, Na20, and K2O. The CKD and/or lime kiln dust may be included in examples of the resin modified cement slurry in an amount suitable for a particular application.

[0051] Slag is generally a granulated, blast furnace by-product from the production of cast iron including the oxidized impurities found in iron ore. The resin modified cement slurry may further include perlite. Perlite is an ore and generally refers to a naturally occurring volcanic, amorphous siliceous rock including mostly silicon dioxide and aluminum oxide. The perlite may be expanded and/or unexpanded as suitable for a particular application. The expanded or unexpanded perlite may also be ground, for example. The resin modified cement slurry may further include shale. A variety of shales may be suitable, including those including silicon, aluminum, calcium, and/or magnesium. Examples of suitable shales include vitrified shale and/or calcined shale.

[0052] Zeolites are generally porous alumino-silicate minerals that may be either natural or synthetic. Synthetic zeolites are based on the same type of structural cell as natural zeolites and may comprise aluminosilicate hydrates. As used herein, the term “zeolite” refers to all natural and synthetic forms of zeolite.

[0053] Amorphous silica is generally a byproduct of a ferrosilicon production process, wherein the amorphous silica may be formed by oxidation and condensation of gaseous silicon suboxide, SiO, which is formed as an intermediate during the process. Amorphous silica as a supplemental cementitious material may be included in embodiments to increase cement compressive strength.

[0054] “Hydrated lime” as used herein will be understood to mean calcium hydroxide. In some embodiments, the hydrated lime may be provided as quicklime (calcium oxide) which hydrates when mixed with water to form the hydrated lime. The hydrated lime may be included in examples of the resin modified cement slurry, for example, to form a hydraulic composition with the supplementary cementitious components. For example, the hydrated lime may be included in a supplementary cementitious material-to-hydrated-lime weight ratio of about 10:1 to about 1:1 or 3:1 to about 5:1. In some examples, the hydrated lime may be present in an amount ranging between any of and/or including any of about 10%, about 20%, about 40%, about 60%, or about 80% by weight of the resin modified cement slurry.

[0055] Lime may be present in the resin modified cement slurry in several; forms, including as calcium oxide and or calcium hydroxide or as a reaction product such as when Portland cement reacts with water. Alternatively, lime may be included in the resin modified cement slurry by amount of silica in the resin modified cement slurry. A resin modified cement slurry may be designed to have a target lime to silica weight ratio. The target lime to silica ratio may be a molar ratio, molar ratio, or any other equivalent way of expressing a relative amount of silica to lime. Any suitable target time to silica weight ratio may be selected including from about 10/90 lime to silica by weight to about 40/60 lime to silica by weight. Alternatively, About 10/90 lime to silica by weight to about 20/80 lime to silica by weight, about 20/80 lime to silica by weight to about 30/70 lime to silica by weight, or about 30/70 lime to silica by weight to about 40/63 lime to silica by weight.

[0056] Where used, one or more of the aforementioned supplementary cementitious materials may be present in the resin modified cement slurry. For example, without limitation, one or more supplementary cementitious materials may be present in an amount of about 0.1% to about 80% by weight of the resin modified cement slurry. For example, the perlite may be present in an amount ranging between any of and/or including any of about 0.1%, about 10%, about 20%, about 30%, about 40%, about 50%, about 60%, about 70%, or about 80% by weight of the resin modified cement slurry.

[0057] Other additives suitable for use in accordance with the present disclosure may be included in embodiments of the resin modified cement slurry. Examples of such additives include, but are not limited to: weighting agents, lightweight additives, gas-generating additives, mechanical-property-enhancing additives, lost-circulation materials, filtration-control additives, fluid-loss-control additives, defoaming agents, foaming agents, thixotropic additives, polymeric additives, organophilically modified clay, bentonine, diatomaceous earth, gilsonite, scleroglucan carragenans, xanthan, welan, diutan gums, celluloses, hydroxyl ethyl celluloses, acrylamide polymers, acrylic acid-acrylamide c-opolymers, acrylamide co-polymers, and combinations thereof. In embodiments, one or more of these additives may be added to the resin modified cement slurry after storing but prior to the placement of a resin modified cement slurry into a carbon capture underground storage formation. In some examples, the resin modified cement slurry may further include a dispersant. Examples of suitable dispersants include, without limitation, sulfonated-formaldehyde-based dispersants (e.g., sulfonated acetone formaldehyde condensate) or polycarboxylated ether dispersants. In some examples, the dispersant may be included in the resin modified cement slurry in an amount in the range of from about 0.01% to about 5% by weight of the cementitious materials. In specific examples, the dispersant may be present in an amount ranging between any of and/or including any of about 0.01%, about 0.1%, about 0.5%, about 1%, about 2%, about 3%, about 4%, or about 5% by weight of a cement, slurry, or cementitious components. In some embodiments, suspension additives may be included in any suitable amount, including at a point in a range of from about 0.1% to about 5% by volume of the resin modified cement slurry. Alternatively, from about 0.1% to about 1% by volume, about 1% to about 3% by volume, about 3% to about 5% by volume, or any ranges therebetween.

[0058] In some examples, an additive may comprise a solvent to reduce viscosity of the resin modified cement slurry for ease of handling, mixing, and transferring. Generally, any solvent that is compatible with a curable resin and that achieves the desired viscosity effect may be suitable for use in a resin modified cement slurry. Suitable solvents may include, but are not limited to, polyethylene glycol, butyl lactate, dipropylene glycol methyl ether, dipropylene glycol dimethyl ether, dimethyl formamide, diethyleneglycol methyl ether, ethyleneglycol butyl ether, diethyleneglycol butyl ether, propylene carbonate, d’limonene, fatty acid methyl esters, and combinations thereof. Selection of an appropriate solvent may be dependent on the curable resin chosen. In some examples, the amount of the solvent used in a resin modified cement slurry may be in the range of about 0.1% to about 30% by volume of the resin modified cement slurry. Alternatively, the solvent may be present in an amount of about 0.1% to about 10%, about 10% to about 20%, or about 20% to about 30% by volume of a resin modified cement slurry. Alternatively, a resin modified cement slurry may be heated to reduce its viscosity, in place of, or in addition to, using a solvent.

[0059] In some examples, an additive may include a cement retarder. A broad variety of cement retarders may be suitable for use in the resin modified cement slurries. For example, the cement retarder may comprise phosphonic acids, such as ethylenediamine tetra(methylene phosphonic acid), di ethylenetriamine penta(methylene phosphonic acid), etc.; lignosulfonates, such as sodium lignosulfonate, calcium lignosulfonate, etc.; salts such as stannous sulfate, lead acetate, monobasic calcium phosphate, organic acids, such as citric acid, tartaric acid, etc.; cellulose derivatives such as hydroxyl ethyl cellulose (HEC) and carboxymethyl hydroxyethyl cellulose (CMHEC); synthetic co- or ter-polymers comprising sulfonate and carboxylic acid groups such as sulfonate-functionalized acrylamide-acrylic acid co-polymers; borate compounds such as alkali borates, sodium metaborate, sodium tetraborate, potassium pentaborate; derivatives thereof, or mixtures thereof. Examples of suitable cement retarders include, among others, phosphonic acid derivatives. Generally, the cement retarder may be present in the resin modified cement slurry in an amount sufficient to delay the setting for a desired time. In some examples, the cement retarder may be present in the resin modified cement slurry in an amount in the range of from about 0.01% to about 10% by weight of the cementitious materials. In specific examples, the cement retarder may be present in an amount ranging between any of and/or including any of about 0.01%, about 0.1%, about 1%, about 2%, about 4%, about 6%, about 8%, or about 10% by weight of a cement, slurry, or cementitious components.

CLAIMS

What is claimed is:

1. A method comprising:

introducing a resin modified cement slurry into a wellbore penetrating a subterranean formation, the subterranean formation comprising a caprock and a carbon dioxide injection zone, the resin modified cement slurry comprising:

a resin;

a hardener;

a hydraulic cement; and

water; and

setting the resin modified cement slurry to form a set cement wherein the set cement forms a carbonation-resistant barrier in the carbon dioxide injection zone in the subterranean formation.

2. The method of claim 1 wherein the carbonation-resistant barrier overlaps with the carbon dioxide injection zone and at least one zone selected from the group consisting of a zone comprising the caprock, a zone containing a shoe of a previous casing, a zone containing a liner hanger assembly, and combinations thereof.

3. The method of claim 1 wherein the subterranean formation comprises a depleted reservoir having at least one characteristic selected from the group consisting of pore pressure gradient less than 9 kPa/m, porosity of 5% or greater, permeability of 0.1 mD or greater, and combinations thereof.

4. The method of claim 1 wherein the resin comprises at least one resin selected from the group consisting of cyclic olefins, phenol-aldehyde resins, urea-aldehyde resins, urethane resins, phenolic resins, furan resins, furan and furfuryl alcohol resins, latex resins, phenol formaldehyde resins, butoxymethyl butyl glycidyl ether resins, bisphenol A-epichlorohydrin resins, bisphenol F resins, diglycidyl ether bisphenol F resin, cyclohexane dimethanol diglycidyl ether, glycidyl ether resins, polyester resins and hybrids and copolymers thereof, polyurethane resins and hybrids and copolymers thereof, acrylate resins, a cycloalkene, epoxy-based resins, novolak resins, polyepoxide resins, phenolic resins, bisphenol A diglycidyl ether resins, polyamine resins, and combinations thereof.

5. The method of claim 1 wherein the hardener comprises at least one hardener selected from the group consisting of aromatic amines, transition metal catalysts, aliphatic tertiary amines, aliphatic amines, cycloaliphatic amines, heterocyclic amines, amido amines, polyamides, poly ethyl amines, polyether amines, polyoxyalkylene amines, carboxylic anhydrides, triethylenetetraamine, ethylene diamine, N-cocoalkyltrimethylene, isophorone diamine, N-amino phenyl piperazine, imidazoline, 1,2-diaminocyclohexane, poly ether amine, diethyl toluene diamine, 4,4'-diaminodiphenyl methane, methyltetrahydrophthalic anhydride, hexahydrophthalic anhydride, maleic anhydride, polyazelaic polyanhydride, phthalic anhydride, dialkylated phenylenediamines, and combinations thereof.

6. The method of claim 1 wherein the resin modified cement slurry is free of bisphenol A diglycidyl ether resin and epoxy phenol novolac resin.

7. The method of claim 1 wherein the resin comprises a cycloalkene and the hardener comprises a transition metal compound catalyst, wherein the transition metal compound catalyst comprises a catalyst having a structure selected from the group consisting of:

Structure 3; and

Structure 4,

where M is ruthenium or osmium, R and R1 are independently selected from hydrogen, C2-C20 alkenyl, C2-C20 alkynyl, C2-C20 alkyl, aryl, C1-C20 carboxylate, C1-C20 alkoxy, C2-C20 alkenyloxy, C2-C20 alkynyloxy, aryloxy, C2-C20 alkoxy carbonyl, C1-C20 alkylthio, Cl-C20 alkylsulfonyl or C1-C20 alkyl sulfinyl, X and XI are each an anionic ligand, L and LI are each a neutral electron donor, and NHC is an N-heterocyclic carbene ligand.

8. The method of claim 7 wherein the cycloalkene is selected from the group consisting of cyclopentadiene, dicyclopentadiene, tricyclopentadiene, cyclobutadiene, cyclobutadiene derivatives, cyclohexadiene, terpinene, norbomadiene, isomers thereof, and combinations thereof.

9. The method of claim 7 wherein the resin and the transition metal compound catalyst are present in a mass ratio of about 50:1 to about 10000:1 of the resin to the transition metal compound catalyst.

10. The method of claim 1 wherein the resin and the hardener are present in a combined amount of about 5% to about 50% by volume of the resin modified cement slurry.

11. The method of claim 1 wherein the resin is present in the resin modified cement slurry in an amount from about 1% to about 20% by weight of the resin modified cement slurry and wherein the hardener is present in the resin modified cement slurry in an amount from about 0.05% to about 5% by weight of the resin modified cement slurry.

12. The method of claim 1 wherein the resin modified cement slurry further comprises at least one supplementary additive selected from the group consisting of supplementary cementitious components, hydraulic binders, micronized solids, inert solid particulates or microparticles, hollow microspheres, low-density elastic beads, weighting agents, lightweight additives, gasgenerating additives, mechanical-property-enhancing additives, lost-circulation materials,

filtration-control additives, fluid-loss-control additives, defoaming agents, foaming agents, thixotropic additive, dispersants, retarders, accelerators, and combination thereof.

13. A method comprising:

providing a carbon capture underground storage system, wherein the carbon capture underground storage system comprises:

a wellbore penetrating a subterranean formation comprising a carbon dioxide injection zone; and

a carbonation-resistant barrier, wherein the carbonation-resistant barrier comprises a set cement formed from a resin modified cement slurry comprising a resin, a hardener, a hydraulic cement, and water, and wherein the carbonation-resistant barrier overlaps with at least a portion of the carbon dioxide injection zone in the subterranean formation;

introducing carbon dioxide into the carbon capture underground storage system; and flowing the carbon dioxide into the carbon dioxide injection zone.

14. The method of claim 13 wherein the resin comprises an epoxy -based resin, wherein the hardener comprises diethyl toluene diamine, and wherein the hydraulic cement comprises a Portland cement.

15. The method of claim 13 wherein the resin comprises a cycloalkene and the hardener comprises a transition metal compound catalyst, wherein the transition metal compound catalyst comprises a catalyst having a structure selected from the group consisting of:

Structure 1;

Structure 4,

where M is ruthenium or osmium, R and R1 are independently selected from hydrogen, C2-C20 alkenyl, C2-C20 alkynyl, C2-C20 alkyl, aryl, C1-C20 carboxylate, C1-C20 alkoxy, C2-C20 alkenyloxy, C2-C20 alkynyloxy, aryloxy, C2-C20 alkoxy carbonyl, C1-C20 alkylthio, Cl-C20 alkylsulfonyl or C1-C20 alkyl sulfinyl, X and XI are each an anionic ligand, L and LI are each a neutral electron donor, and NHC is an N-heterocyclic carbene ligand.

16. The method of claim 13 wherein the cycloalkene is selected from the group consisting of cyclopentadiene, dicyclopentadiene, tricyclopentadiene, cyclobutadiene, cyclobutadiene derivatives, cyclohexadiene, terpinene, norbomadiene, isomers thereof, and combinations thereof.

17. The method of claim 13 wherein the resin and the transition metal compound catalyst are present in a mass ratio of about 50: 1 to about 10000: 1 of the resin to the transition metal compound catalyst

18. The method of claim 13 wherein the resin and the hardener are present in a combined amount of about 5% to about 50% by volume of the resin modified cement slurry.

19. The method of claim 13 wherein the carbon dioxide injection zone comprises at least one zone selected from the group consisting of a highly porous or permeable formation, a depleted reservoir, a depleted formation, a salt cavern, and combinations thereof.

20. The method of claim 13 wherein the carbon dioxide is introduced into the carbon capture underground storage system as a gas, a liquid, a vapor, a supercritical fluid, or a combination thereof.

Documents

Application Documents

# Name Date
1 202427100988-REQUEST FOR EXAMINATION (FORM-18) [19-12-2024(online)].pdf 2024-12-19
2 202427100988-PROOF OF RIGHT [19-12-2024(online)].pdf 2024-12-19
3 202427100988-PRIORITY DOCUMENTS [19-12-2024(online)].pdf 2024-12-19
4 202427100988-POWER OF AUTHORITY [19-12-2024(online)].pdf 2024-12-19
5 202427100988-FORM 18 [19-12-2024(online)].pdf 2024-12-19
6 202427100988-FORM 1 [19-12-2024(online)].pdf 2024-12-19
7 202427100988-FIGURE OF ABSTRACT [19-12-2024(online)].pdf 2024-12-19
8 202427100988-DRAWINGS [19-12-2024(online)].pdf 2024-12-19
9 202427100988-DECLARATION OF INVENTORSHIP (FORM 5) [19-12-2024(online)].pdf 2024-12-19
10 202427100988-COMPLETE SPECIFICATION [19-12-2024(online)].pdf 2024-12-19
11 Abstract.jpg 2025-01-17
12 202427100988-FORM 3 [12-06-2025(online)].pdf 2025-06-12
13 202427100988-Proof of Right [18-06-2025(online)].pdf 2025-06-18