Oxidizers for carbon dioxide-based fracturing fluids

Abstract

A method for treating kerogen in a subterranean zone which includes the use of supercritical carbon dioxide or emulsions of liquid carbon dioxide and an aqueous fluid. The carbon dioxide or emulsions can further include oxidizers. The oxidizers can include inorganic oxidizers or organic oxidizers, for example an oxidizer including an organic cation and an oxidizing anion. Additional additives such as polymers, crosslinkers, clay inhibitors, scale inhibitors and corrosion inhibitors can further enhance the efficiency of the kerogen-treating carbon dioxide or emulsion.

Description

TECHNICAL FIELD

This document relates to methods and compositions used in treating subterranean formations for enhancing hydrocarbon fluid recovery.

BACKGROUND

Unconventional source rock reservoirs differ from conventional reservoirs due to the presence of the hydrocarbon source material, that is, a Total Organic Content (TOC) including kerogen, bitumen and other organics. Kerogen is an irregular organic material that often represents 5 to 10 percent by weight (wt %) (10 to 20 percent by volume (vol %)) of a sedimentary source rock formation. In source rock formations, clay and non-clay minerals are woven and compacted together with the kerogen to form a complex hierarchical structure with mechanical and physical parameters similar to other porous natural materials. The polymeric nature of kerogen with its chemomechanical characteristics interwoven with the granular material results in a problematic role that these composite materials play, first in increasing the tensile strength resistance generated during hydraulic fracturing, and second in masking the capacity of the fracture faces to communicate with the main fracture. The interwoven polymer characteristics of kerogen present a challenge that needs to be addressed in optimizing hydraulic fracturing operations and the overall formation productivity.

Early developments in hydraulic fracturing have resulted in fracturing fluids with additives such as polymers or crosslinkers or both. These viscosified fracturing fluids were designed to move and evenly distribute proppant in the main fracture, while other additives, such as polymer breakers, biocides, clay swelling inhibitors, and scale inhibitors, were added to improve the hydraulic fracturing operations. Additionally, slickwater systems have been developed for stimulating unconventional formations. Slickwater incorporates a friction-reducing synthetic polymer, which increases the rate at which stimulation fluids may be pumped. Fracturing fluids incorporating gas or other components to reduce or eliminate water altogether are also used in fracturing operations.

SUMMARY

This disclosure describes organic and inorganic oxidizers for carbon dioxide (CO₂)-based hydraulic fracturing fluids.

In some implementations, a method for treating kerogen or organic matter in a subterranean zone includes placing a composition in the subterranean zone. The composition includes carbon dioxide and a fluid including an oxidizer. The fluid is an aqueous fluid. The composition includes an emulsion of carbon dioxide and the aqueous fluid.

In some implementations, a composition for treating kerogen in a subterranean zone includes carbon dioxide and a fluid including an oxidizer. The fluid is an aqueous fluid. The composition includes an emulsion of carbon dioxide and the aqueous fluid.

In some implementations, a method of making a hydraulic fracturing fluid includes adding a quantity of a composition to a hydraulic fracturing fluid. The composition includes carbon dioxide and a fluid including an oxidizer. The fluid is an aqueous fluid. The composition includes an emulsion of carbon dioxide and aqueous fluid. The method further includes mixing the hydraulic fracturing fluid and the composition.

In some implementations, a method of making a kerogen breaking composition includes reacting two or more salts to form a composition with an organic cation and an oxidizing anion, and adding the composition to carbon dioxide (CO₂).

The following units of measure have been mentioned in this disclosure:

Unit of Measure Full form
mL              milliliter
uL              microliter
mmol            millimole
g               gram
kDa             kilodalton
cm              centimeter
h               hour
° C.            degree Celsius
M.P.            melting point

The details of one or more implementations of the disclosure are set forth in the accompanying drawings and the description that follows. Other features, objects, and advantages of the disclosure will be apparent from the description and drawings, and from the claims.

DESCRIPTION OF DRAWINGS

FIG. 1 shows example structures of butylammonium cations.

FIG. 2 shows example structures of organic cations.

FIG. 3 shows an example of a fracture treatment for a well.

FIG. 4 is a flow chart of an example method for treating a well.

Like reference symbols in the various drawings indicate like elements.

DETAILED DESCRIPTION

Reference will now be made in detail to certain implementations of the disclosed subject matter, examples of which are illustrated in part in the accompanying drawings. While the disclosed subject matter will be described in conjunction with the enumerated claims, it will be understood that the exemplified subject matter is not intended to limit the claims to the disclosed subject matter.

Provided in this disclosure, in part, are methods, compositions, and systems for degrading organic matter, such as kerogen, in a subterranean formation. Implementations of the disclosure include reactive fluids that can break down the polymeric nature of the kerogen and other organic matter on the hydraulic fracture faces. Water-based fracturing fluids with a reactive nature, which were previously developed for source rock reservoirs, have now been extended to CO₂-based systems. A synthetic strategy was developed where oxidizing anions are paired with organic cations that render the oxidizing compounds soluble or dispersible in CO₂ while still being reactive towards kerogen. Implementing the strategy can enhance the hydraulic conductivity and formation communication with the main fracture. In this manner, implementations of the disclosure can optimize hydraulic fracturing and overall formation productivity in unconventional source rock reservoirs. Further, these methods, compositions, and systems allow for increased hydraulic fracturing efficiencies in subterranean formations, such as unconventional rock reservoirs.

In some implementations, hydraulic fracturing is performed using a hydraulic fracturing fluid that includes supercritical CO₂ or liquid CO₂.

This disclosure describes reactive compounds, for example, synthetic oxidizers, which are both soluble in supercritical CO₂ or liquid CO₂ and capable of degrading organic material such as kerogen. The oxidizers can be directly soluble in CO₂ or dispersed in it as droplet or slurry. The oxidizers include both inorganic and organic oxidizers.

In some implementations, these oxidizers include chlorate or bromate which are known to degrade kerogen in combination with organic cations that render the compound soluble or dispersible in CO₂.

In some implementations, oxidizers capable of degrading kerogen can be present in an emulsion of aqueous fluid with liquid CO₂. The process of making an emulsion of a water-in-CO₂ or CO₂-in-water containing oxidizers involves dissolving the oxidizer in either water or CO₂, providing an emulsifier/surfactant at 0.01 to 2 wt %, followed by introduction of the other solvent (water if the initial solvent was CO₂). The oxidizer should be soluble or dispersible in the first phase of the mixing process (for example, sodium bromate in water).

Examples of surfactants suitable for creating emulsions include perfluoropolyethers, polysorbates, and other cationic and anionic surfactants. For example, water-in-CO₂ emulsions can be formed by perfluoropolyether ammonium carboxylate surfactants with molecular weights of 500 to 10,000 Da, for example, compounds with the general formula CF₃—(O—CF₂—CF(CF₃))_n—(O—CF₂)—COO⁻ NH₄⁺. These surfactants are highly soluble in CO₂ (>5 wt %) and less soluble in water (<0.01 wt %).

In another example, beta-lactoglobulin can form CO₂-in-water emulsions at pressures between 40-100 bar.

Polysorbates such as polysorbate 80 can be used to form CO₂-in-water and water-in-CO₂ emulsions. At pressures up to 250 bar and temperatures between 25-60° C., CO₂-in-water emulsions are formed for water concentrations at or greater than 10%. On the addition of NaCl or other inorganic salts, the surfactant partitions away from water towards CO₂ and water-in-CO₂ emulsions are formed. Other cationic-anionic surfactants can be used to form water-in-CO₂ emulsions, such as [C₆F₁₃methylimidazolium][C₆F₁₃S], [C₅F₁₁methylimidazolium][C₅F₁₁S], [C₆F₁₃methylimidazolium][(CF₃)₃S]. C₆F₁₃methylimidazolium, C₅F₁₁methylimidazolium, [C₆F₁₃S], [C₅F₁₁S] and [(CF₃)₃S] are shown in Table 1, where the abbreviation “mim” represents methylimidazolium.

TABLE 1
Chemical Structures of Surfactant Ions
[C6F13S]
[C5F11S]
[(CF3)3S]
[C6F13mim]
[C5F11mim]

Other surfactants that are used to form water-in supercritical CO₂ microemulsions are sodium 1-oxo-1-[4-(perfluorohexyl)phenyl]hexane-2-sulfonate and 1-oxo-1-[4-(hexyl)phenyl]-2-hexanesulfonates.

In some implementations, an emulsion of aqueous fluid and liquid CO₂ can include the aqueous fluid as the internal phase and the liquid CO₂ as the external phase. The emulsion can include hydrophobic particles, including but not limited to particles of polytetrafluoroethylene, carbon black, or pulverized coal, where the hydrophobic particles stabilize the emulsion.

In some implementations, an emulsion of aqueous fluid and liquid CO₂ can include the liquid CO₂ as the internal phase and the aqueous fluid as the external phase. The emulsion can include hydrophilic particles including but not limited to limestone, silica, fly ash, shale, or magnesium silicate to stabilize the emulsion. The compositions described within this disclosure can be used as a kerogen control material to break down, dissolve, or remove all or parts of the kerogen in or near the areas to be hydraulically fractured in a subterranean formation. Using a composition described within this disclosure, the kerogen or other organic matter (or both) can be broken down by, for example, pumping the composition into a subterranean formation.

The compounds soluble in CO₂ include oxidizers. The oxidizers can include organic cations and oxidizing anions. For example, organic cations include but are not limited to ammonium (NH₄⁺) substituted with methyl, ethyl, propyl, hexadecyl and phenyl groups, and butylammonium cations, such as BuNH₃⁺, Bu₂NH₂⁺, Bu₃NH⁺ and Bu₄N⁺. FIG. 1 shows some example structures from the butylammonium cations, including unsubstituted NH₄⁺ (FIG. 1A), BuNH₃⁺ (FIG. 1B), Bu₂NH²⁺ (FIG. 1C), Bu₃NH⁺ (FIG. 1D) and Bu₄N⁺ (FIG. 1E). Other organic cations suitable for pairing with oxidizing anions include tetraphenylphosphinium [Ph₄P]⁺, bis(triphenylphosphine)iminium [PPN]⁺, pyridinium [Pyr]⁺, pyrrolidinium [Pyrr]⁺, and imidazolium [Im]⁺. FIG. 2 shows some example structures of these organic cations, including tetraphenylphosphinium [Ph₄P]⁺ (FIG. 2A), bis(triphenylphosphine)iminium [PPN]⁺ (FIG. 2B), pyridinium [Pyr]⁺ (FIG. 2C), pyrrolidinium [Pyrr]⁺ (FIG. 2D), and imidazolium [Im]⁺ (FIG. 2E). These organic cations can also be further substituted, with additional functional groups, for example, 1-butyl-3-methyl-imidazolium [BMIm]⁺. In addition, the organic cations can be partially or fully fluorinated. Suitable oxidizing anions include but are not limited to chlorate and bromate.

In addition, compounds soluble in CO₂ include organic peroxides, such as hydroperoxides, peroxy acids and esters, diacyl peroxides, and dialkylperoxides.

The compounds soluble in water include aqueous oxidizers including, for example, sodium bromate, potassium bromate, sodium chlorate, potassium chlorate, sodium chlorite, potassium chlorite, sodium perchlorate, potassium perchlorate, sodium persulfate, ammonium persulfate, potassium persulfate, sodium perborate, potassium perborate, sodium percarbonate, potassium percarbonate, sodium hypochlorite, potassium hypochlorite, sodium nitrite, potassium nitrite, ammonium nitrite, sodium nitrate, potassium nitrate, ammonium nitrate, calcium peroxide, magnesium peroxide, hydrogen peroxide, or any combination of them.

In addition, organic oxidizers as described in any of the other implementations can also be used in an emulsion with liquid CO₂. The organic oxidizers as described in any of the other implementations can also be dissolved or dispersed in CO₂, or dissolved or dispersed in a fluid including CO₂.

Depending on the exact nature of the cation and anions combined, the resulting salt can be either a solid or liquid at room temperature.

The concentration of the components of the composition (for example, the oxidizers, ions, fine particles, or a combination of the same) can depend on the quantity of kerogen or other organic matter in the reservoir rock. For example, the concentration of the oxidizer in the composition can be increased for formations in response to the quantity of organic matter to be removed or partially removed.

The composition can also include other fracturing fluid additives including but not limited to polymer, crosslinker, surfactant, clay inhibitor, scale inhibitor, corrosion inhibitor.

Polymers can be added to viscosify the CO₂. Suitable polymers include fluorinated or oxygenated polymers which can self-assemble or are crosslinked. In some implementations, polymers can be added at a concentration of 0.1-10 wt %. Crosslinkers can optionally be added based on the specific polymer used, and can be used to crosslink polymers to add more viscosity.

Surfactants in the composition can enhance flowback of fluid from the reservoir to the surface. Suitable surfactants include zwitterionic/amphoteric surfactants, for example betaine, phosphobetaine, and sultaine. Suitable surfactants also include cationic surfactants, for example quaternary ammonium compounds, anionic surfactants, for example alkyl sarcosinate or alkyl sulfonate, or non-ionic surfactants, for example amido amino oxides. In some implementations, surfactants are added at 0.01-2 wt %.

Clay inhibitors in the composition can prevent clay swelling in the presence of water. Clay inhibitors include quaternary ammonium compounds. As some of the oxidizers used in the composition include quaternary ammonium compounds (for example, tetramethylammonium bromate and tetramethylammonium chloride), the organic component of the oxidizers can serve as a clay inhibitor. Alternatively, the clay inhibitor may consist of a polyamine, quaternary ammonium compound, or alkali metal salt. In some implementations, clay inhibitors are added to the composition at 0-5 wt %, preferably 0-1 wt %.

Scale inhibitors in the composition can prevent precipitation of minerals in the formation as a result of the composition interacting with the rock and its native brine. Scale inhibitors include polyphosphates, phosphate esters, polyacrylic acid derivatives, and chelating agents, for example, EDTA. In some implementations, scale inhibitors are added to the composition at 0-5 wt %, preferably 0-1 wt %.

Corrosion inhibitors in the composition can prevent corrosion of well tubulars by the composition components, for example the oxidizers. Corrosion inhibitors include amides, imidazolines, salts of nitrogenous bases, nitrogen quaternaries, polyoxylated amines, polyoxylated amides, polyoxylated imidazolines, mercaptan modified products, nitrogen heterocyclics, carbonyl compounds, silicate-based inhibitors, and thioacetals. In some implementations, corrosion inhibitors can be added to the composition at 0-5 wt %, for example, 0-1 wt %.

The composition can further include a fracturing fluid or a pad fluid and can be pumped into a subterranean formation before fracturing, during fracturing, or both. In some implementations, the release of the composition including oxidizers can be delayed from a carrier fluid. Delaying the release of the composition from a carrier fluid can be accomplished by encapsulating the composition. In some implementations, the composition can be encapsulated with coatings through which the composition can be slow-released, for example, where the coating slowly degrades so that the encapsulated composition is released a fraction at a time, rather than all at once. Alternatively, or in addition, the coatings can break during fracture closure to release the composition. The composition can be a solid or a powder that can be encapsulated. A delayed release of the composition can decrease corrosion issues (for example, in metal tubing in the wellbore through which the fluids are delivered to the formation) and polymer degradation in the treating fluid. The polymers subject to degradation include, for example, friction reducers.

In some implementations, one or more fluids are placed in the subterranean zone, for example alternating between placing the composition and placing a second fluid.

FIG. 3 illustrates an example of a fracture treatment 10 for a well 12. The well 12 can be a reservoir or formation 14, for example, an unconventional reservoir in which recovery operations in addition to conventional recovery operations are practiced to recover trapped hydrocarbons.

The well 12 can include a well bore 20, casing 22 and well head 24. The well bore 20 can be a vertical or deviated bore.

For the fracture treatment 10, a work string 30 can be disposed in the well bore 20. A fracturing tool 32 can be coupled to an end of the work string 30. Packers 36 can seal an annulus 38 of the well bore 20 above and below the formation 14.

One or more pump trucks 40 can be coupled to the work string 30 at the surface 25. The pump trucks 40 pump fracture fluid 58 down the work string 30 to perform the fracture treatment 10 and generate the fracture 60. The fracture fluid 58 can include a fluid pad, proppants and/or a flush fluid.

One or more instrument trucks 44 can also be provided at the surface 25. The instrument truck 44 can include a fracture control system 46 and a fracture simulator 47. The fracture control system 46 monitors and controls the fracture treatment 10.

A quantity of energy applied by the fracture control system 46 to generate the fractures 60 in the reservoir or formation 14 can be affected not only by the properties of the reservoir rock in the formation but also by the organic matter (for example, kerogen 75) intertwined within the rock matrix. As discussed within this disclosure, kerogen in a reservoir can increase the tensile strength of the rock, for example, by as much as 100-fold, resulting in a corresponding increase in the ultimate tensile strength of the rock. The high modulus of toughness of the rock-kerogen combination compared to the rock alone can require a large quantity of energy to generate fractures in such a reservoir. Moreover, the presence of kerogen in the reservoir can affect production as well. For example, the rubber-like properties of elastomeric kerogen has a high elasticity, which can prematurely close fractures resulting in a decrease in production. Accordingly, the presence of kerogen in a subterranean formation can decrease an efficiency of hydraulic fracturing treatments.

This specification describes compositions 81 to degrade the kerogen encountered in subterranean formations, such as at the openings of cracks in hydraulic fractures. The compositions can include hydraulic fracturing fluids (for example, the fracture fluid 58) that are flowed through the subterranean formation (for example, a reservoir). As or after the kerogen is degraded, a quantity of energy to generate and propagate fractures in the subterranean formation (for example, a reservoir) can decrease, thereby increasing an efficiency (for example, cost, time, long-term effect) of the fracturing process. In addition, fracture length and formation surface exposure after wellbore shut-in can be greater than corresponding parameters in reservoirs in which the kerogen has not been degraded. In addition, removing or partially removing the kerogen and other organic matter from the near fracture zone can decrease the propensity for the fractures to close (reheal) after the pressure is released from pumping the fracturing, thereby improving the overall productivity of the well.

This application describes the creation of synthetic organic oxidizers that are soluble or dispersible in CO₂. The synthetic alkylammonium bromates and chlorates described in this application can be created by a double displacement reaction of [RR′₃N]₂SO₄ with BaXO₃ to yield [RR′₃N]XO₃ and BaSO₄ (R=alkyl, R′═H, alkyl, X═Br, Cl).

Example 1, Preparation of Tetrabutylammonium Bromate ([Bu₄N]BrO₃)

In a 250 mL Erlenmeyer flask, 0.9 g (2.29 mmol) of barium bromate (Ba(BrO₃)₂) were added to 100 mL of deionized water (DI H₂O) and the mixture was stirred. To this mixture was added 2.66 g of a 50 wt % tetrabutylammonium sulfate solution (2.29 mmol). The mixture instantly turned a milky white. The mixture was stirred for 3 hours. The mixture was then allowed to stand for 20 hours. The mixture was then filtered to remove barium sulfate (BaSO₄). The reaction yield of the product, [Bu₄N]BrO₃, was 1.66 g (99% yield). Infrared spectroscopy of the product revealed the following spectrum: wavenumber (υ), cm⁻¹=2950 (vs), 2905 (vs), 2840 (vs), 2740 (w), 2100 (w, br), 1650 (s), 1480 (vs), 1385 (s) 1290 (w), 1250 (w), 1170 (m), 1100 (s) 1060 (s) 1020 (m), 880 (s), 800 (vs). Melting point analysis of the product revealed a melting point of 54° C. In the previous sentence, “vs,” “s,” “m,” “w,” “sh,” and “br” stand for very strong, strong, moderate, weak, sharp and broad, respectively.

Example 2, Preparation of Tributylammonium Bromate ([Bu₃NH]BrO₃)

In a 125 mL Erlenmeyer flask, 0.5 mL (2.1 mmol) of tributylamine was added to 20 mL of DI H₂O. Next, 57 μL of 98% sulfuric acid (H₂SO₄) (1.1 mmol) was added to the mixture. Then, the mixture was sonicated for 5 minutes. The result was a tributylammonium sulfate solution. Separately, 0.42 g (1.1 mmol) of Ba(BrO₃)₂ were added to 80 mL of DI H₂O. This mixture was sonicated for 5 minutes. The tributylammonium sulfate solution was then added rapidly to the Ba(BrO₃)₂ solution. The resulting mixture was sonicated for 30 minutes. Then the mixture was vacuum filtered twice to give a clear solution. Water was then removed under vacuum. The product, [Bu₃NH]BrO₃, was a colorless liquid at room temperature. Infrared spectroscopy of the product revealed the following spectrum: υ (cm⁻¹)=3430 (m, br), 2960 (st), 2935 (m), 2873 (m), 1722 (vw), 1628 (m), 1460 (m), 1381 (w), 1066 (w), 786 (vs, sh), 768 (vs), 740 (s, sh).

Example 3, Preparation of Dibutylammonium Bromate ([Bu₂NH₂]BrO₃)

In a 125 mL Erlenmeyer flask, 0.5 mL (3.3 mmol) of dibutylamine was added to 20 mL of DI H₂O. To this mixture was added 88 uL of 98% H₂SO₄ (1.6 mmol). The resulting mixture was sonicated for 5 minutes, resulting in a dibutylammonium sulfate solution. Separately, 0.64 g (1.6 mmol) of Ba(BrO₃)₂ were added to 80 mL of deionized H₂O and sonicated for 5 minutes. Then, the dibutylammonium sulfate solution was added rapidly to the Ba(BrO₃)₂ solution. The resulting mixture was sonicated for 30 minutes. Next, the mixture was vacuum filtered twice to give a clear solution. Water was removed from the solution under vacuum. The resulting product, [Bu₂NH₂]BrO₃, is a colorless liquid at room temperature. Infrared spectroscopy of the product revealed the following spectrum: υ (cm⁻¹)=3430 (m, br), 2960 (st), 2935 (m), 2873 (m), 1722 (vw), 1628 (m), 1617 (m), 1460 (m), 1381 (w), 1066 (w), 915 (w), 780 (vs), 727 (vs). Melting point analysis of the product revealed a melting point of 4° C.

Example 4, Preparation of Butylammonium Bromate, [BuNH₃]BrO₃

In a 125 mL Erlenmeyer flask, 0.33 mL (3.3 mmol) of butylamine were added to 20 mL of DI H₂O. To this mixture was added 88 uL of 98% H₂SO₄, (1.6 mmol). The resulting mixture was sonicated for 5 minutes, to yield a butylammonium sulfate solution. Separately, 0.64 g (1.6 mmol) of Ba(BrO₃)₂ were added to 80 mL of DI H₂O and sonicated for 5 minutes. Then, the butylammonium sulfate solution was rapidly added to the Ba(BrO₃)₂ solution. The resulting mixture was sonicated for 30 minutes and vacuum filtered twice to give a clear solution. Water was removed from the solution under vacuum. The yield of the product, [BuNH₃]BrO₃, was 0.65 g (97% yield). Infrared spectroscopy of the product revealed the following spectrum: υ (cm⁻¹)=3041 (st, br), 2960 (st), 2935 (m), 2875 (m), 1606 (m), 1600 (m), 1570 (s), 1174 (m), 1077 (m), 915 (m), 830 (s), 768 (vs), 757 (vs).

Example 5, Preparation of Tetrabutylammonium Chlorate ([Bu₄N]ClO₃)

In a 250 mL Erlenmeyer flask, 0.76 g (2.29 mmol) of barium chlorate (Ba(ClO₃)₂) was added to 100 mL of DI H₂O and the mixture was stirred. To this mixture was added 2.66 g of a 50 wt % tetrabutylammonium sulfate solution (2.29 mmol). The mixture instantly turned a milky white. The mixture was stirred for 3 hours. Then, the mixture was allowed to stand for 20 hours. The mixture was then filtered to remove the BaSO₄. The yield of the product, [Bu₄N]ClO₃, was 0.73 g (98% yield). Infrared spectroscopy of the product revealed the following spectrum: υ(cm⁻¹)=2960 (m), 2935 (m), 2875 (m), 1476 (w), 1472 (w), 1381 (w), 1650 (s), 954 (vs), 930 (vs), 881 (m), 800 (w), 740 (m). Melting point analysis revealed a melting point of 116-118° C.

Example 6, Preparation of bis(Triphenylphosphine)iminium Bromate ([PPN]BrO₃)

In a 120 mL glass tube, 4.0 g (26.5 mmol) of sodium bromate (NaBrO₃) were dissolved in 30 mL of DI H₂O. To this solution was added 1.0 g (1.86 mmol) of bis(triphenylphosphine)iminium chloride and the solution was heated at 100° C. for 15 minutes without stirring. Over the course of this time, a liquid formed and collected at the bottom of the tube. Upon cooling, this material crystallized and was isolated by filtration. Recrystallization of this material in 15 mL of DI H₂O yielded 0.88 g of the product, [PPN]BrO₃ (71% yield). Infrared spectroscopy of the product revealed the following spectrum: IR (cm⁻¹), υ=3170 (w) 3150 (w) 3040 (s) 3010 (s), 2990 (s) 2700 (w) 2600 (w) 2230 (w) 2100 (w), 2080 (w), 2050 (w) 2000 (w), 1900 (w), 1830 (w), 1800 (w), 1780 (w) 1670 (w) 1600 (vs), 1480 (vs), 1420 (vs) 1300 (vs, br), 1190 (vs) 1100 (vs), 1020 (vs), 1000 (vs) 930 (w), 840 (vs), 790 (vs). Melting point analysis revealed a melting point of 236-238° C.

Example 7, Preparation of Pyridinium Bromate, ([PyrH]BrO₃)

First, 0.5 mL (6.6 mmol) of pyridine was added to 10 mL of DI H₂O. Next, 180 uL of concentrated H₂SO₄ (18.4 M) was added to the solution. The solution was stirred for two hours. This solution was then added to a second solution of 1.3 g (3.3 mmol) of Ba(BrO₃)₂ in 120 mL of water. The resulting mixture was sonicated for two hours. Then, the mixture was allowed to settle and was vacuum filtered. The water was removed with a rotary evaporator. The product, [PyrH]BrO₃, was a colorless liquid. The yield of the product was 1.36 g (98% yield).

FIG. 4 is a flowchart of an example of a process 200 for degrading kerogen in a subterranean zone. The process can be implemented using different types of hydraulic fracturing fluids, for example, fracturing fluid including aqueous oxidizers, with or without proppant; fracturing fluids including organic oxidizers, with or without proppant; fracturing fluids including an emulsified oxidizer, with or without proppant; fracturing fluid including aqueous, organic, or emulsified oxidizers pumped with nanoproppant; or fracturing fluid including aqueous, organic, or emulsified oxidizers pumped with degradable nanoparticles such as poly(lactic acid) (PLA) or poly(glycolic acid) (PGA). At 201, a kerogen- and organic matter-degrading composition (for example, a composition including an oxidizer, such as an alkylammonium bromate) is mixed with a fluid. The fluid can be a hydraulic fracture fluid or a pad fluid that is flowed into the reservoir before the hydraulic fracture fluid (or both). At 205, the fluid (with the kerogen- and organic matter-degrading composition) is flowed into the reservoir as part of a hydraulic fracture treatment. As described previously, the kerogen and organic matter degrade upon reacting with the composition. At 203, an additive, such as polymer, crosslinker, breaker, surfactant, scale inhibitor, corrosion inhibitor, or flowback aid, can be added to the mixture of the composition and the fluid before pumping the fluid into the reservoir at 205. Other potential additives include any material that is compatible with the kerogen- and organic matter-degrading composition.

The term “about” as used in this disclosure can allow for a degree of variability in a value or range, for example, within 10%, within 5%, or within 1% of a stated value or of a stated limit of a range.

The term “substantially” as used in this disclosure refers to a majority of, or mostly, as in at least about 50%, 60%, 70%, 80%, 90%, 95%, 96%, 97%, 98%, 99%, 99.5%, 99.9%, 99.99%, or at least about 99.999% or more.

The term “solvent” as used in this disclosure refers to a liquid that can dissolve a solid, another liquid, or a gas to form a solution. Non-limiting examples of solvents are silicones, organic compounds, water, alcohols, hydrocarbons, ionic liquids, and supercritical fluids.

The term “room temperature” as used in this disclosure refers to a temperature of about 15 degrees Celsius (° C.) to about 28° C.

The term “downhole” as used in this disclosure refers to under the surface of the earth, such as a location within or fluidly connected to a wellbore.

As used in this disclosure, the term “fracturing fluid” refers to fluids or slurries used downhole during fracturing operations.

As used in this disclosure, the term “fluid” refers to liquids and gels, unless otherwise indicated.

As used in this disclosure, the term “subterranean material” or “subterranean zone” refers to any material under the surface of the earth, including under the surface of the bottom of the ocean. For example, a subterranean zone or material can be any section of a wellbore and any section of a subterranean petroleum- or water-producing formation or region in fluid contact with the wellbore. Placing a material in a subterranean zone can include contacting the material with any section of a wellbore or with any subterranean region in fluid contact the material. Subterranean materials can include any materials placed into the wellbore such as cement, drill shafts, liners, tubing, casing, or screens; placing a material in a subterranean zone can include contacting with such subterranean materials. In some examples, a subterranean zone or material can be any downhole region that can produce liquid or gaseous petroleum materials, water, or any downhole section in fluid contact with liquid or gaseous petroleum materials, or water. For example, a subterranean zone or material can be at least one of an area desired to be fractured, a fracture or an area surrounding a fracture, and a flow pathway or an area surrounding a flow pathway, in which a fracture or a flow pathway can be optionally fluidly connected to a subterranean petroleum- or water-producing region, directly or through one or more fractures or flow pathways.

In some implementations, a method for treating kerogen or organic matter in a subterranean zone includes placing a composition in the subterranean zone. The composition includes carbon dioxide and a fluid including an oxidizer. The fluid is an aqueous fluid. The composition includes an emulsion of carbon dioxide and the aqueous fluid.

This aspect, taken alone or combinable with any other aspect, can include the following features. The method further includes alternating placing the composition in the subterranean zone with placing a second fluid in the subterranean zone.

This aspect, taken alone or combinable with any other aspect, can include the following features. The oxidizer includes a cation and an anion.

This aspect, taken alone or combinable with any other aspect, can include the following features. The anion includes at least one of chlorate or bromate.

This aspect, taken alone or combinable with any other aspect, can include the following features. The cation includes at least one of an ammonium ion, a butylammonium ion, a dibutylammonium ion, a tributyl ammonium ion, or a tetrabutylammonium ion.

This aspect, taken alone or combinable with any other aspect, can include the following features. The cation includes at least one of an ammonium ion substituted with alkyl or phenyl groups, bis(triphenylphosphine)iminium, or tetraphenylphosphinium.

This aspect, taken alone or combinable with any other aspect, can include the following features. The cation includes a cationic heterocycle.

This aspect, taken alone or combinable with any other aspect, can include the following features. The cationic heterocycle is at least one of pyridinium, pyrrolidinium, pyrazolium, or imidazolium.

This aspect, taken alone or combinable with any other aspect, can include the following features. The cation is partially or fully fluorinated.

This aspect, taken alone or combinable with any other aspect, can include the following features. The external phase of the emulsion includes aqueous fluid and the internal phase of the emulsion includes carbon dioxide.

This aspect, taken alone or combinable with any other aspect, can include the following features. The emulsion includes hydrophobic particles to stabilize the emulsion.

This aspect, taken alone or combinable with any other aspect, can include the following features. The external phase of the emulsion includes carbon dioxide and the internal phase of the emulsion includes aqueous fluid.

This aspect, taken alone or combinable with any other aspect, can include the following features. The aqueous fluid includes an inorganic oxidizer.

This aspect, taken alone or combinable with any other aspect, can include the following features. The inorganic oxidizer includes at least one of bromate, chlorate, chlorite, persulfate, perborate, percarbonate, hypochlorite, nitrite, nitrate, perchlorate, or peroxide.

This aspect, taken alone or combinable with any other aspect, can include the following features. The emulsion includes an organic oxidizer.

This aspect, taken alone or combinable with any other aspect, can include the following features. The emulsion is stabilized by surfactants or particles.

This aspect, taken alone or combinable with any other aspect, can include the following features. The method further includes flowing the composition into the subterranean zone with a fracturing fluid.

This aspect, taken alone or combinable with any other aspect, can include the following features. The fracturing fluid includes at least one of a polymer, a crosslinker, a breaker, a surfactant, a scale inhibitor, a corrosion inhibitor, or a flowback aid.

This aspect, taken alone or combinable with any other aspect, can include the following features. The method further includes flowing the composition and the fracturing fluid with proppants.

This aspect, taken alone or combinable with any other aspect, can include the following features. The subterranean zone includes carbonate rock or sandstone rock that includes organic matter.

In some implementations, a composition for treating kerogen in a subterranean zone includes carbon dioxide and a fluid including an oxidizer. The fluid is an aqueous fluid. The composition includes an emulsion of carbon dioxide and the aqueous fluid.

This aspect, taken alone or combinable with any other aspect, can include the following features. The oxidizer includes a cation and an anion.

This aspect, taken alone or combinable with any other aspect, can include the following features. The anion includes at least one of chlorate or bromate.

This aspect, taken alone or combinable with any other aspect, can include the following features. The cation includes at least one of an ammonium ion, a butylammonium ion, a dibutylammonium ion, a tributyl ammonium ion, or a tetrabutylammonium ion.

This aspect, taken alone or combinable with any other aspect, can include the following features. The cation includes at least one of an ammonium ion substituted with alkyl, phenyl, or other groups, for example, bis(triphenylphosphine)iminium or tetraphenylphosphinium.

This aspect, taken alone or combinable with any other aspect, can include the following features. The cation includes at least one of pyridinium, pyrrolidinium, pyrazolium or imidazolium.

This aspect, taken alone or combinable with any other aspect, can include the following features. The cation is partially or fully fluorinated.

This aspect, taken alone or combinable with any other aspect, can include the following features. The external phase of the emulsion includes an aqueous fluid and an internal phase of the emulsion includes carbon dioxide.

This aspect, taken alone or combinable with any other aspect, can include the following features. The emulsion includes hydrophilic particles to stabilize the emulsion.

This aspect, taken alone or combinable with any other aspect, can include the following features. The aqueous fluid includes an inorganic oxidizer.

This aspect, taken alone or combinable with any other aspect, can include the following features. The inorganic oxidizer includes at least one of bromate, chlorate, chlorite, persulfate, perborate, percarbonate, hypochlorite, nitrite, nitrate, perchlorate, or peroxide.

This aspect, taken alone or combinable with any other aspect, can include the following features. The emulsion includes an organic oxidizer.

This aspect, taken alone or combinable with any other aspect, can include the following features. The emulsion includes surfactants.

In some implementations, a method of making a hydraulic fracturing fluid includes adding a quantity of a composition to a hydraulic fracturing fluid. The composition includes carbon dioxide and a fluid including an oxidizer. The fluid is an aqueous fluid. The composition includes an emulsion of carbon dioxide and aqueous fluid. The method further includes mixing the hydraulic fracturing fluid and the composition.

In some implementations, a method of making a kerogen breaking composition includes reacting two or more salts to form a composition with an organic cation and an oxidizing anion, and adding the composition to carbon dioxide.

As used in this disclosure, “treatment of a subterranean zone” can include any activity directed to extraction of water or petroleum materials from a subterranean petroleum- or water-producing formation or region, for example, including drilling, stimulation, hydraulic fracturing, clean-up, acidizing, completion, cementing, remedial treatment, abandonment, aquifer remediation, and identifying oil rich regions via imaging techniques.

As used in this disclosure, a “flow pathway” downhole can include any suitable subterranean flow pathway through which two subterranean locations are in fluid connection. The flow pathway can be sufficient for petroleum or water to flow from one subterranean location to the wellbore or vice-versa. A flow pathway can include at least one of a hydraulic fracture, and a fluid connection across a screen, across gravel pack, across proppant, including across resin-bonded proppant or proppant deposited in a fracture, and across sand. A flow pathway can include a natural subterranean passageway through which fluids can flow. In some implementations, a flow pathway can be a water source and can include water. In some implementations, a flow pathway can be a petroleum source and can include petroleum. In some implementations, a flow pathway can be sufficient to divert water, a downhole fluid, or a produced hydrocarbon from a wellbore, fracture, or flow pathway connected to the pathway.

As used in this disclosure, “weight percent” (wt %) can be considered a mass fraction or a mass ratio of a substance to the total mixture or composition. Weight percent can be a weight-to-weight ratio or mass-to-mass ratio, unless indicated otherwise.

As used in this disclosure, “volume percent” (vol %) can be considered a volume fraction or a volume ratio of a substance to the total mixture or composition.

A number of implementations of the disclosure have been described. Nevertheless, it will be understood that various modifications may be made without departing from the spirit and scope of the disclosure.

Claims

1. A method for treating kerogen or organic matter in a subterranean zone, the method comprising placing a composition in the subterranean zone, the composition comprising: supercritical carbon dioxide (CO2); anda fluid comprising an oxidizer, wherein the fluid is an aqueous fluid, and wherein the composition comprises an emulsion of supercritical carbon dioxide and the aqueous fluid, wherein the supercritical carbon dioxide and the fluid comprising the oxidizer are mixed to form the emulsion before placing the composition in the subterranean zone,wherein the oxidizer comprises a cation and an anion, and the cation comprises a fluorinated organic cation.

2. The method of claim 1, further comprising alternating placing the composition in the subterranean zone with placing a second fluid in the subterranean zone.

3. The method of claim 1, wherein the anion comprises at least one of chlorate or bromate.

4. The method of claim 1, wherein the cation comprises at least one of an ammonium ion, a butylammonium ion, a dibutylammonium ion, a tributyl ammonium ion, or a tetrabutylammonium ion.

5. The method of claim 1, wherein the cation comprises at least one of: an ammonium ion substituted with alkyl or phenyl groups; bis(triphenylphosphine)iminium; or tetraphenylphosphinium.

6. The method of claim 1, where the cation comprises a cationic heterocycle.

7. The method of claim 6, wherein the cationic heterocycle is at least one of pyridinium, pyrrolidinium, pyrazolium, or imidazolium.

8. The method of claim 1, wherein an external phase of the emulsion comprises the aqueous fluid and an internal phase of the emulsion comprises the supercritical CO2.

9. The method of claim 1, wherein the emulsion comprises hydrophobic particles to stabilize the emulsion.

10. The method of claim 1, wherein an external phase of the emulsion comprises the supercritical CO2 and an internal phase of the emulsion comprises the aqueous fluid.

11. The method of claim 1, wherein the aqueous fluid comprises an inorganic oxidizer.

12. The method of claim 11, wherein the inorganic oxidizer comprises at least one of bromate, chlorate, chlorite, persulfate, perborate, percarbonate, hypochlorite, nitrite, nitrate, perchlorate, or peroxide.

13. The method of claim 1, wherein the emulsion comprises an organic oxidizer.

14. The method of claim 1, wherein the emulsion is stabilized by surfactants or particles.

15. The method of claim 1, further comprising flowing the composition into the subterranean zone with a fracturing fluid.

16. The method of claim 15, wherein the fracturing fluid comprises at least one of a polymer, a crosslinker, a breaker, a surfactant, a scale inhibitor, a corrosion inhibitor, or a flowback aid.

17. The method of claim 15, further comprising flowing the composition and the fracturing fluid with proppants.

18. The method of claim 1, wherein the subterranean zone comprises carbonate rock or sandstone rock comprising organic matter.

19. The method of claim 1, wherein: the cation comprises a member selected from the group consisting of tetrabutylammonium bromate, tributylammonium bromate, dibutylammonium bromate, butylammonium bromate, tetrabutylammonium chlorate, bis(triphenylphosphine)iminium bromate, pyridinium bromate; andthe cation is made by a double displacement reaction.

20. A method for treating kerogen or organic matter in a subterranean zone, the method comprising placing a composition in the subterranean zone, the composition comprising: supercritical carbon dioxide (CO2); anda fluid comprising an oxidizer, wherein the fluid is an aqueous fluid, and wherein the composition comprises an emulsion of carbon dioxide and the aqueous fluid, wherein an external phase of the emulsion comprises the supercritical CO2 and an internal phase of the emulsion comprises the aqueous fluid, and wherein the supercritical carbon dioxide and the fluid comprising the oxidizer are mixed to form the emulsion before placing the composition in the subterranean zone, wherein:the oxidizer comprises a cation and an anion;the anion comprises at least one of chlorate or bromate;the cation comprises a member selected from the group consisting of tetrabutylammonium bromate, tributylammonium bromate, dibutylammonium bromate, butylammonium bromate, tetrabutylammonium chlorate, bis(triphenylphosphine)iminium bromate, pyridinium bromate; andthe cation is made by a double displacement reaction.

21. A method for treating kerogen or organic matter in a subterranean zone, the method comprising placing a composition in the subterranean zone, the composition comprising: supercritical carbon dioxide (CO2); anda fluid comprising an oxidizer, wherein the fluid is an aqueous fluid, and wherein the composition comprises an emulsion of supercritical carbon dioxide and the aqueous fluid, wherein the supercritical carbon dioxide and the fluid comprising the oxidizer are mixed to form the emulsion before placing the composition in the subterranean zone,wherein: the oxidizer comprises a cation and an anion;the cation comprises a member selected from the group consisting of tetrabutylammonium bromate, tributylammonium bromate, dibutylammonium bromate, butylammonium bromate, tetrabutylammonium chlorate, bis(triphenylphosphine)iminium bromate, pyridinium bromate; andthe cation is made by a double displacement reaction.