Subterranean banded iron based injection fluid for hydrogen storage
12428232 ยท 2025-09-30
Assignee
Inventors
Cpc classification
C01B3/0084
CHEMISTRY; METALLURGY
International classification
B65G5/00
PERFORMING OPERATIONS; TRANSPORTING
Abstract
A method of hydrogen storage is described. The method includes injecting hydrogen into a subterranean banded iron formation, including magnetite, hematite, and/or pyrite, where the hydrogen is mainly hydrogen (H.sub.2) gas based on the total volume of the hydrogen. Further, the subterranean banded iron formation includes mainly magnetite, hematite, and/or pyrite based on a total weight of the subterranean banded iron formation, where the hydrogen is adsorbed on the magnetite, the hematite, and/or the pyrite. Further, the method includes injecting ethylenediaminetetraacetic acid into the subterranean banded iron formation to release the hydrogen from the magnetite, the hematite, and/or the pyrite.
Claims
1. A method of hydrogen storage, comprising: injecting hydrogen into a subterranean banded iron formation comprising magnetite, hematite, and/or pyrite, wherein the hydrogen is mainly hydrogen (H.sub.2) gas based on a total volume of the hydrogen, wherein the subterranean banded iron formation is mainly magnetite, hematite, and/or pyrite based on a total weight of the subterranean banded iron formation, wherein the hydrogen is adsorbed on the magnetite, the hematite, and/or the pyrite, injecting ethylenediaminetetraacetic acid into the subterranean banded iron formation to release the hydrogen from the magnetite, the hematite, and/or the pyrite.
2. The method of claim 1, further comprising: injecting a brine solution into the subterranean banded iron formation before injecting the hydrogen.
3. The method of claim 2, wherein the subterranean banded iron formation is at least 80% by weight magnetite and has a hydrogen index of 640 to 670 mg H.sub.2/g.
4. The method of claim 2, wherein the subterranean banded iron formation is at least 80% by weight hematite and has a hydrogen index of 670 to 690 mg H.sub.2/g.
5. The method of claim 2, wherein the subterranean banded iron formation is at least 80% by weight pyrite and has a hydrogen index of 520 to 540 mg H.sub.2/g.
6. The method of claim 2, wherein the brine solution comprises sodium chloride, sodium bicarbonate, sodium sulfate, magnesium chloride, and calcium chloride.
7. The method of claim 2, wherein the brine solution has a total dissolved solids concentration of 57,000 to 58,000 ppm.
8. The method of claim 1, further comprising: injecting an ethylenediaminetetraacetic acid solution into the subterranean banded iron formation before injecting the hydrogen.
9. The method of claim 8, wherein the subterranean banded iron formation is at least 80% by weight hematite and has a hydrogen index of 740 to 770 mg H.sub.2/g.
10. The method of claim 1, wherein the subterranean banded iron formation is at least 80% by weight hematite and has a hydrogen index of 520 to 530 mg H.sub.2/g.
11. The method of claim 1, wherein the subterranean banded iron formation is at least 80% by weight magnetite and has a hydrogen index of 540 to 550 mg H.sub.2/g.
12. The method of claim 1, wherein the subterranean banded iron formation comprises at least 80% by weight magnetite and has an average grain size of 50 to 55 m.
13. The method of claim 1, wherein the subterranean banded iron formation comprises at least 80% by weight hematite and has an average grain size of 25 to 30 m.
14. The method of claim 1, wherein the subterranean banded iron formation comprises at least 80% by weight pyrite and has an average grain size of 5 to 10 m.
15. The method of claim 1, wherein a pressure of the hydrogen in the subterranean banded iron formation is 500 to 1500 psi.
16. The method of claim 1, wherein the subterranean banded iron formation is at a temperature of 50 to 100 C. during the injecting.
17. The method of claim 1, wherein the subterranean banded iron formation magnetite comprises 66 to 72 percent by weight (wt. %) iron(II, III) oxide, 25 to 30 wt. % silicon dioxide (SiO.sub.2), and 1 to 4 wt. % vermiculite ((Mg, Fe.sup.2+, Fe.sup.3+).sub.3[(Al, Si).sub.4O.sub.10](OH).sub.2.Math.4H.sub.2O) based on a total weight of the magnetite.
18. The method of claim 1, wherein the subterranean banded iron formation hematite comprises at least 99 wt. % iron(III) oxide based on a total weight of the hematite.
19. The method of claim 1, wherein the subterranean banded iron formation pyrite comprises 80 to 85 wt. % iron sulfide (FeS.sub.2) and 15 to 20 wt. % SiO.sub.2 based on a total weight of the pyrite.
20. The method of claim 1, wherein the subterranean banded iron formation comprises at least 80% by weight hematite and a binding energy of the hydrogen to the hematite is 13 to 11 kcal/mol.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1) A more complete appreciation of this disclosure and many of the attendant advantages thereof may be readily obtained as the same becomes better understood by reference to the following detailed description when considered in connection with the accompanying drawings, wherein:
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DETAILED DESCRIPTION
(35) In the drawings, like reference numerals designate identical or corresponding parts throughout the several views. Further, as used herein, the words a, an and the like generally carry a meaning of one or more, unless stated otherwise.
(36) Furthermore, the terms approximately, approximate, about and similar terms generally refer to ranges that include the identified value within a margin of 20%, 10%, or preferably 5%, and any values therebetween.
(37) As used herein, the term subterranean refers to to something that is located beneath the surface of the earth. Specifically, it describes the banded iron formation that is found underground, as opposed to being exposed on the surface. So, the hydrogen is being injected into rock formations located below ground that contain magnetite, hematite, and/or pyrite.
(38) As used herein, the term average grain size refers to the typical size of the individual mineral crystals (or grains) within a rock or material. In the context of the disclosure, it represents the mean diameter of the magnetite grains within the subterranean banded iron formation. The average grain size is usually determined by measuring a representative sample of grains and calculating their average size, often in micrometers (m).
(39) As used herein, the term subterranean banded iron formation (BIF) refers a type of sedimentary rock that forms in ancient marine environments. It is characterized by alternating layers of iron-rich minerals, such as magnetite (Fe.sub.3O.sub.4), hematite (Fe.sub.2O.sub.3), and sometimes pyrite (FeS.sub.2), along with silica (SiO.sub.2) or other minerals. Such formations are often composed of thin, alternating bands of iron oxide minerals and chert or silica-rich material. Banded iron formations are significant in geological studies because they provide important evidence about the early atmosphere of Earth and the development of oxygen-rich conditions, which contributed to the evolution of life.
(40) As used herein, the term total dissolved solids concentration refers to the total amount of dissolved substances, such as salts, minerals, and organic matter, present in a liquid, typically measured in milligrams per liter (mg/L) or parts per million (ppm).
(41) As used herein, the term brine solution refers to a high-concentration mixture of water and dissolved salts, primarily sodium chloride (NaCl), but it may contain other minerals. It is often used in industrial processes, food preservation, or as a byproduct of certain operations like oil and gas extraction.
(42) As used herein, the term binding energy of the hydrogen refers to the amount of energy required to break the bond between hydrogen atoms in a molecule, such as in H.sub.2, or to separate a hydrogen atom from an atom or molecule. It is a measure of the stability of the hydrogen bond or molecule.
(43) Aspects of this disclosure pertain to a method of hydrogen storage by being adsorbed within a subterranean banded iron formation, including magnetite, hematite, and/or pyrite, and its subsequent retrieval by injecting another injection fluid. Presently there is no mechanism in place that ensures that hydrogen stored underground may be retrieved. The present disclosure circumvents the drawbacks of prior art by addressing key limitations such as high operational and maintenance costs, short-term stability, and hydrogen loss through leakage, of the materials known in the art. The present invention seeks to solve the challenge of underground hydrogen storage, specifically focusing on how it can be safely retrieved while ensuring the security of the hydrogen gas in storage.
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(45) At step 52, the method 50 includes injecting a brine solution into a subterranean banded iron formation. A subterranean banded iron formation is a deep underground layer of rock characterized by alternating bands of iron-rich minerals (such as magnetite, hematite, and pyrite) and silica-rich material (like chert or quartz). In some embodiments, the subterranean banded iron formations include goethite, siderite, limonite, ferrihydrite, maghemite, and chlorite. In a preferred embodiment, the subterranean banded iron formation mainly includes magnetite, hematite, and/or pyrite
(46) In some embodiments, the subterranean banded iron formation magnetite includes 36 to 42 percent by weight (wt. %) iron (II, III) oxide, 10 to 15 wt. % silicon dioxide (SiO.sub.2), and 0.01 to 0.05 wt. % vermiculite ((Mg, Fe.sup.2+, Fe.sup.3+).sub.3[(Al, Si).sub.4O.sub.10](OH).sub.2.Math.4H.sub.2O) based on a total weight of the magnetite. In some other embodiments, the subterranean banded iron formation magnetite includes 46 to 52 percent by weight (wt. %) iron (II, III) oxide, 11 to 16 wt. % silicon dioxide (SiO.sub.2), and 0.05 to 1 wt. % vermiculite ((Mg, Fe.sup.2+, Fe.sup.3+).sub.3[(Al, Si).sub.4O.sub.10](OH).sub.2.Math.4H.sub.2O) based on a total weight of the magnetite. Yet, in another embodiment, the subterranean banded iron formation magnetite includes 56 to 62 percent by weight (wt. %) iron(II, III) oxide, 18 to 25 wt. % silicon dioxide (SiO.sub.2), and 1 to 3 wt. % vermiculite ((Mg, Fe.sup.2+, Fe.sup.3+).sub.3[(Al, Si).sub.4O.sub.10](OH).sub.2.Math.4H.sub.2O) based on the total weight of the magnetite. In a preferred embodiment, the subterranean banded iron formation magnetite includes 66 to 72 percent by weight (wt. %) iron (II, III) oxide, 25 to 30 wt. % silicon dioxide (SiO.sub.2), and 1 to 4 wt. % vermiculite ((Mg, Fe.sup.2+, Fe.sup.3+).sub.3[(Al, Si).sub.4O.sub.10](OH).sub.2.Math.4H.sub.2O) based on a total weight of the magnetite.
(47) In some embodiments, the subterranean banded iron formation hematite includes at least 75 wt. % iron (III) oxide based on a total weight of the hematite, preferably 85 wt. % iron (III) oxide based on a total weight of the hematite, and more preferably 99 wt. % iron (III) oxide based on a total weight of the hematite. In a preferred embodiment, the subterranean banded iron formation hematite includes at least 99 wt. % iron (III) oxide based on a total weight of the hematite.
(48) In some embodiments, the subterranean banded iron formation pyrite includes 50 to 55 wt. % iron sulfide (FeS.sub.2) and 5 to 8 wt. % SiO.sub.2 based on a total weight of the pyrite, preferably 55 to 60 wt. % iron sulfide (FeS.sub.2) and 8 to 11 wt. % SiO.sub.2 based on a total weight of the pyrite, and more preferably 70 to 75 wt. % iron sulfide (FeS.sub.2) and 14 to 18 wt. % SiO.sub.2 based on a total weight of the pyrite. In a preferred embodiment, the subterranean banded iron formation pyrite includes 80 to 85 wt. % iron sulfide (FeS.sub.2) and 15 to 20 wt. % SiO.sub.2 based on a total weight of the pyrite.
(49) In some embodiments, in addition to iron sulfide (FeS.sub.2) and silica (SiO.sub.2), other components that may be present in pyrite within a subterranean banded iron formation may include trace amounts of other sulfur compounds, minor amounts of metals like copper, zinc, or nickel, and other minerals such as clay or carbonates. However, these are typically present in much smaller quantities.
(50) In some embodiments, the subterranean banded iron formation includes at least 60% by weight magnetite and has an average grain size of 30 to 35 m, preferably at least 65% by weight magnetite and has an average grain size of 35 to 40 m, preferably at least 70% by weight magnetite and has an average grain size of 40 to 45 m, and more preferably at least 75% by weight magnetite and has an average grain size of 45 to 50 m. In a preferred embodiment, the subterranean banded iron formation includes at least 80% by weight magnetite and has an average grain size of 50 to 55 m.
(51) In some embodiments, the subterranean banded iron formation includes at least 60% by weight hematite and has an average grain size of 10 to 15 m, preferably at least 65% by weight hematite and has an average grain size of 15 to 20 m, preferably at least 70% by weight hematite and has an average grain size of 20 to 25 m, and more preferably at least 75% by weight hematite and has an average grain size of 21 to 24 m. In a preferred embodiment, the subterranean banded iron formation includes at least 80% by weight hematite and has an average grain size of 25 to 30 m.
(52) In some embodiments, the subterranean banded iron formation includes at least 60% by weight pyrite and has an average grain size of 0.01 to 0.05 m, preferably at least 65% by weight pyrite and has an average grain size of 0.05 to 1 m, preferably at least 70% by weight pyrite and has an average grain size of 1 to 4 m, and more preferably at least 75% by weight pyrite and has an average grain size of 4 to 8 m. In a preferred embodiment, the subterranean banded iron formation includes at least 80% by weight pyrite and has an average grain size of 5 to 10 m.
(53) Injecting a brine solution first helps to stabilize the subterranean banded iron formation, maintain pressure, and reduce the risk of clogging or mineral precipitation during subsequent hydrogen injection. The brine solution may help facilitate the dissolution of minerals, improve fluid flow within the formation, and prepare the environment for more effective hydrogen injection by creating a more favorable chemical and physical condition for the process.
(54) In some embodiments, the brine solution includes sodium chloride (NaCl), calcium chloride (CaCl.sub.2)), or magnesium chloride (MgCl.sub.2), along with other dissolved minerals to enhance the ionic strength. It may include trace amounts of other salts like potassium chloride (KCl) or sodium bicarbonate (NaHCO.sub.3), depending on the specific requirements of the formation and the process. In a specific embodiment, the brine solution includes NaCl, NaHCO.sub.3, Na.sub.2SO.sub.4, MgCl.sub.2, and CaCl.sub.2. In some embodiments, the brine solution includes, by mass, ions of, Na.sup.+: 5,000-50,000 parts per million (ppm), more preferably 15,000-20,000 ppm, and yet more preferably 18,300; Ca.sup.2+: 100-1,500 ppm, more preferably 600-700 ppm, and yet more preferably 650 ppm; Mg.sup.2+: 500-5,000 ppm, more preferably 2,000-3,000 ppm, and yet more preferably 2,110 ppm; SO.sub.4.sup.2: 1,000-9,000 ppm, more preferably 4,000-5,000 ppm, and yet more preferably 4,290 ppm; Cl.sup.: 10,000-70,000 ppm, more preferably 32,000-33,000 ppm, and yet more preferably 32,200 ppm; and HCO.sub.3.sup.: 10-500 ppm, more preferably 100-150 ppm, and yet more preferably 120 ppm. The composition of the brine solution is designed to stabilize the formation, facilitate fluid flow, and potentially help in dissolving minerals before the injection of hydrogen.
(55) In some embodiments, the brine solution has a total dissolved solids concentration of 35000 to 40,000 ppm, preferably 45000 to 50,000 ppm, and more preferably 48000 to 55,000 ppm. In a preferred embodiment, the brine solution has a total dissolved solids concentration of 57,000 to 58,000 ppm. The specified total dissolved solids (TDS) concentration of 57,000 to 58,000 ppm in the brine solution is required to ensure that the solution has the appropriate salinity level, which is critical for the desired chemical reactions or processes in the method, such as optimizing the extraction or reduction processes in the subterranean formation.
(56) At step 54, the method 50 includes injecting an ethylenediaminetetraacetic acid (EDTA) solution into the subterranean banded iron formation. Injecting an EDTA solution first helps to chelate and dissolve iron minerals like magnetite, hematite, and pyrite in the subterranean banded iron formation. The process breaks down the iron compounds and releases hydrogen in a controlled manner, making it easier for the subsequent hydrogen injection to be more effective.
(57) At step 56, the method 50 includes injecting hydrogen into a subterranean banded iron formation, wherein the hydrogen is adsorbed on the magnetite, the hematite, and/or the pyrite. In the present disclosure, at least 30%, preferably 40%, preferably 50%, preferably 60%, preferably 65%, preferably 75%, preferably 80%, preferably 85%, preferably 90%, preferably 95%, preferably 96%, preferably 97%, preferably 98%, preferably 99%, preferably 99.5%, preferably 100% of the hydrogen is injected mainly as hydrogen (H.sub.2) gas based on the total volume of the hydrogen. The hydrogen is adsorbed on the magnetite, the hematite, and/or the pyrite.
(58) In some embodiments, a pressure of the hydrogen in the subterranean banded iron formation is 100 to 200 psi, preferably 200 to 300 psi, preferably 400 to 600 psi, preferably 450 to 650 psi, and more preferably 500 to 1200 psi. In a preferred embodiment, pressure of the hydrogen in the subterranean banded iron formation is 500 to 1500 psi. The pressure of 500 to 1500 psi in the subterranean banded iron formation ensures optimal conditions for the reaction between hydrogen and the iron-bearing minerals, facilitating efficient reduction processes such as converting hematite or magnetite to magnetite or iron.
(59) In some embodiments, the subterranean banded iron formation is at a temperature of 30 to 60 C. during the injecting process (in all the embodiments as described earlier), preferably 15 to 65 C., preferably 25 to 75 C., preferably 35 to 85 C., and more preferably 45 to 95 C. In a preferred embodiment, the subterranean banded iron formation is at a temperature of 50 to 100 C. during the injecting process. The temperature range is crucial because it enhances the reaction rate between hydrogen and the minerals in the subterranean banded iron formation, such as magnetite, hematite, and pyrite. This temperature range helps optimize the reduction processes, making them more efficient and effective without causing unwanted side reactions or instability in the formation.
(60) The hydrogen index (HI) is the ratio of hydrogen content of a sample to its organic carbon content. The HI value suggests the hydrogen release capacity for a formation, making it an effective source for hydrogen production when treated appropriately. This value is useful for evaluating the efficiency of the process and optimizing the conditions for maximum hydrogen extraction. HI function may indicate how much hydrogen is present per gram of material, with higher values generally signifying a higher hydrogen content and potentially greater reactivity or energy content.
(61) In some embodiments, the subterranean banded iron formation with at least 50% by weight hematite and has a hydrogen index of 450 to 480 mg H.sub.2/g, preferably at least 60% by weight hematite and has a hydrogen index of 460 to 490 mg H.sub.2/g, preferably at least 65% by weight hematite and has a hydrogen index of 465 to 495 mg H.sub.2/g, and more preferably at least 70% by weight hematite and has a hydrogen index of 500 to 510 mg H.sub.2/g. In a preferred embodiment, the subterranean banded iron formation is at least 80% by weight hematite and has a hydrogen index of 520 to 530 mg H.sub.2/g. In another preferred embodiment, the subterranean banded iron formation is at least 80% by weight hematite and has a hydrogen index of 740 to 770 mg H.sub.2/g. In yet another preferred embodiment, the subterranean banded iron formation is at least 80% by weight hematite and has a hydrogen index of 670 to 690 mg H.sub.2/g.
(62) In some embodiments, the subterranean banded iron formation is at least 50% by weight magnetite and has a hydrogen index of 450 to 480 mg H.sub.2/g, preferably at least 60% by weight magnetite and has a hydrogen index of 480 to 490 mg H.sub.2/g, preferably at least 65% by weight magnetite and has a hydrogen index of 500 to 530 mg H.sub.2/g, and more preferably at least 70% by weight magnetite and has a hydrogen index of 530 to 540 mg H.sub.2/g. In a preferred embodiment, the subterranean banded iron formation is at least 80% by weight magnetite and has a hydrogen index of 540 to 550 mg H.sub.2/g. In another preferred embodiment, the subterranean banded iron formation is at least 80% by weight magnetite and has a hydrogen index of 640 to 670 mg H.sub.2/g.
(63) In some embodiments, the subterranean banded iron formation is at least 50% by weight pyrite and has a hydrogen index of 340 to 380 mg H.sub.2/g, preferably at least 60% by weight pyrite and has a hydrogen index of 360 to 390 mg H.sub.2/g, preferably at least 65% by weight pyrite and has a hydrogen index of 465 to 495 mg H.sub.2/g, and more preferably at least 70% by weight pyrite and has a hydrogen index of 500 to 510 mg H.sub.2/g. In a preferred embodiment, the subterranean banded iron formation is at least 80% by weight pyrite and has a hydrogen index of 520 to 540 mg H.sub.2/g. In another preferred embodiment, the subterranean banded iron formation is at least 80% by weight pyrite and has a hydrogen index of 355 to 370 mg H.sub.2/g.
(64) In some embodiments, the subterranean banded iron formation includes at least 50% by weight hematite and a binding energy of the hydrogen to the hematite is 8 to 5 kcal/mol, preferably at least 55% by weight hematite and a binding energy of the hydrogen to the hematite is 9 to 6 kcal/mol, preferably at least 65% by weight hematite and a binding energy of the hydrogen to the hematite is 10 to 7 kcal/mol, and more preferably at least 75% by weight hematite and a binding energy of the hydrogen to the hematite is 12 to 10 kcal/mol. In a preferred embodiment, the subterranean banded iron formation includes at least 80% by weight hematite and a binding energy of the hydrogen to the hematite is 13 to 11 kcal/mol. The negative binding energy indicates that hydrogen binds relatively strongly to the hematite, which is important for facilitating reactions like reduction or hydrogenation.
EXAMPLES
(65) The following examples demonstrate an injection fluid for hydrogen storage in subterranean formation. The examples are provided solely for illustration and are not to be construed as limitations of the present disclosure, as many variations thereof are possible without departing from the spirit and scope of the present disclosure.
Example 1: Materials
(66) The pyrite, magnetite and hematite samples used in the disclosure were purchased from Ward's Science, Rochester, NY. The makeup of the sample was determined using an X-ray diffraction (XRD) system by Malvern Panalytical, with the composition shown in Table 1. Salts used in the disclosure to prepare the brine solution (Table 2) are of American Chemical Society (ACS) reagent grade and included salts such as sodium chloride (NaCl), sodium bicarbonate (NaHCO.sub.3), sodium sulfate (Na.sub.2SO.sub.4), magnesium chloride (MgCl.sub.2), and calcium chloride (CaCl.sub.2).
(67) TABLE-US-00001 TABLE 1 Sample composition from XRD analysis. Sample Composition (%) Mineral Chemical Formula Wt. % Wt. % Wt. % Pyrite FeS.sub.2 82.3 Magnetite Fe.sub.3O.sub.4 69 Hematite Fe.sub.2O.sub.3 100 Vermiculite (Mg,Fe.sup.2+,Fe.sup.3+).sub.3[Al,Si).sub.4O.sub.10] (OH).sub.24H.sub.2O 2.8 Quartz SiO.sub.2 17.7 28.3
(68) TABLE-US-00002 TABLE 2 Seawater composition. Ion Concentration (ppm) Na.sup.+ 18,300 Ca.sup.2+ 650 Mg.sup.2+ 2,110 SO.sub.4.sup.2 4,290 Cl.sup. 32,200 HCO.sub.3.sup. 120 TDS 57,670
Example 2: Methodology
(69) The samples used in the disclosure were ground into powder using a mortar and pestle to minimize the destruction of the crystals of the minerals. After the grinding process, the particle size distribution of the particles was determined. The samples have average particle size values of 7.03 micrometers (m), 52.55 m, and 27.72 m, for pyrite, magnetite, and hematite, respectively. The hydrogen index (HI) of the original (crushed, unexposed to hydrogen) sample was determined before exposure to hydrogen gas to serve as the basis for comparison using Rock-Eval analysis (procedure explained in the following section). To expose the samples to hydrogen gas, the samples were placed in a Teflon cup (5 g sample) and placed inside the ageing cell. The cover of the ageing cells was then placed and fastened firmly. The cell is then vacuumed for 3 minutes to remove trapped air inside the ageing cell. Subsequently, hydrogen gas is introduced into the cell at a set pressure. The pressure inside the cell is monitored via a pressure gauge installed upstream of the cell. Once the pressure (1000 psi) is reached, the valve on the cell is locked. The assembly is then dismantled, and the cell is placed in an oven at a preset temperature of 80 C.
(70) After 24 hours, the ageing cell is removed from the oven, and the pressure left inside the ageing cell is determined before opening the cell to release unabsorbed hydrogen gas. The solid samples are thereafter retrieved, and their hydrogen index is determined as in the case of the original samples. For each mineral in this disclosure, two cases were investigated. The case of hydrogen adsorption on dry samples is referred to as a dry case hereon, and the case of samples immersed in seawater (50 ml seawater with the composition shown in (Table 2) is referred to as a wet case. The disclosure unlike others as rightly pointed out recently [See: Zeng L, Sarmadivaleh M, Saeedi A, Chen Y, Zhong Z, Xie Q. Storage integrity during underground hydrogen storage in depleted gas reservoirs], has considered real iron-bearing minerals (presence of other minerals in sample make-up) other than pure minerals which have been used in the literature. Moreover, the impact of brine on the hydrogen interaction with the iron-bearing mineral was again studied in the present disclosure. The HI of both the dry and wet cases are determined and assessed in comparison to the original samples.
(71) The effect of the adsorption capacity of the sample for hydrogen gas due to treatment with a chelating agent (ethylenediaminetetraacetic acid (EDTA)) is another evaluation which is reported in the disclosure. The experiment is repeated in cases of both dry and wet, with the corresponding HI determined for EDTA-treated samples. The HI is then used to assess the viability of hydrogen storage in the iron minerals.
(72) Rock-Eval Analysis (Method of Hydrogen Adsorption Quantification)
(73) The Rock-Eval 7 analyzer was utilized in the disclosure for the evaluation of the total organic carbon and total sulfur content of rocks, as well as the calculation of indexes like the hydrogen and oxygen indexes. However, the focus of the disclosure is on the evaluation of the hydrogen index, which is used to infer the amount of adsorbed hydrogen on the treated samples. The device has an alumina crucible, an oxidation temperature range of 200 C.-850 C., and pyrolysis temperatures of 40 C.-850 C., respectively. It includes flame ionization detectors (FID) and infrared detectors (IR), which are used to detect CO.sub.2 and hydrocarbons, respectively. The Rock-Eval 7 is composed of two significant furnaces, one for oxidation and the other for pyrolysis. In a combustion oven connected to the pyrolysis furnace, a portion of the effluents undergo pyrolysis, where the sulfur compounds are converted to sulfur dioxide (SO.sub.2). The FID and IR spectrometers are used to identify hydrocarbons and carbon monoxide/carbon dioxide (CO/CO.sub.2), respectively, whereas the ultra-violet (UV) spectrometer is used to detect SO.sub.2. After pyrolysis, the pyrolysis byproduct is oxidized in the oxidation furnace. The SO.sub.2, CO, and CO.sub.2 emissions are detected by UV and IR spectrometers, respectively. The adoption of a twin furnace design (pyrolysis and oxidation) is necessary to produce a long-lasting carbonaceous layer at the inner surface of the pyrolysis furnace. The coating prevents further adsorption and subsequent hydrocarbon loss that may affect hydrocarbon readings. The S1 and S2 peaks of the FID indicate that it is oxidized in single furnace machines. The superposition of the SO.sub.2 and hydrocarbon signals allows us to distinguish between the organic sulfur, which is associated with the S1 and S2 peaks of the FID, and the pyritic sulfur. In the disclosure, the quantities of pyritic sulfur and organic sulfur are estimated using a mathematical model based on parameters produced from the Rock-Eval 7 analysis as published by Aboussou [See: Aboussou A. New Rock-Eval method for Pyritic and Organic Sulphur quantification: Application to study organic matter preservation in Jurassic sediments]. Additionally, the kerogen technique of analysis was applied with a sample weight of 9 milligrams (mg) 14 mg, determined with a precision of 0.02 mg.
Example 3: Scanning Electron Microscope (SEM) Imaging
(74) The change in the surface morphology of the samples due to exposure to hydrogen gas was investigated using a Gemini 550 scanning electron microscope (SEM). The SEM was fitted with an Aztec energy-dispersive X-ray spectrometer (EDX) and a backscattered electron (BSE) detector. To prepare the SEM samples, rectangular sample chips were cut and polished using smooth grit paper to get them ready for SEM imaging. The samples were subjected to hydrogen gas exposure in both wet (in the presence of brine) and dry (without brine) conditions, as well as with and without prior EDTA treatment. After the hydrogen gas exposure, the wet samples were dried at 40 C. for 24 hours before being used for imaging. Crucially, the SEM samples were kept under identical circumstances to the previously mentioned powdered samples, i.e., they were aged at the same temperature of 80 C. to mimic the same conditions. Following the ageing time, the samples were allowed to dry, mounted on stubs, and coated with 30 nm palladium-gold using a Quorum QR150R sputter coater before being subjected to SEM examination. The voltage and current used for the SEM analysis ranged from 2 kilovolt (kV) to 15 kV and 100 picoampere (pA) to 2000 pA, respectively.
Example 4: Density Functional Theory (DFT) Calculations
(75) To provide insight into the hydrogen-iron mineral interactions that result in improved interaction or adsorption, density functional theory (DFT) calculations were performed. As implemented in Gaussian 16 [See: Frisch M J, Trucks G W, Schlegel H B, Scuseria G E, Robb M a., Cheeseman J R and other co-workers], all DFT computations were carried out at a B3LYP/6-311g(d, p) level of theory. Using the self-consistent reaction field of the polarizable continuum model (PCM-SCRF) [See: Tomasi J, Mennucci B, Cammi R. Quantum mechanical continuum solvation models], the calculations were performed implicitly in the solvent. To verify that the optimized structures are in a minimum energy state, frequency calculations are carried out. Using the same degree of theory as previously, the binding energies (counterpoise adjusted) from the intermolecular interaction of hydrogen and iron minerals are estimated, along with additional attributes such as the frontier molecular orbitals and electrostatic potential maps. Moreover, the Multiwfn program was used to analyze non-covalent interactions (NCI) and determine the type of interactions [See: Lu T, Chen F. Multiwfn: A multifunctional wavefunction analyzer]. Van der Waals interactions, steric clashes, and hydrogen bonds are a few interactions that may be observed and identified using NC. This may be achieved by plotting the reduced gradient s(r) vs (r) for low reduced gradient locations. More so the NCI analysis may be applied to affirm bond formation which is marked by a lack of peaks on the RDG maps.
Results and Discussion
(76) The purpose of the disclosure is to demonstrate how iron-mineral-rich formations are suited to store hydrogen gas. Specifically, to emphasize the process that may be used to store and extract hydrogen from such storage media. The hydrogen index determined by the Rock-Eval analysis is utilized to provide insights into the feasibility of hydrogen storage and extraction in iron minerals. The ratio of hydrogen content of the sample to its organic carbon content is called the hydrogen index. More precisely, it is the total hydrogen content in milligrams per gram of sample as determined by the S2 curve of Rock-Eval analysis.
(77) The impact of exposing iron minerals to hydrogen gas and treating them with a chelating agent to determine improvement in the amount of adsorbed hydrogen gas is discussed in the subsequent sections. The purpose of it is to determine whether the minerals may be employed on an industrial scale as primary hydrogen storage media. Another important aspect of hydrogen storage in formations rich in iron minerals is the retrieval of the stored gas.
(78) Magnetite mineral interaction with hydrogen in cases of dry and wet conditions, as well as with and without EDTA treatment, is depicted in
(79) On the other hand, in the wet experimental conditions where the magnetite particles are dispersed in brine before exposure to hydrogen, higher HI (higher than the native state) is observed. Compared to the native state and the dry conditions, the increase in the HI is by 20.6% and 306%, respectively. This means that some hydrogen, either from the brine or the hydrogen gas, had adsorbed on the magnetite surface. This is not surprising as the magnetite oxygen binding property has been reported to enable the formation of iron hydroxide aggregates [See: Evgenia-Maria P. Retention of toxic pollutants by nanomagnetite aggregates]. Thus, in a moist environment (presence of brine), it should be able to imbibe water to itself. Recently, the use of magnetite for the natural production of hydrogen gas has been re-evaluated [See: Geymond U, Briolet T, Combaudon V, Sissmann O, Martinez I, Duttine M, et al. Reassessing the role of magnetite during natural hydrogen generation]. With a focus on magnetite, the authors assessed the hydrogen production from the banded iron formations. The authors noted that hydrogen generation and the conversion of magnetite to maghemite (Eq.1) occurred at temperatures below 200 C. Consequently, the path indicated in Eq. 2 allowed for the production of hydrogen. Experimental results demonstrated the transition, with water being identified as the oxidizing agent. Thus, aside from the ability of magnetite to produce hydrogen by its interaction with water, it may adsorb hydrogen. However, the increase in the HI is not due to the production of hydrogen from Eq.2 because the temperature conditions in these experiments (80 C.) are lower than the reported temperature (180 C.-200 C.) at which the interactions should occur, as shown in
(80)
(81) Like magnetite, hematite is an iron oxide mineral with a composition like that of magnetite except for the oxidation state of the iron element. Like magnetite, the native state of hematite mineral has a high HI value, almost comparable to that of magnetite. This is not surprising as in many cases, these minerals share reaction routes. However, its behavior differs significantly from that of magnetite when exposed to hydrogen gas. Unlike the case of magnetite where a significant decrease in the HI was recorded in the dry instances, a less drastic reduction is observed in the case of the untreated sample with an HI of 489 compared to the native state with 525, as shown in
(82) Pyrite mineral interaction with hydrogen in both cases of wet and dry conditions, as well as with and without EDTA treatment, is discussed herein. The results of the HI evaluation are shown in
(83) Dry conditions are not the case in oil and gas reservoirs, which have been stated to be an option when it comes to storage site selection. More so, depleted reservoirs are good candidates since the infrastructure required to inject gases into the reservoirs is already in place. Additionally, present in the reservoirs are brines which were the first occupants of the pore spaces before the drainage process which replaces the water with either oil or gas. In reservoirs, where waterflooding has taken place, may have a significant amount of brine in place thus, the impact of the presence of brine on the adsorption of hydrogen on the pyrite mineral is investigated. The presence of brine is observed to increase the HI of the pyrite sample in both cases of untreated and treated samples. Thus, it is a significant advantage as most reservoirs have brine presence. In the case of the untreated sample, the recorded HI is 66 mg/g-sample compared to 17 and 20 in the cases of dry and native samples, respectively.
(84) The interaction of pyrite mineral in brine with H.sub.2 may result in the formation of sulfate and iron oxyhydroxide as shown in
(85) Although the discussion thus far has shown that the pyrite mineral may serve as a storage media for H.sub.2, its retrieval from the pyrite surface is the next subject of discussion. This is because, after storage for a certain period, the stored H.sub.2 may need to be produced back for usage. The observed HI of the pyrite system has shown pyrite to be a good H.sub.2 storage medium.
(86) This portion of the study assesses how H.sub.2 interacts with iron minerals affects the structural integrity (permeability and hardness) of the sample. This is important because excellent structural integrity is required for the iron-banded formation-which is regarded to have the potential for storing hydrogen gas in terms of a viable storage option. Furthermore, it is important that oil and gas reservoirs-particularly the depleted ones designated as possible storage locationsbe able to tolerate such kinds of interactions. The pyrite and magnetite samples are among those examined in this section. As in the previously stated adsorption investigations, such samples are aged and exposed to hydrogen gas at 1000 psi in both dry and wet conditions. The hardness and permeability of the iron minerals were evaluated following a 24-hour exposure to H.sub.2 to evaluate the structural integrity of the minerals. Furthermore, the degree of variation in the attributes (permeability and hardness) before and after treatment is examined by reporting the changes in percentages. It is critical to note that the untreated samples received the same temperature and duration of treatment as the samples that were exposed to H.sub.2. This may guarantee a fair comparison.
(87) The hardness of the pyrite sample and magnetite samples is shown in
(88) In the case of the magnetite sample, as shown in
(89) Just as the sample hardness was analyzed, sample permeability was measured. The results of permeability measurements of the treated samples compared to the untreated samples are shown in
(90) The DFT calculations provided in this disclosure utilized a simple molecular representation of each mineral to interact with a single molecule of hydrogen to establish the degree of interaction and the nature of the interaction. Table 3 and
(91) TABLE-US-00003 TABLE 3 Mineral-H.sub.2 interaction energies. Pairs Binding Energy (kcal/mol) Pyrite-H.sub.2 5.74 Magnetite-H.sub.2 20.98 Hematite-H.sub.2 11.69
(92) SEM image analysis presented herein is to examine the change in the surface properties of the samples exposed to hydrogen gas in both dry and wet conditions, as well as evaluate the effect of EDTA treatment on the sample surface. In this section, only the pyrite and magnetite samples were examined due to the availability of solid samples of the minerals. More so, although the iron oxide minerals may slightly differ in the manner they interact with hydrogen, their behavior should be similar. Thus, observations discussed in the following paragraphs in the case of magnetite may apply to hematite. The SEM image of the intact or unexposed magnetite in its natural form as received from the supplier is shown in
(93) In the cases of dry conditions where the magnetite samples are exposed to hydrogen in the absence of brine, the results of the SEM analysis are shown in
(94) In the wet condition, which is where the magnetite sample is immersed in brine and then exposed to hydrogen gas in the presence of brine, the SEM images are shown in
(95) The SEM image of the intact pyrite sample and its EDX is shown in
(96) The SEM images of pyrite in the wet conditions depicted in
(97) In this disclosure, DFT calculations and experimental analysis are used to support the assessment of the potential for hydrogen storage in formations rich in iron minerals by examining the interaction of iron minerals with hydrogen. This is the first attempt, despite the numerous studies that have been published in the literature, to quantitatively investigate the possibility of iron minerals acting as media for storing hydrogen and to develop a procedure that ensures both the storage of hydrogen and its retrieval for use. Thus, based on findings from both experimental data and DFT calculations, the conclusions that may be drawn are that iron mineral, magnetite being the most promising, may be utilized as hydrogen gas storage media. Further, the ability for hydrogen to be adsorbed onto iron mineral surfaces is significantly influenced by the state of the minerals, whether they are dry or in the presence of brine. Still further, the treatment with EDTA as a chelating agent may enhance hydrogen adsorption (in the case of pyrite). It may be utilized as a strategy for hydrogen recovery (in the case of magnetite). Thus, chemical methods are used to recover hydrogen following adsorption. Hydrogen may bind onto the iron mineral surfaces by forming covalent bonds and the order of binding affinity to the minerals is hematite>pyrite>magnetite. The binding affinity of hydrogen correlates with the HI reduction in the dry state. Several banded iron formations throughout the world may be used to store hydrogen gas, therefore this has enormous industrial potential. Consequently, the downside of widespread adoption of underground storage has been the provision of the necessary storage security which is demonstrated in this disclosure. Furthermore, the hardness and permeability of the sample are affected by its state, whether it is wet or dry. Further, there is a relationship between the hardness of the sample and the quantity of hydrogen adsorbed on it. Still further, treatment of pyrite with hydrogen results in significant permeability increase.
(98) Numerous modifications and variations of the present disclosure are possible in light of the above teachings. It is therefore to be understood that within the scope of the appended claims, the invention may be practiced otherwise than as specifically described herein.