Patent Application
20230017556
Naturally-sourced coal such as low-rank coal (e.g., subbituminous coal and lignite) can have undesirable properties such as low carbon concentration, high oxygen concentration, and high ash content. Such properties can make the coal less suitable for energy generation and production of high value materials such as graphene films.
Graphene is the name denoted to a single sheet (1 atom thick) of sp2-bonded carbon atoms. Effectively this is a single sheet of graphitic carbon. However, the term graphene has also come to be used to describe in a more general sense thin films (1-40 layers) of sp2-bonded carbon under the auspices of discussions of single layer interactions and electrical behavior. Due to the difficulty of mass-producing graphene films, it remains an extremely expensive material.
Graphite is a key material used in the fabrication of lithium-ion battery (LIB) anodes. The properties of graphite, such as high thermal and electrical conductivity, excellent mechanical properties, and lubricating properties, make graphite a good choice of material for a. variety of applications. With growing demand for clean energy technologies and a gradual transition away from fossil fuel energy, graphite is at the center of many energy storage applications such as LIB for electric vehicles (EVs), hybrid electric vehicles (HEVs), and plug-in electric vehicles (PEVs). Most of the current commercial graphite production relies mostly on natural graphite resources which are becoming increasingly scarce and are unable to meet the rapidly growing demand for graphite for the electric vehicle industries.
The present invention provides a method of carbonizing an upgraded coal. The method includes heating the upgraded coal in an inert environment, to form a carbonized upgraded coal.
The present invention provide a method of carbonizing an upgraded coal. The method includes heating the upgraded coal in an inert environment, to form a carbonized upgraded coal. The heating includes heating to a first temperature for a first duration, wherein the first temperature is in the range of 500° C. to 700° C., and wherein the first duration is in the range of 15 min to 1 h. The heating includes heating to a second temperature higher than the first temperature for a second duration, wherein the second temperature is in the range of 900° C. to 1100° C., and wherein the second duration is in the range of 15 min to 1 h. The heating also includes heating to a third temperature higher than the second temperature for a third duration, wherein the third temperature is in the range of 1,500° C. to 1,600° C., and wherein the third duration is in the range of 1 h to 3 h. The carbonized upgraded coal has an ash content of 1 wt % to 20 wt %. The carbonized upgraded coal has a fixed carbon (FC) content of 80 wt % to 99 wt %.
The present invention provides a carbonized upgraded coal formed by the method of carbonizing an upgraded coal described herein.
The present invention provides a carbonized upgraded coal that includes a fixed carbon (FC) content of 85 wt % to 98 wt %. The carbonized upgraded coal also includes an ash content of 2 wt % to 12 wt %.
The present invention provides a method of forming graphite. The method includes graphitizing carbonized upgraded coal, to form the graphite.
The present invention provides a method of forming graphite. The method includes carbonizing upgraded coal, the carbonizing including heating the upgraded coal in an inert environment, to form a carbonized upgraded coal. The method also includes graphitizing the carbonized upgraded coal, to form the graphite. The graphitizing includes heating the carbonized upgraded coal, the heating including heating to a first graphitization temperature for a first graphitization duration, wherein the first graphitization temperature is in the range of 1000° C. to 1500° C., and wherein the first graphitization duration is in the range of 0.1 s to 10 min. The heating also includes heating to a second graphitization temperature higher than the first graphitization temperature for a second graphitization duration, wherein the second graphitization duration is in the range of 0.1 s to 10 min. The heating also includes heating to a third graphitization temperature higher than the second graphitization temperature for a third graphitization duration, wherein the third graphitization temperature is in the range of 2700° C. to 3000° C., and wherein the third graphitization duration is in the range of 30 min to 3 h. The formed graphite has a fixed carbon content of 99 wt % to 100 wt %.
The present invention provides a method of forming graphite. The method includes heating upgraded coal in an inert environment, to form a carbonized upgraded coal, wherein the heating includes heating to a first temperature for a first duration, wherein the first temperature is in the range of 500° C. to 700° C., and wherein the first duration is in the range of 15 min to 1 h. The heating also includes heating to a second temperature higher than the first temperature for a second duration, wherein the second temperature is in the range of 900° C. to 1100° C., and wherein the second duration is in the range of 15 min to 1 h. The heating also includes heating to a third temperature higher than the second temperature for a third duration, wherein the third temperature is in the range of 1,500° C. to 1,600° C., and wherein the third duration is in the range of 1 h to 3 h. The carbonized upgraded coal has an ash content of 1 wt % to 20 wt %. The carbonized upgraded coal has a fixed carbon (FC) content of 80 wt % to 99 wt %. The method also includes graphitizing the carbonized upgraded coal, to form the graphite. The graphitizing includes heating the carbonized upgraded coal, the heating including heating to a first graphitization temperature for a first graphitization duration, wherein the first graphitization temperature is in the range of 1000° C. to 1500° C., and wherein the first graphitization duration is in the range of 0.1 s to 10 min. The heating also includes heating to a second graphitization temperature higher than the first graphitization temperature for a second graphitization duration, wherein the second graphitization duration is in the range of 0.1 s to 10 min. The heating also includes heating to a third graphitization temperature higher than the second graphitization temperature for a third graphitization duration, wherein the third graphitization temperature is in the range of 2700° C. to 3000° C., and wherein the third graphitization duration is in the range of 30 min to 3 h. The graphite has a fixed carbon content of 99 wt % to 100 wt %.
The present invention provides a method of forming graphite. The method includes cleaning coal to form a cleaned coal residue. The method includes at least one of (A) reacting the cleaned coal residue with an oxidizable inorganic metallic agent, and (B) reacting the cleaned coal residue with a reducing agent (i.e., includes (A), (B), or a combination of (A) and (B), to form an upgraded coal. The method includes heating the upgraded coal to a temperature of 500° C. to 2,000° C. in an inert environment, to form a carbonized upgraded coal. The method also includes heating the carbonized upgraded coal to a graphitization temperature in the range of 2500° C. to 3500° C. for a graphitization duration of 10 min to 10 h, to form the graphite.
The present invention provides a method of forming graphite. The method includes cleaning coal having a largest dimension of 25 mm or less using a strong mineral acid at a temperature of 30° C. to 100° C. to form a cleaned coal residue. The method also includes at least one of (A) reacting the cleaned coal residue at 100° C. to 500° C. under an inert gas with an oxidizable inorganic metallic agent including iron (II) sulfate heptahydrate (FeSO4.7H2O), iron (II) chloride tetrahydrate (FeCl.4H2O), or a combination thereof, and (B) reacting the cleaned coal residue at 0° C. to 50° C. in an organic solvent with a reducing agent including lithium aluminum hydride (LAH), sodium borohydride (NAH), or a combination thereof, to form an upgraded coal. The upgraded coal has a lower ash content, as compared to the coal used to form the upgraded coal. The upgraded coal has at least one of a lower oxygen concentration and a higher carbon concentration, as compared to the naturally-sourced coal used to form the upgraded coal. The method includes heating the upgraded coal to a temperature of 500° C. to 2,000° C. in an inert environment, to form a carbonized upgraded coal. The method also includes heating the carbonized upgraded coal to a graphitization temperature in the range of 2500° C. to 3500° C. for a graphitization duration of 10 min to 10 h, to form the graphite.
The present invention provides a method of forming graphite. The method includes cleaning coal having a largest dimension of 25 mm or less using a strong mineral acid at a temperature of 30° C. to 100° C. to form a cleaned coal residue. The method includes at least one of (A) reacting the cleaned coal residue at 100° C. to 500° C. under an inert gas with an oxidizable inorganic metallic agent including iron (II) sulfate heptahydrate (FeSO4.7H2O), iron (II) chloride tetrahydrate (FeCl.4H2O), or a combination thereof, and (B) reacting the cleaned coal residue at 0° C. to 50° C. in an organic solvent with a reducing agent including lithium aluminum hydride (LAH), sodium borohydride (NAH), or a combination thereof, to form an upgraded coal. The method includes heating the upgraded coal in an inert environment, to form a carbonized upgraded coal, wherein the heating includes heating to a first temperature for a first duration, wherein the first temperature is in the range of 500° C. to 700° C., and wherein the first duration is in the range of 15 min to 1 h. The heating also includes heating to a second temperature higher than the first temperature for a second duration, wherein the second temperature is in the range of 900° C. to 1100° C., and wherein the second duration is in the range of 15 min to 1 h. The heating also includes heating to a third temperature higher than the second temperature for a third duration, wherein the third temperature is in the range of 1,500° C. to 1,600° C., and wherein the third duration is in the range of 1 h to 3 h. The carbonized upgraded coal has an ash content of 1 wt % to 20 wt %. The carbonized upgraded coal has a fixed carbon (FC) content of 80 wt % to 99 wt %. The method also includes graphitizing the carbonized upgraded coal, to form the graphite. The graphitizing includes heating the carbonized upgraded coal, the heating including heating to a first graphitization temperature for a first graphitization duration, wherein the first graphitization temperature is in the range of 1000° C. to 1500° C., and wherein the first graphitization duration is in the range of 0.1 s to 10 min. The heating also includes heating to a second graphitization temperature higher than the first graphitization temperature for a second graphitization duration, wherein the second graphitization duration is in the range of 0.1 s to 10 min. The heating also includes heating to a third graphitization temperature higher than the second graphitization temperature for a third graphitization duration, wherein the third graphitization temperature is in the range of 2700° C. to 3000° C., and wherein the third graphitization duration is in the range of 30 min to 3 h. The graphite has a fixed carbon content of 99 wt % to 100 wt %.
The present invention provides a graphite that is formed using the method of forming graphite described herein.
The present invention provides a graphite that includes a carbonized and graphitized upgraded coal.
The present invention provides a graphite including croissant graphite that includes a croissant-like texture and shape.
The present invention provides an electrochemical cell. The electrochemical cell includes an electrode that includes the graphite of the present invention.
The present invention provides an electrochemical cell. The electrochemical cell includes a cathode. The electrochemical cell also includes an anode that includes the graphite of the present invention.
The present invention provides a lithium-ion battery that includes the electrochemical cell of the present invention.
Various aspects of the carbonization method, carbonized upgraded coal, graphitization method, graphitized carbonized upgraded coal, and graphite of the present invention have advantages over other methods, carbonized coals, and graphite.
For example, the carbonized upgraded coal, and/or the graphite formed therefore, can have lower ash content, oxygen content, volatile matter content, heteroatom content (e.g., S, N, O), and/or higher carbon content, as compared to other carbonized upgraded coals and graphites formed therefrom. In various aspects, the graphite of the present invention, such as graphite including “croissant” graphite, and the method of making the same, can provide more cost-effective and efficient graphite material for a variety of purposes, such as lithium-ion battery anodes, building materials (e.g., as building mixtures or composites), carbon-enhanced lubricants, additive manufacturing, carbon-based inks, coatings for corrosion prevention, or a combination thereof, as compared to other graphite provided from other sources.
The drawings illustrate generally, by way of example, but not by way of limitation, various aspects of the present invention.
Reference will now be made in detail to certain aspects of the disclosed subject matter. 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.
Throughout this document, values expressed in a range format should be interpreted in a flexible manner to include not only the numerical values explicitly recited as the limits of the range, but also to include all the individual numerical values or sub-ranges encompassed within that range as if each numerical value and sub-range is explicitly recited. For example, a range of “about 0.1% to about 5%” or “about 0.1% to 5%” should be interpreted to include not just about 0.1% to about 5%, but also the individual values (e.g., 1%, 2%, 3%, and 4%) and the sub-ranges (e.g., 0.1% to 0.5%, 1.1% to 2.2%, 3.3% to 4.4%) within the indicated range. The statement “about X to Y” has the same meaning as “about X to about Y,” unless indicated otherwise. Likewise, the statement “about X, Y, or about Z” has the same meaning as “about X, about Y, or about Z,” unless indicated otherwise.
In this document, the terms “a,” “an,” or “the” are used to include one or more than one unless the context clearly dictates otherwise. The term “or” is used to refer to a nonexclusive “or” unless otherwise indicated. The statement “at least one of A and B” or “at least one of A or B” has the same meaning as “A, B, or A and B.” In addition, it is to be understood that the phraseology or terminology employed herein, and not otherwise defined, is for the purpose of description only and not of limitation. Any use of section headings is intended to aid reading of the document and is not to be interpreted as limiting; information that is relevant to a section heading may occur within or outside of that particular section.
In the methods described herein, the acts can be carried out in a specific order as recited herein. Alternatively, in any aspect(s) disclosed herein, specific acts may be carried out in any order without departing from the principles of the invention, except when a temporal or operational sequence is explicitly recited. Furthermore, specified acts can be carried out concurrently unless explicit claim language recites that they be carried out separately or the plain meaning of the claims would require it. For example, a claimed act of doing X and a claimed act of doing Y can be conducted simultaneously within a single operation, and the resulting process will fall within the literal scope of the claimed process.
The term “about” as used herein 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, and includes the exact stated value or range.
The term “substantially” as used herein 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, or 100%. The term “substantially free of” as used herein can mean having none or having a trivial amount of, such that the amount of material present does not affect the material properties of the composition including the material, such that about 0 wt % to about 5 wt % of the composition is the material, or about 0 wt % to about 1 wt %, or about 5 wt % or less, or less than, equal to, or greater than about 4.5 wt %, 4, 3.5, 3, 2.5, 2, 1.5, 1, 0.9, 0.8, 0.7, 0.6, 0.5, 0.4, 0.3, 0.2, 0.1, 0.01, or about 0.001 wt % or less, or about 0 wt %.
Method of carbonizing an upgraded coal.
Various aspects of the present invention provide a method of carbonizing an upgraded coal. The method can include heating the upgraded coal in an inert environment, to form a carbonized upgraded coal. The inert environment can be any suitable inert environment, such as argon. The carbonization can include applying sufficient heat to the upgraded coal under sufficient conditions to drive off volatile carbon.
The carbonization heating can include heating to a carbonization temperature of 500° C. to 2,000° C. (e.g., 550° C. to 1,650° C., or less than or equal to 1650° C. and greater than or equal to 550° C., 600, 650, 700, 750, 800, 850, 900, 950, 1000, 1050, 1100, 1150, 1200, 1250, 1300, 1350, 1400, 1450, 1500, 1550, or 1600° C.) fora duration of 10 min to 6 h (e.g., 20 min to 4 h, or less than or equal to 4 h and greater than or equal to 20 min, 30, 40, 50 min, 1 h, 1.5, 2, 2.5, 3, 3.5, 4, 4.5, 5, or 5.5 h). The carbonization heating can be performed at any suitable pressure, such as about 1 atm, or about 0.5 atm to 2 atm, or about 0.1 atm to 10 atm.
The carbonization heating can include heating to a first temperature for a first duration. The first temperature can be in the range of 400° C. to 1,000° C., or 500° C. to 700° C., or less than or equal to 1000° C. and greater than or equal to 400° C., 450, 500, 550, 600, 650, 700, 750, 800, 850, 900, or 950° C. The first duration can be in the range of 10 min to 4 h, or 15 min to 1 h, or less than or equal to 4 h and greater than or equal to 10 min, 20, 30, 40, 50 min, 1 h, 1.5, 2, 2.5, 3, or 3.5 h. The heating can include heating to the first temperature at any suitable rate, such as at a rate of 1° C./min to 30° C./min, or 5° C./min to 15° C./min, or less than or equal to 30° C./min and greater than or equal to 1° C./min, 2, 3, 4, 5, 6, 8, 10, 12, 14, 16, 18, 20, 22, 24, 26, or 28° C./min.
The carbonization heating can further include heating to a second temperature higher than the first temperature for a second duration. The second temperature can be in the range of 600° C. to 1,500° C., or 900° C. to 1100° C., or less than or equal to 1500° C. and greater than or equal to 600° C., 650, 700, 750, 800, 850, 900, 850, 1000, 1050, 1100, 1150, 1200, 1250, 1300, 1350, 1400, or 1450° C. The second duration can be in the range of 10 min to 4 h, or 15 min to 1 h, or less than or equal to 4 h and greater than or equal to 10 min, 20, 30, 40, 50 min, 1 h, 1.5, 2, 2.5, 3, or 3.5 h. The heating from the first temperature to the second temperature can be performed at any suitable rate, such as a rate of 1° C./min to 30° C./min, 5° C./min to 15° C./min, or less than or equal to 30° C./min and greater than or equal to 1° C./min, 2, 3, 4, 5, 6, 8, 10, 12, 14, 16, 18, 20, 22, 24, 26, or 28° C./min.
The carbonization heating can further include heating to a third temperature higher than the second temperature for a third duration. The third temperature can be in the range of 1,000° C. to 2,000° C., or 1,500° C. to 1,600° C., or less than or equal to 2,000° C. and greater than or equal to 1000° C., 1050, 1100, 1150, 1200, 1250, 1300, 1350, 1400, 1450, 1500, 1550, 1600, 1650, 1700, 1750, 1800, 1850, 1900, or 1950° C. The third duration can be in the range of 30 min to 4 h, or 1 h to 3 h, or less than or equal to 4 h and greater than or equal to 10 min, 20, 30, 40, 50 min, 1 h, 1.5, 2, 2.5, 3, or 3.5 h. The heating from the second temperature to the third temperature can be performed at any suitable rate, such as a rate of 1° C./min to 30° C./min, or 5° C./min to 15° C./min, or less than or equal to 30° C./min and greater than or equal to 1° C./min, 2, 3, 4, 5, 6, 8, 10, 12, 14, 16, 18, 20, 22, 24, 26, or 28° C./min.
The carbonizing can further include allowing the temperature of the carbonized upgraded coal to cool to a suitable temperature, such as 0° C. to 1,000° C., or 0° C. to 40° C., or less than the carbonization temperature or less than or equal to 1000° C. and greater than or equal to 0° C., 5, 10, 15, 20, 25, 30, 35, 40, 50, 75, 100, 150, 200, 250, 500, 750, or 900° C. The cooling can be performed in an inert environment. The carbonized upgraded coal can be cooled or allowed to cool. The carbonized upgraded coal can be cooled at any suitable rate, such as at a rate of 1° C./min to 50° C./min, or 10° C./min to 30° C./min, or less than or equal to 50° C./min and greater than or equal to 1° C./min, 2, 3, 4, 5, 10, 15, 20, 25, 30, 35, 40, or 45° C./min.
The carbonization heating can include raising the temperature to about 600° C. at about 10° C./min and holding at about 600° C. for about 30 min, ramping the temperature to about 1000° C. at about 10° C./min and holding for about 30 min, and ramping the temperature to about 1600° C. at about 6° C./min and holding for about 2 h.
The upgraded coal on which the graphitization is performed can be any suitable upgraded coal, such as an upgraded lignite coal, and upgraded subbituminous coal, an upgraded bituminous coal, an upgraded anthracite coal, or a combination thereof. In various aspects, the upgraded coal is an upgraded lignite coal, an upgraded subbituminous coal, or a combination thereof.
The method can have any suitable yield of the carbonized upgraded coal from the upgraded coal, such as a yield of 30% to 99%, or 40% to 60%, or less than or equal to 99% and greater than or equal to 30%, 35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90, 95, 96, 97, or 98%.
The carbonized upgraded coal can have any suitable ash content, such as an ash content of 1 wt % to 20 wt %, or 2 wt % to 12 wt %, or less than or equal to 20 wt % and greater than or equal to 1 wt %, 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, 18, or 19 wt %.
The carbonized upgraded coal can have any suitable fixed carbon (FC) content, such as a FC content of 80 wt % to 99 wt %, or 85 wt % to 98 wt %, or less than or equal to 99 wt % and greater than or equal to 80 wt %, 82, 84, 86, 88, 90, 92, 94, 96, or 98 wt %.
The carbonized upgraded coal can include graphitic carbon and non-graphitic carbon. The carbonized upgraded coal can include non-graphitic carbon and can be substantially free of graphitic carbon.
In various aspects, the upgraded coal on which the carbonization is performed can includes an ash content of less than 5 wt %, an oxygen concentration of 10 wt % to 25 wt %, and a carbon concentration of 40 wt % to 75 wt %.
In various aspects, the upgraded coal is pre-formed prior to the onset of the method of carbonization or the method of forming graphite. In other aspects, the method of carbonization or the method of forming graphite include preparing the upgraded coal.
The upgraded coal can be prepared in any suitable way. In various aspects, upgrading the coal includes cleaning coal (e.g., starting material coal) to form a cleaned coal residue. The method can also include at least one of (A) reacting the cleaned coal residue with an oxidizable inorganic metallic agent, and (B) reacting the cleaned coal residue with a reducing agent (i.e., (A), (B), or (A) and (B)), to form the upgraded coal.
The coal that is cleaned can be any suitable coal (e.g., starting material coal). For example, the coal that is cleaned can be a crushed coal, a particulate coal, a coal waste (e.g., weathered overburden, underburden, coal fines, and/or coal processing reject materials), or a combination thereof.
The starting material coal can be a crushed coal or a particulate coal. The starting material coal can have any suitable size, such as having a largest dimension of 25 mm or less, or 1 micron to 25 mm, or 1 micron to 10 mm, or less than or equal to 25 mm but greater than or equal to 1 micron, 2, 3, 4, 5, 6, 8, 10, 12, 14, 15, 20, 25, 30, 40, 50, 75, 100, 150, 200, 250, 300, 400, 500, 750, 1 mm, 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, 18, 19, 20, 21, 22, 23, or 24 mm.
The cleaning of the coal to form the cleaned coal residue can be any suitable cleaning, such as cleaning the coal with a mineral acid, cleaning the coal with a base, physically cleaning the coal, or a combination thereof.
The cleaning of the coal to form the cleaned coal residue can include cleaning the coal with a base (e.g., an aqueous solution of a base). The base cleaning can be followed by washing with water to remove residual base therefrom and drying of the coal to remove some or all of the water.
The cleaning of the coal to form the cleaned coal residue can include physically cleaning the coal. The physical cleaning can include placing the coal in an aqueous solution of suitable density, as controlled by dissolution of a salt therein, and removing one or more desired fractions of the coal from the surface, bottom, or middle sections of the aqueous solution. For example, the physical cleaning can include suspending the coal in an aqueous solution comprising a salt such as cesium chloride. The aqueous solution can have any suitable specific gravity, such as a specific gravity of 1 to 2, or 1.4 to 1.6, or less than or equal to 2 but greater than or equal to 1, 1.1, 1.2, 1.3, 1.4, 1.5, 1.6, 1.7, 1.8, or 1.9.
The cleaning of the coal to form the cleaned coal residue can include cleaning the coal with a mineral acid, such as a strong mineral acid. The cleaning of the coal with the mineral acid can remove one or more inorganic elements from the coal, thereby reducing the ash content of the coal. The mineral acid can be any suitable mineral acid, such as phosphoric acid, sulfuric acid, boric acid, hydrofluoric acid, hydrobromic acid, perchloric acid, hydrochloric acid, nitric acid, or a combination thereof. The mineral acid can include hydrochloric acid, nitric acid, or a combination thereof. The mineral acid can include hydrochloric acid. The mineral acid can include nitric acid. The mineral acid can be of any suitable strength, such as 0.1 M to 10 M, 1 M to 5 M, 1 M to 1.5 M, or equal to or less than 10 M but greater than or equal to 0.1 M, 0.2, 0.4, 0.6, 0.8, 1, 1.1, 1.2, 1.3, 1.4, 1.5, 1.6, 1.8, 2, 2.5, 3, 3.5, 4, 4.5, 5, 6, 7, 8, or 9 M. During the acid cleaning, a ratio of a volume of the mineral acid to a weight of the coal can be 1:10 to 10:1, or 2:1 to 4:1, or less than or equal to 10:1 but greater than or equal to 1:10, 1:9, 1:8, 1:7, 1:6, 1:5, 1:4, 1:3, 1:2, 1:1, 2:1, 3:1, 4:1, 5:1, 6:1, 7:1, 8:1, or 9:1. The cleaning of the coal with the mineral acid can be conducted at any suitable temperature, such as a temperature of 30° C. to 100° C., 60° C. to 80° C., or less than or equal to 100° C. but greater than or equal to 30° C., 35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90, or 95° C. The coal can be cleaned with the mineral acid, and the temperature can be maintained, for any suitable duration, such as 1 h to 72 h, 12 h to 36 h, or greater than or equal to 1 h, 2, 4, 6, 8, 10, 12, 14, 16, 18, 20, 22 h, 1 d, 1.5, 2, 2.5, or 3 d or more. The cleaning of the coal with the mineral acid can be conducted at any suitable pressure, such as atmospheric pressure.
The method can further include washing the cleaned coal residue with an aqueous liquid. For example, the washing can be performed after the physical cleaning to remove residual acid or base from the coal, or residual salts left on the coal from an aqueous solution used for physical cleaning. The method can further include drying the coal to remove water therefrom prior to subsequent steps of the method.
The method can optionally include a size reduction step after the cleaning. The size reducing step can include crushing or grinding the coal residue to reduce the particle size thereof, to a size that is smaller than the coal prior to the cleaning. The smaller size can include a largest dimension of 500 microns or less, such as 1 micron to 100 microns, such as less than or equal to 500 microns but greater than or equal to 1 micron, 2, 3, 4, 5, 6, 8, 10, 12, 14, 15, 20, 25, 30, 40, 50, 75, 100, 200, 300, or 400 microns.
The method can include reacting the cleaned coal residue with an oxidizable inorganic metallic agent. The reacting of the cleaned coal residue with the oxidizable inorganic metallic agent can remove one or more heteroatoms from the cleaned coal residue, such as oxygen, sulfur, or a combination thereof. The oxidizable inorganic metallic agent can be any suitable material that removes one or more heteroatoms from the cleaned coal residue, such as a salt including iron(II), cerium(III), manganese(II), cobalt(II), chromium(III), copper(I), tin(II), or a combination thereof. The oxidizable inorganic metallic acid can include iron sulfate or a hydrate thereof. The oxidizable inorganic metallic agent can include iron (II) sulfate heptahydrate (FeSO4.7H2O). The oxidizable inorganic metallic agent can include iron chloride or a hydrate thereof. The oxidizable inorganic metallic agent can include iron (II) chloride tetrahydrate (FeCl.4H2O). The oxidizable inorganic metallic can be reacted with the cleaned coal residue in a suitable solvent, such as an aqueous solvent.
The reacting of the cleaned coal residue with the oxidizable inorganic metallic agent can be performed in a reactor, such as an autoclave. The reacting of the cleaned coal residue with the oxidizable inorganic metallic agent can be performed at any suitable reaction temperature, such as 100° C. to 500° C., 250° C. to 350° C., or less than or equal to 500° C. but greater than or equal to 100° C., 120, 140, 160, 180, 200, 220, 240, 250, 260, 270, 280, 290, 300, 310, 320, 330, 340, 350, 360, 380, 400, 420, 440, 460, or 480° C. The reacting of the cleaned coal residue with the oxidizable inorganic metallic agent can be performed under any suitable gas environment, such as under air, or under an inert gas such as argon. The reaction of the cleaned coal residue with the oxidizable inorganic metallic agent can be performed in an environment that has been evacuated and flushed with an inert gas (e.g., argon) one or more times. The reaction of the cleaned coal residue with the oxidizable inorganic metallic agent can be performed in the substantial absence of oxygen (e.g., less than 0.01 vol %, or less than 0.0001 vol %). The reaction of the cleaned coal residue with the oxidizable inorganic metallic agent can be performed for any suitable duration, during which the reaction temperature is maintained, such as 30 min to 5 h, 1 h to 3 h, or at least 30 min, 1 h, 2, 3, 4, or 5 h, or less than or equal to 5 h but greater than or equal to 30 min, 1 h, 1.5, 2, 2.5, 3, 3.5, 4, or 4.5 h.
After the reaction of the cleaned coal residue with the oxidizable inorganic metallic agent, the reaction mixture can be actively or passively cooled, such as to room temperature. After the reaction of the cleaned coal residue with the oxidizable inorganic metallic agent, the cleaned coal residue can be washed with water one or more times to remove residual oxidizable inorganic metallic agent or other undesired material from the coal. After the reaction of the cleaned coal residue with the oxidizable inorganic metallic agent, the cleaned coal residue can be dried to remove water therefrom.
The method can include reacting of the cleaned coal residue with the reducing agent. The reacting of the cleaned coal residue with the reducing agent can remove organic functional groups from the cleaned coal residue, such as carboxylic acids, carbonyl groups, ethers, aliphatic groups, or a combination thereof. The reacting of the cleaned coal residue with the reducing agent can reduce C═O groups in the cleaned coal residue (e.g., to alcohols, and/or with complete removal of the oxygen atom). The reducing agent can be any suitable reducing agent, such as lithium aluminum hydride, sodium borohydride, diborane, 9-BBN, aluminum hydride, lithium borohydride, diisobutylaluminum hydride, or a combination thereof. The reducing agent can include lithium aluminum hydride (LAH).
The reacting of the cleaned coal residue with the oxidizable inorganic metallic agent can be performed in a reactor. The reaction temperature of the reaction of the cleaned coal residue with the reducing agent can be at any suitable temperature, such as 0° C. to 50° C., or room temperature, or less than or equal to 50° C. but greater than or equal to 0° C., 5, 10, 15, 20, 25, 30, 35, 40, or 45° C. The reacting of the cleaned coal residue with the reducing agent can be conducted for any suitable duration, during which the reaction temperature is maintained, such as 1 min to 24 h, 10 min to 30 min, or at least 1 min, or less than or equal to 24 h but greater than or equal to 1 min, 2, 4, 6, 8, 10, 15, 20, 25, 30, 35, 40, 45, 50, 55 min, 1 h, 1.5, 2, 2.5, 3, 4, 5, 6, 8, 10, 12, 14, 16, 18, 20, or 22 h. The reacting of the cleaned coal residue with the reducing agent can be performed in a suitable solvent, such as an organic solvent, such as an ether (e.g., diethylether).
Reacting the cleaned coal residue with the reducing agent can further include working up the product of the reacting of the cleaned coal residue with the reducing agent, such as working up the product with water. The method can further include drying the cleaned coal residue after performing the reacting of the cleaned coal residue with the reducing agent, to remove water therefrom.
In some embodiments of the method, reacting of the cleaned coal residue with the oxidizable inorganic metallic agent is performed and the reacting of the cleaned coal residue with the reducing agent is not performed. In some embodiments, reacting of the cleaned coal residue with the reducing agent is performed and the reacting of the cleaned coal residue with the oxidizable inorganic metallic agent is not performed. In some embodiments, both the reacting of the cleaned coal residue with the oxidizable inorganic metallic agent is performed and the reacting of the cleaned coal residue with the reducing agent is performed, as sequential reactions. For example, the method can include first reacting the cleaned coal residue with the oxidizable inorganic metallic agent and then reacting the product thereof with the reducing agent. In another example, the method can include first reacting the cleaned coal residue with the reducing agent, and then reacting the product thereof with the oxidizable inorganic metallic agent. In embodiments that include both reactions in sequence, it is to be understood that for the second reaction, references herein to the starting material of the reaction being the cleaned coal residue can be replaced with the product of the prior reaction.
The upgraded coal can include any suitable ash content. Ash content can be determined via ASTM D7582. The upgraded coal can include an ash content of less than 5 wt %, or 0.5 to 2 wt %, or less than or equal to 5 wt % but greater than or equal to 0.1 wt %, 0.2, 0.3, 0.4, 0.5, 0.6, 0.7, 0.8, 0.9, 1, 1.2, 1.4, 1.6, 1.8, 2, 2.2, 2.4, 2.6, 2.8, 3, 3.5, 4, or 4.5 wt %. The upgraded coal can include an ash content that is lower than an ash content of the coal prior to the cleaning, such as 4 wt % to 15 wt % lower, or lower by less than or equal to 15 wt % but greater than or equal to 4 wt %, 5, 6, 7, 8, 9, 10, 11, 12, 13, or 14 wt %.
The upgraded coal can include any suitable oxygen content. The upgraded coal can include an oxygen concentration of 10 wt % to 25 wt %, or less than or equal to 25 wt % but greater than or equal to 10 wt %, 11, 12, 13, 14, 15, 16, 17, 18, 19, 20, 21, 22, 23, or 24 wt %. The upgraded coal can include an oxygen content that is lower than an oxygen content of the coal prior to the cleaning, such as 1% to 50% lower, 15% to 25% lower, 17% to 21% lower, or less than or equal to 50% lower but greater than or equal to 1% lower, 2, 3, 4, 5, 6, 8, 10, 11, 12, 13, 14, 15, 16, 17, 18, 19, 20, 21, 22, 23, 24, 25, 26, 28, 30, 35, 40, or 45% lower.
The upgraded coal can have any suitable carbon concentration. The upgraded coal can include a carbon concentration of 40 wt % to 75 wt %, or less than or equal to 75 wt % but greater than or equal to 40 wt %, 42, 44, 46, 48, 50, 52, 54, 56, 58, 60, 62, 64, 66, 68, 70, 72, or 74 wt %. The upgraded coal can include a higher carbon concentration than the coal prior to the cleaning, such as 1% to 30% higher, or 5% to 15% higher, or less than or equal to 30% higher but greater than or equal to 1% higher, 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, 18, 19, 20, 22, 24, 26, or 28% higher.
The upgraded coal can have any suitable sulfur concentration. The upgraded coal can include a sulfur concentration of 0.1 wt % to 5 wt %, or 0.7 wt % to 1.05 wt %, or less than or equal to 5 wt % but greater than or equal to 0.1 wt %, 0.2, 0.4, 0.6, 0.7, 0.8, 0.85, 0.9, 0.95, 1, 1.05, 1.1, 1.15, 1.2, 1.25, 1.3, 1.35, 1.4, 1.45, 1.5, 1.6, 1.8, 2, 3, or wt %. The upgraded coal can include a lower sulfur concentration than the coal prior to the cleaning, such as 10% to 30% lower, or 15% to 25% lower, or less than or equal to 30% lower but greater than or equal to 10% lower, 11, 12, 13, 14, 15, 16, 17, 18, 19, 20, 21, 22, 23, 24, 25, 26, 27, 28, or 29% lower.
In various aspects, the present invention provides a carbonized upgraded coal formed by the method of carbonizing an upgraded coal described herein. The carbonized upgraded coal can be any suitable carbonized upgraded coal that can be formed using the method.
In various aspects, the present invention provides a carbonized upgraded coal that includes a fixed carbon (FC) content of 85 wt % to 98 wt %, or equal to or less than 98 wt % and greater than or equal to 85 wt %, 86, 87, 88, 89, 90, 91, 92, 93, 94, 95, 96, or 97 wt %. The carbonized upgraded coal can include an ash content of 2 wt % to 12 wt %, or less than or equal to 12 wt % and greater than or equal to 2 wt %, 3, 4, 5, 6, 7, 8, 9, 10, or 11 wt %.
In various aspects, the method of carbonizing an upgraded coal is a method of forming graphite, and the method includes graphitizing the carbonized upgraded coal to form the graphite. In various aspects, the present invention provides a method of forming graphite from a carbonized upgraded coal that is formed prior to the onset of the method, wherein the method includes graphitizing the carbonized upgraded coal to form the graphite. The graphitizing can include applying sufficient energy to the carbonized upgraded coal under sufficient conditions to induce a change of crystal structure and form graphite.
The graphitizing can include heating the carbonized upgraded coal in an inert environment, to form the graphite. The inert environment can be any suitable inert environment, such as argon. The heating can include heating to a graphitization temperature in the range of 2500° C. to 3500° C. (e.g., 2700° C. to 3000° C., or less than or equal to 3500° C. and greater than or equal to 2500, 2550, 2600, 2650, 2700, 2750, 2800, 2850, 2900, 2950, 3000, 3050, 3100, 3150, 3200, 3250, 3300, 3350, 3400, or 3450° C.) for a graphitization duration of 10 min to 10 h (e.g., 30 min to 3 h, or less than or equal to 10 h and greater than or equal to 10 min, 20, 30, 40, 50 min, 1 h, 1.5, 2, 2.5, 3, 4, 5, 6, 7, 8, or 9 h). The graphitization heating can be performed at any suitable pressure, such as about 1 atm, or about 0.5 atm to 2 atm, or about 0.1 atm to 10 atm.
The graphitization heating can include heating to the graphitization temperature for the graphitization duration a first time, allowing the temperature to cool to a temperature below the graphitization temperature, and heating to the graphitization temperature for the graphitization duration a second time. The temperature to which the material is allowed to cool between multiple heating steps (the temperature below the graphitization temperature) can be 0° C. to 50° C., or 0° C. to 1000° C., or less than the graphitization temperature or less than or equal to 1000° C. and greater than or equal to 0° C., 5, 10, 15, 20, 25, 30, 35, 40, 50, 75, 100, 150, 200, 500, 750, or 900° C.
The graphitization heating can include heating to a first graphitization temperature for a first graphitization duration. The first graphitization temperature can be in the range of 700° C. to 1700° C., or 1000° C. to 1500° C., or less than or equal to 1700° C. and greater than or equal to 700° C., 750, 800, 850, 900, 950, 1000, 1050, 1100, 1150, 1200, 1250, 1300, 1350, 1400, or 1450° C. The first graphitization duration can be in the range of 0.01 s to 4 h, or 0.1 s to 10 min, or less than or equal to 4 h and greater than or equal to 0.01 s, 0.05, 0.1, 0.5, 1, 2, 5, 10, 20, 30, 40, 50 s, 1 min, 2, 3, 4, 5, 10, 20, 30, 40, 50 min, 1 h, 1.5, 2, 2.5, 3, or 3.5 h. The heating can include heating to the first graphitization temperature at a rate of 5° C./min to 100° C./min, 40° C./min to 80° C./min, or less than or equal to 100° C./min and greater than or equal to 5° C./min, 10, 15, 20, 25, 30, 35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90, or 95° C./min.
The graphitization heating can further include heating to a second graphitization temperature higher than the first graphitization temperature for a second graphitization duration. The second graphitization temperature can be in the range of 1500° C. to 3000° C., or 2200° C. to 2800° C., or less than or equal to 3000° C. and greater than or equal to 1500° C., 1550, 1600, 1650, 1700, 1750, 1800, 1850, 1900, 1950, 2000, 2050, 2100, 2150, 2200, 2250, 2300, 2350, 2400, 2450, 2500, 2550, 2600, 2650, 2700, 2750, 2800, 2850, 2900, or 2950° C. The second graphitization duration can be in the range of 0.01 s to 4 h, or 0.1 s to 10 min, or less than or equal to 4 h and greater than or equal to 0.01 s, 0.05, 0.1, 0.5, 1, 2, 5, 10, 20, 30, 40, 50 s, 1 min, 2, 3, 4, 5, 10, 20, 30, 40, 50 min, 1 h, 1.5, 2, 2.5, 3, or 3.5 h. The graphitization heating can include heating from the first graphitization temperature to the second graphitization temperature at a lower rate than heating to the first graphitization temperature. The graphitization heating can include heating from the first graphitization temperature to the second graphitization temperature at a rate of 1° C./min to 50° C./min, 10° C./min to 30° C./min, or less than or equal to 50° C./min and greater than or equal to 1° C./min, 2, 3, 4, 5, 6, 8, 10, 12, 14, 16, 18, 20, 22, 24, 26, 28, 30, 35, 40, or 45° C./min.
The graphitization heating can further include heating to a third graphitization temperature higher than the second graphitization temperature for a third graphitization duration. The third graphitization temperature can be in the range of 2500° C. to 3500° C., or 2700° C. to 3000° C., or less than or equal to 3500° C. and greater than or equal to 2500° C., 2550, 2600, 2650, 2700, 2750, 2800, 2850, 2900, 2950, 3000, 3050, 3100, 3150, 3200, 3250, 3300, 3350, 3400, or 3450° C. The third graphitization duration can be in the range of 0.01 s to 4 h, or 30 min to 3 h, or less than or equal to 4 h and greater than or equal to 0.01 s, 0.05, 0.1, 0.5, 1, 2, 5, 10, 20, 30, 40, 50 s, 1 min, 2, 3, 4, 5, 10, 20, 30, 40, 50 min, 1 h, 1.5, 2, 2.5, 3, or 3.5 h. The graphitization heating can include heating from the second graphitization temperature to the third graphitization temperature at a lower rate than heating from the first graphitization temperature to the second graphitization temperature. The heating can include heating from the second graphitization temperature to the third graphitization temperature at a rate of 1° C./min to 30° C./min, or 2° C./min to 20° C./min, or less than or equal to 30° C./min and greater than or equal to 1° C./min, 2, 3, 4, 5, 6, 8, 10, 12, 14, 16, 18, 20, 22, 24, 26, or 28° C./min.
The method can further include allowing the graphite to cool. The cooling can be performed under an inert atmosphere. The graphite can be cooled or allowed to cool to any suitable temperature below the graphitization temperature. For example, the method can include allowing the graphite to cool to 0° C. to 1,000° C., 0° C. to 40° C., or less than the graphitization temperature or less than or equal to 1000° C. and greater than or equal to 0° C., 5, 10, 15, 20, 25, 30, 35, 40, 50, 100, 150, 200, 250, 500, 750, or 900° C. The graphite can be cooled or allowed to cool at any suitable rate, such as a rate of 1° C./min to 50° C./min, or 10° C./min to 30° C./min, or less than or equal to 50° C./min and greater than or equal to 1° C./min, 2, 3, 4, 5, 6, 8, 10, 15, 20, 25, 30, 35, 40, or 45° C./min.
The graphitization heating can include heating at about 60° C./min to about 1250° C., and then heating at about 20° C./min to about 2500° C., and then heating at about 8° C./min to about 2800° C.
The graphite formed by the method can have any suitable moisture content, such as a moisture content of about 0 wt %, or 0 wt % to 0.03 wt %, or less than or equal to 0.03 wt % and greater than or equal to 0 wt %, 0.0001 wt %, 0.0005 wt %, 0.001 wt %, 0.005 wt %, 0.01 wt %, or 0.02 wt %, 0.03 wt %
The graphite formed by the method can have any suitable ash content, such as an ash content of 0 wt % to 2 wt %, or 0.0001 wt % to 0.03 wt %, or less than or equal to 2 wt % and greater than or equal to 0 wt %, 0.0001 wt %, 0.0005 wt %, 0.001 wt %, 0.005 wt %, 0.01 wt %, or 0.02 wt %.
The graphite formed by the method can have any suitable fixed carbon (FC) content, such as an FC content of 98 wt % to 100 wt %, 99 wt % to 99.9999 wt %, or less than or equal to 100 wt % and greater than or equal to 98 wt %, 98.5 wt %, 99 wt %, 99.2, 99.4, 99.6, 99.7, 99.8, 99.9, 99.99, or 99.999 wt %.
The graphite formed by the method can have any suitable volatile matter (VM) content, such as a VM content of 0.01 wt % to 2 wt %, 0.1 wt % to 1.2 wt %, or less than or equal to 2 wt % and greater than or equal to 0.01 wt %, 0.05, 0.1, 0.2, 0.4, 0.6, 0.8, 1, 1.2, 1.4, 1.6, or 1.8 wt %.
The graphite formed by the method can have any suitable oxygen concentration, such as an oxygen concentration of 0 wt % to 2 wt %, 0.001 wt % to 0.5 wt %, or less than or equal to 2 wt % and greater than or equal to 0 wt %, 0.0001 wt %, 0.0005, 0.001, 0.005, 0.01, 0.05, 0.1, 0.2, 0.3, 0.4, 0.5, 0.6, 0.8, 1, 1.2, 1.4, 1.6, or 1.8 wt %.
The graphite formed by the method can have any suitable nitrogen concentration, such as a nitrogen concentration of 0 wt % to 2 wt %, 0.001 wt % to 0.5 wt %, or less than or equal to 2 wt % and greater than or equal to 0 wt %, 0.0001 wt %, 0.0005, 0.001, 0.005, 0.01, 0.05, 0.1, 0.2, 0.3, 0.4, 0.5, 0.6, 0.8, 1, 1.2, 1.4, 1.6, or 1.8 wt %.
The graphite formed by the method can have any suitable sulfur concentration, such as a sulfur concentration of 0 wt % to 2 wt %, 0.001 wt % to 0.5 wt %, or less than or equal to 2 wt % and greater than or equal to 0 wt %, 0.0001 wt %, 0.0005, 0.001, 0.005, 0.01, 0.05, 0.1, 0.2, 0.3, 0.4, 0.5, 0.6, 0.8, 1, 1.2, 1.4, 1.6, or 1.8 wt %.
The graphite formed by the method can have any suitable heteroatom content, such as a heteroatom content of 0 wt % to 2 wt %, or 0.001 wt % to 0.5 wt %, or less than or equal to 2 wt % and greater than or equal to 0 wt %, 0.0001 wt %, 0.0005, 0.001, 0.005, 0.01, 0.05, 0.1, 0.2, 0.3, 0.4, 0.5, 0.6, 0.8, 1, 1.2, 1.4, 1.6, or 1.8 wt %.
The graphite can include croissant graphite, needle-like graphite, isotropic blocky graphite, flake graphite, or a combination thereof. The graphite can include croissant graphite; e.g., the graphite includes particles that have a croissant-like texture and shape, and/or the graphite includes particles that are or that include 2D-graphene sheets spiral-wound or folded into ribbon-like structures. The croissant graphite can have a crystallinity that is comparable to (e.g., substantially the same as) that of natural flake graphite, as determined by XRD.
Various aspects of the present invention provide a graphite made by the method of the present invention or having identical properties to a graphite made by the method of the present invention. The graphite can be any graphite made by a method of the present invention, such as a graphite including croissant graphite. The graphite can include a carbonized graphitized upgraded coal. The graphite can include particles that have a croissant-like texture and shape.
In various aspects, the present invention provides an electrochemical cell. The electrochemical cell includes at least one electrode that includes the graphite of the present invention (e.g., including croissant-shaped graphite). The electrochemical cell can include an anode and a cathode, and the anode can include the graphite of the present invention.
In various aspects, the present invention provides a lithium-ion battery. The lithium-ion battery includes the electrochemical cell of the present invention, including an electrode (e.g., an anode) that includes the graphite of the present invention (e.g., including croissant-shaped graphite).
X-ray diffraction (XRD) analysis shows that croissant graphite particles possess a high degree of crystallinity that is comparable to that of natural flake graphite. Although the mechanisms of formation of the croissant graphite structures are still under investigation, initial examination of several particle morphologies suggests the mode of formation might involve spiral-winding or folding of 2D graphene sheets into ribbon-like structures and to croissant graphite structures. Because of the texture and spheroidal shapes of croissant graphite particles, it is expected that these types of particles will be useful for the fabrication of efficient lithium-ion batteries for electric vehicle (EV) and energy storage applications as well as preparation of high-value solid carbon products such as graphene.
Various aspects of the present invention can be better understood by reference to the following Examples which are offered by way of illustration. The present invention is not limited to the Examples given herein.
The coal samples were obtained from Center Mine, Freedom Mine, and Falkirk Mine in North Dakota, USA and crushed to ¼-inch-size particles and subjected to physical and chemical cleaning procedures. The coals were crushed to ¼-inch size particles and subsamples were analyzed to determine the coal properties by proximate analysis (ASTM D7582), ultimate analysis (ASTM D5373, D5016), heating value (ASTM D5865), and x-ray fluorescence (XRF) spectroscopy. The results presented in Table 1 are as expected for ND lignite.
The goal of cleaning the raw coal is to reduce the ash content so that the resultant product can be a better precursor for making graphene, other materials and/or utilized as feedstock to other processes. The cleaning process involved three steps presented below, together with the results obtained.
Step 1A. Physical cleaning. Physical cleaning was performed on Center Mine and Freedom Mine coals using the float-sink method in an aqueous solution of CsCl with varying specific gravities. The principle of physical cleaning is that inorganic minerals in coals that produce ash are heavier than coal and should sink in an aqueous salt solution with higher specific gravity than water. Thus, the float fraction at an optimal specific gravity is the clean fraction. Two specific gravities of CsCl solutions or 1.4 and 1.5 were investigated using the +20-mesh size fraction of the coals. The ash content of the physically cleaned residue was determined by ASTM D7582. The results presented in Table 2 show that better cleaning was achieved by a higher specific gravity solution of CsCl. However, the ash content of the “cleaned” coals were higher than those of the raw coals primarily because of the difficulty of removing residual Cs from the clean coal residue. Thus, the resulting residue was subjected to a further cleaning step with mineral acid.
Step 1B. Chemical cleaning after physical cleaning. The +20-mesh float fraction of Center Mine and Freedom Mine lignite after physical cleaning were subjected to chemical cleaning using nitric and hydrochloric acids. DI water was used as the control, while 1.4 M and 1.5 M concentrations of HNO3 and HCl were tested to determine their performance, using a 3:1 ratio of acid to coal (volume:weight). The acid cleaned residues were analyzed to determine the ash content. The results presented in Table 3 indicate that physical cleaning, followed by chemical cleaning yielded percent reductions of 79% to 85%, with actual residual ash in the cleaned product of 1-2 wt %. This residual ash content is well below the 5-wt % target set at the beginning of the project.
Step 2. Chemical cleaning only. A chemical cleaning only step was investigated to evaluate the possibility to use only chemical acids for the cleaning without an initial physical cleaning step to avoid unnecessary steps, which enhances the process economic feasibility. The chemical cleaning step involved using mineral acids such as hydrochloric acid to clean the +20-mesh coal samples. For comparison, a −200-mesh particle-size sample of Falkirk lignite was also cleaned to determine any potential particle-size effects on the cleaning process. The ash content of the cleaned residues was determined by proximate analysis (ASTM D7582). The results shown in Table 4 indicate percent ash reductions in the range 43% to 66%, with no major particle-size effects observed in the Falkirk coal results. While these results are good, they represent a slightly lower ash reduction performance by only conducting chemical cleaning compared to physical and chemical cleaning combined (see Table 4).
The clean coal residue obtained by acid cleaning of the raw coal was treated in an autoclave reactor, with the aim to reduce the content of heteroatoms such as oxygen or sulfur. Heteroatoms, particularly oxygen, can promote cross-linking reactions that produce isotropic char during heat treatment in the production of synthetic graphite. Cross-linking reduces the quality (low crystallinity) of the resulting graphitic material, thus, rendering it unsuitable for making graphene or for other applications that require high quality graphite. The autoclave reactor used in these experiments is rated at maximum temperature and pressure limits of 600° C. and about 5000 psi, respectively. A schematic of the autoclave reactor system 10 is shown in
The coal sample was prepared as a slurry of the coal in an aqueous solution of the oxidizable inorganic metallic agent. Center lignite was reacted with an aqueous solution of hydrated ferrous chloride, while Falkirk and Freedom lignite were reacted with an aqueous solution of hydrated ferrous sulfate. The coal slurry sample was placed in the autoclave reactor sleeve, and the system was sealed off. The reactor was evacuated to about −28 inHg vacuum to remove any trapped air/oxygen and then backfilled and flushed with argon. After five cycles of evacuation, backfilling and flushing, the system was placed at atmospheric pressure using argon. The reactor was heated to the target temperature of 300° C. (572° F.). The target temperature was maintained for about 1 hr 30 min, and then the heaters were turned off to allow gradual cooling to room temperature overnight. Ideally, the reactor is cooled rapidly to room temperature to quench the reaction by installing cooling coils in the autoclave reactor. The coal residue was recovered and rinsed three times with DI water or until a clear solution filtrate was obtained. The filtered residue was placed in aluminum trays and dried in an oven at 70° C. for 24 hrs and then stored in an air-tight container.
Samples of the vapors generated during reaction in the autoclave were collected using chromatographic gas bags, which were subsequently analyzed by gas chromatography (GC). The results are presented in Table 5 and include all gas components with available calibrations. The results show that a significant fraction of the gases evolved was CO2 for all three coals. Alongside CO2 were H2, CO, N2, and H2S, with small detections of light hydrocarbons (C1-C5) at less than 0.1%, except for methane that was detected at 0.4%, 0.8%, and 1.8% for Center lignite, Falkirk lignite, and Freedom lignite, respectively. The closures for the gas analyses were 99.5%, 105.6%, and 110.6% for Center, Falkirk, and Freedom lignite, respectively. These closures indicate that the amount of undetected species (due to no calibration standard) was about 10% or less, which suggest that the results in Table 5 give a good representation of the major components of the gas stream evolved during autoclave coal reactions for each lignite. The results further indicate that loss of oxygen and sulfur likely occur as CO2, CO, and H2S.
The results of proximate and ultimate analyses of the autoclave-reacted coal residues are presented in Table 6 together with the raw coal analysis for comparison. The proximate analysis data indicate that the volatile matter (VM) in the coals reduced by 13%-19%, with a corresponding increase in fixed carbon (FC) by 16%-19%. Ultimate analysis results show a 17%-21% reduction in oxygen, 9%-10% increase in Btu, 8%-10% decrease in H2, and 9%-11% increase in carbon, which corroborate the reduced VM and increased FC observed in proximate analysis. There is a small sulfur reduction of 4% for reacted Center lignite, but a 13% and 29% increase in sulfur for Freedom and Falkirk lignite, respectively. The observed differences in sulfur contents is attributed to the use of ferrous sulfate for treating Falkirk and Freedom lignite as opposed to ferrous chloride used for Center lignite. Because the chemical reagent used in these tests was primarily aimed at reducing the oxygen content in the coals, the reduction of sulfur by 4% in Center lignite provides additional benefit and ability to reduce the heteroatom content of coals. The decrease in VM, increase in FC, and reduction in oxygen content of the reacted coals relative to the raw coals are all good characteristics that enable the reacted coals to be better graphene precursors.
The XRF analysis results of the autoclave-reacted coals, including data for the raw coals for comparison, are presented in Table 7. The results show an increase in some of the components and a decrease in others; these findings are consistent with the nature of the reactions. Sulfur represented in oxide form shows a significant reduction, which is different from what was observed in ultimate analysis and can be attributed to differences in the analytical techniques.
The residue obtained from the acid cleaning process or from the autoclave experiments was treated with lithium aluminum tetrahydride (LAH) primarily to reduce multiple bonds of oxygen functional groups such as carbonyl or carboxylic acid or multiple bonds in any nitrogen functional groups. The LAH experiments were conducted on separate portions of the coal residue obtained from the acid cleaning step or from the autoclave reaction. In each experiment, 20 g of coal residue was mixed with 50 mL of LAH solution in diethylether (DEE) and stirred for 20 minutes. DI water was used for reaction work-up. The resultant mixture was rinsed several times with additional DI water until a clear filtrate solution was obtained. The final residue was dried in an oven at 70° C. overnight and then stored in air-tight containers prior to analysis.
Elemental analysis results shown in Table 8 indicate a reduction in sulfur content by 24 wt % and 22 wt % for Center lignite and Freedom lignite, respectively. The nitrogen content was reduced by 15 wt % (Center coal) and 5 wt % (Freedom coal), while the oxygen content increased by 19 wt % for Center coal and 21 wt % for Freedom coal. The increase in oxygen, rather than a decrease, is because of residual oxygen content in the leftover LAH products of the reactions. Since the ultimate analysis determines oxygen content by difference, it is impossible to distinguish oxygen present in LAH products versus oxygen in coal residue. As discussed later in the FTIR analysis section, the LAH reactions were successful in reducing the C═O multiple bond groups to alcohols, as well as demonstrate efficacy in reducing the heteroatom content. Removal of the LAH reaction byproducts would further improve the quality of the residue as a graphene precursor or for other applications.
FTIR spectroscopy is an effective, quick, nondestructive technique for obtaining chemical information from a sample, especially regarding the different organic functional groups. An attenuated total reflection (ATR) FTIR spectrometer was used for these analyses. In each case, a finely ground powder sample sieved through a −325 mesh (≤44 μm) was used for the analysis.
To demonstrate the effectiveness of the LAH reaction and its ability to reduce C═O multiple bonds in the coals to their corresponding single bonds as in alcohols, this reaction was carried out on Center Mine and Freedom lignite autoclave-reacted residues. In
The method developed in this Part comprises four steps, including physical and chemical cleaning, heteroatom reduction reaction (HRR), carbonization, and graphitization.
Subsamples of coal were crushed to −30-mesh (0.57 mm) or −60-mesh (0.26 mm) or ¼-inch (6.35 mm) particle sizes. About 500 g was subjected to physical and chemical cleaning procedures. Physical cleaning involved a flotation approach based on specific gravity separation where the crushed coal sample was mixed with a cesium chloride (CsCl) solution prepared to have a specific gravity of about 1.5, 1.8 or 2.0 or higher in a large separatory funnel or similar device. The mixture was allowed to separate freely under gravity for about 5 to 10 minutes and the float fraction was recovered for further cleaning with mineral acids. Multiple physical separations can be utilized depending on the feedstock material and its starting ash content, with higher ash content requiring multiple physical separations.
Chemical cleaning was performed with aqueous hydrochloric acid solution. The coal sample from the physical cleaning step was mixed with a 1.5 M or 1.8 M or 2.0 M or 2.5 M or 3.0 M HCl solution in the ratio of 3 parts acid by volume to 1 part coal by mass. The mixture was stirred gently overnight at 50° C. to 70° C. using the apparatus with the schematic shown in
Heteroatoms in the starting carbon ore materials or feedstocks refer to nitrogen (N), sulfur (S), and oxygen (O) which are collectively referred to as NSO. The clean coal residue was further upgraded by reacting with a 0.5 M or suitable concentration of ferrous chloride solution in an autoclave reactor (as illustrated in
Carbonization of the upgraded coal samples was conducted using a system illustrated in
Graphitization of the coal samples was performed using the graphite furnace shown schematically in
Two sets of samples that underwent different preprocessing conditions were graphitized. The first set was cleaned, carbonized, and graphitized (prefix C-), while the second set was cleaned, HRR in an autoclave, carbonized, and graphitized (prefix CA-). The coal-derived graphite samples are abbreviated as LDG, SDG, BDG, and ADG for lignite-, subbituminous-, bituminous-, and anthracite-derived graphite, respectively. For example, the first set is named C-LDG, C-SDG, C-BDG, and C-ADG. The graphitization conditions were varied from 1 hr (1H), 2 hrs total time heated 1 hr in succession (1H1H), and 2 hrs direct heating (2H). The sample identifications based on graphitization conditions is provided in Table 9.
In this Part, the carbon ore feedstock used was primarily coal. The raw coal samples were analyzed to determine the coal characteristics by proximate and ultimate analysis, x-ray fluorescence (XRF) spectroscopy, and solid-state attenuated total reflectance-Fourier transform infrared (ATR-FTIR) spectroscopy. XRF results in Table 10 indicate that the bituminous and anthracite samples are high in silica and alumina, while lignite and subbituminous samples are high in calcium and sulfur. All other chemical species across all four coals are moderate to low in concentration. The proximate and ultimate analysis results (Table 11) show high moisture for lignite and subbituminous coals and relatively low moisture for bituminous and anthracite coals. The ash content of bituminous coal sample was high. The heating values of lignite and subbituminous coals are higher than typical and indicate relatively good quality coal samples. These results were helpful in developing methods to effectively remove inorganic constituents that produce ash in coals.
FTIR spectroscopy provides information about the key functional groups in the coals and was used to qualitatively evaluate the coal samples for ash content, volatile (aliphatic) content, aromatic content, and oxygen-containing functional groups. The ATR-FTIR spectra of the raw coal samples (
Proximate and ultimate analysis (Table 12) of the clean coal samples shows that the ash impurity reductions ranged from 37% to 80% (
Proximate and ultimate analysis of the autoclave-reacted samples (Table 13) indicates that the oxygen content reductions of the autoclave-reacted coal residues relative to raw coals were 24%, 15%, and 8% for lignite, subbituminous, and bituminous coals, respectively (
Of the 90 g of starting coal sample placed in the furnace, the recovered carbonized residues obtained for each coal were 44 g for lignite, 49 g for subbituminous coal, 50 g for bituminous coal, and 74 g for anthracite. Thus, the yield of carbonized residue was 49% for lignite, 54% for subbituminous, 56% for bituminous, and 82% for anthracite coals, respectively. Representative photos of the carbonized residues are shown in
Proximate analysis of the carbonized residues (Table 14) shows that the residual VM content was in the range 0.7-1.5 wt % and the corresponding FC content ranged from 89 wt % to 95 wt %, which is a significant improvement over the corresponding raw coal samples (Table 10). The ash content ranges from about 3 to 10 wt %. Ultimate analysis results show trace to minor amounts of N and S. Because of incomplete combustion of the sample in the elemental analysis instrument, the carbon content from ultimate analysis is lower than expected. Based on the proximate analysis, the carbon content should be greater than 90-95 wt %, and a more accurate oxygen content should be in the range of 0-4 wt % instead of 6-19 wt %, as shown in Table 14. The limitation of the ASTM method for doing proximate and ultimate analysis for graphite samples is being pursued as a separate investigation.
ATR-FTIR spectra of the carbonized residues (
The Raman spectra (
X-ray diffraction (XRD) analysis was performed on the raw, cleaned, autoclaved, and carbonized coal samples and compared to a graphite reference. The peak intensity/height of the graphite reference is scaled to 15% of the original height for the purpose of comparison with the diffractograms derived from the coal samples. The XRD diffractograms (
Proximate analysis of the graphitized samples (Table 15) shows 99+wt % FC, ˜0.8 wt % VM, and residual ash content that was BDL or zero, except for the subbituminous coal-derived graphite sample that had 0.02 wt % ash. Ultimate analysis results show negligible to trace amounts of N and S. Because of incomplete combustion of the sample in the elemental analysis instrument, the carbon content from ultimate analysis is lower than expected. Based on the proximate analysis, the content should be 99+wt %, and a more accurate oxygen content should be in the range 0-0.5 wt %, instead of 10-18 wt %, as shown in Table 15. The limitation of the ASTM method for proximate and ultimate analysis of graphite samples is under development as a separate study.
The ATR-FTIR spectra (
Raman spectra of the coal-derived graphite samples are shown in
SEM was performed on the coal-derived graphite samples as well as on reference flake graphite to gain insights into the morphological features and potential heterogeneity of the graphitized samples. The big finding from SEM morphology is the observation of a potential new graphite structure from lignite and subbituminous coals, which we call “croissant graphite.” Needle-like graphite structures are also observed. These needle and croissant graphite structures were not seen in the carbonized coal samples. Thus, we believe these are formed under graphitization conditions and so are graphite structures. The observations described below were made on samples with both the first set of preprocessing conditions designated by prefix C- and the second set with prefix CA- designation.
Representative images of the reference flake graphite are shown in
The morphological features of lignite-derived graphite samples are shown in
The images from subbituminous-derived graphite are displayed in
Bituminous coal-derived graphite SEM morphologies are presented in
Anthracite-derived graphite morphologies are shown in
XRD analysis of graphite made from the C-set of samples was compared to the results obtained on a reference flake graphite sample. A silicon internal standard was used to correct for potential instrument-induced shifts on the peaks in the diffractograms. To facilitate comparison of peak positions, the diffractogram for the reference graphite was scaled to match the tallest coal-derived graphite peak observed for anthracite-derived graphite. Two major observations can be made from the diffractograms in
To evaluate the improvements on coal graphitizability and quality of coal-derived graphite, XRD analysis was performed on graphite made from the CA-set of samples and compared to results from the C-set of samples. In general, the results (
Quantitative graphitization parameters are presented in Table 16 for the C-set and CA-set of samples. The graphite reference (flake graphite) was determined to be highly crystalline, with essentially 100% DoG, while the coal-derived graphite samples contain two possible graphite-1 and graphite-2 phases. In general, the error margin for the DoGs reported in Table 16 is ±3%. The results of the coal-derived graphite samples are very promising especially for a process that has not been fully optimized. As illustrated by the peak intensities in
The needle-like and croissant-shaped graphite particles observed in SEM analysis are most likely among the particle population that makes up the higher-crystalline graphite-2 phase, while the larger isotropic particles are lower-order or disordered graphite particles (graphite-1) at varying stages of graphitization. The presence of the two phases in the coal-derived graphite samples also illustrates the varying degrees of graphitization achieved in each case. These results further indicate that additional optimization of graphitization conditions is needed to improve the crystallinity and long-range order in bulk coal-derived graphite samples. However, for the purpose of making graphene from coal-derived graphite by exfoliation, it may not be necessary to achieve perfect long-range ordered crystals because the turbostratic graphene layers would be easier to exfoliate. These results demonstrate an exciting possibility and opportunity to be able to make high-quality graphite from coals of all ranks.
1Degree of graphitization.
The four-step process that constitutes the proposed method for preparing high-quality graphite from carbon ores is based on scientifically sound chemical principles. Removal of ash and other impurities greatly reduces the chances of imperfections in the graphite crystal lattices due to the presence of inorganic species. Heteroatoms such as oxygen, sulfur, and nitrogen tend to form bridges that promote polymerization and/or formation isotropic char which renders the material nongraphitizable or significantly reduces the quality of the resulting graphite. Carbonization of the upgraded coal/coal waste precursors removes the volatile matter and concentrates the graphitic carbon content at 1000° C. Additional heat treatment at 1600° C. prior to graphitization at 2800° C. helps to further strengthen the graphitic carbon domains which are ordered at graphitization temperatures to high quality, highly crystalline graphite.
The new graphite structure revealed by FESEM analysis of the graphitized materials shows oval or spherical morphologies and texture that looks like croissant, hence, the name croissant graphite. The fact that these structures were observed in graphite samples prepared from upgraded lignite, subbituminous, and bituminous coals, and not in anthracite, suggest that coal ranks lower than anthracite may have the possibility for structural rearrangement that is not available in anthracite. Although the mechanisms of formation of the croissant graphite structures are still under investigation, initial examination of several particle morphologies suggests the mode of formation might involve spiral-winding or folding of 2D graphene sheets into ribbon-like structures and to croissant graphite structures. X-ray diffraction (XRD) analysis shows that croissant graphite particles possess a high degree of crystallinity that is comparable to that of natural flake graphite. However, XRD results also show a lower order graphite phase that suggests that long-range ordering of the graphitic domains can be further improved to increase the quantity of high-quality graphite from coal-derived precursors.
For LIB applications, the graphite material used to fabricate battery anodes has stringent requirements such as a high carbon purity of about 99.95% and small, spherical particles. To satisfy these requirements, natural graphite from graphite mines often has to be purified and spheroidized to improve performance. Because of the texture and spheroidal shapes of croissant graphite particles, it is expected that these types of particles will be useful for the fabrication of efficient lithium-ion batteries for electric vehicle (EV) and energy storage applications. Additionally, such high-quality graphite will be a good precursor for solid high-value carbon products such as graphene.
A method for preparing high-quality graphite from carbon ores and carbonaceous feedstocks has been developed. The carbon ores materials used as feedstocks in this study were primarily coal or coal wastes. This method comprises four steps, including removal of ash and impurities, heteroatoms reduction reactions, carbonization, and graphitization. Analysis of the graphitized materials by field emission scanning electron microscopy (FESEM) revealed a new graphite structure currently ascribed the name “croissant graphite” based on the observed morphological texture and shape. These structures were observed in graphite samples prepared from upgraded lignite, subbituminous, and bituminous coals. Anthracite samples that underwent the same upgrading treatment did not show any particles that resemble croissant graphite particles morphologies. X-ray diffraction (XRD) analysis shows that croissant graphite particles possess a high degree of crystallinity that is comparable to that of natural flake graphite. Although the mechanisms of formation of the croissant graphite structures are still under investigation, initial examination of several particle morphologies suggests the mode of formation might involve spiral-winding or folding of 2D graphene sheets into ribbon-like structures and to croissant graphite structures. Because of the texture and spheroidal shapes of croissant graphite particles, it is expected that these types of particles will be useful for the fabrication of efficient lithium-ion batteries for electric vehicle (EV) and energy storage applications as well as preparation of high-value solid carbon products such as graphene.
The terms and expressions that have been employed are used as terms of description and not of limitation, and there is no intention in the use of such terms and expressions of excluding any equivalents of the features shown and described or portions thereof, but it is recognized that various modifications are possible within the scope of the aspects of the present invention. Thus, it should be understood that although the present invention has been specifically disclosed by specific aspects and optional features, modification and variation of the concepts herein disclosed may be resorted to by those of ordinary skill in the art, and that such modifications and variations are considered to be within the scope of aspects of the present invention.
The following exemplary aspects are provided, the numbering of which is not to be construed as designating levels of importance:
Aspect 1 provides a method of carbonizing an upgraded coal, the method comprising:
heating the upgraded coal in an inert environment, to form a carbonized upgraded coal.
Aspect 2 provides the method of Aspect 1, wherein the inert environment comprises argon.
Aspect 3 provides the method of any one of Aspects 1-2, wherein the heating comprises heating to a temperature of 500° C. to 2,000° C. for a duration of 10 min to 6 h.
Aspect 4 provides the method of any one of Aspects 1-3, wherein the heating comprises heating to a temperature of 550° C. to 1,650° C. for a duration of 20 min to 4 h.
Aspect 5 provides the method of any one of Aspects 1-4, wherein the heating comprises heating to a first temperature for a first duration, wherein the first temperature is in the range of 400° C. to 1,000° C., and wherein the first duration is in the range of 10 min to 4 h.
Aspect 6 provides the method of Aspect 5, wherein the first temperature is in the range of 500° C. to 700° C., and wherein the first duration is in the range of 15 min to 1 h.
Aspect 7 provides the method of any one of Aspects 5-6, wherein the heating comprises heating to the first temperature at a rate of 1° C./min to 30° C./min.
Aspect 8 provides the method of any one of Aspects 5-7, wherein the heating comprises heating to the first temperature at a rate of 5° C./min to 15° C./min.
Aspect 9 provides the method of any one of Aspects 5-8, wherein the heating further comprises heating to a second temperature higher than the first temperature for a second duration, wherein the second temperature is in the range of 600° C. to 1,500° C., and wherein the second duration is in the range of 10 min to 4 h.
Aspect 10 provides the method of Aspect 9, wherein the second temperature is in the range of 900° C. to 1100° C., and wherein the second duration is in the range of 15 min to 1 h.
Aspect 11 provides the method of any one of Aspects 9-10, wherein the heating comprises heating from the first temperature to the second temperature at a rate of 1° C./min to 30° C./min.
Aspect 12 provides the method of any one of Aspects 9-11, wherein the heating comprises heating from the first temperature to the second temperature at a rate of 5° C./min to 15° C./min.
Aspect 13 provides the method of any one of Aspects 9-12, wherein the method further comprises heating to a third temperature higher than the second temperature for a third duration, wherein the third temperature is in the range of 1,000° C. to 2,000° C., and wherein the third duration is in the range of 30 min to 4 h.
Aspect 14 provides the method of Aspect 13, wherein the third temperature is in the range of 1,500° C. to 1,600° C., and wherein the third duration is in the range of 1 h to 3 h.
Aspect 15 provides the method of any one of Aspects 13-14, wherein the heating comprises heating from the second temperature to the third temperature at a rate of 1° C./min to 30° C./min.
Aspect 16 provides the method of any one of Aspects 13-15, wherein the heating comprises heating from the second temperature to the third temperature at a rate of 5° C./min to 15° C./min.
Aspect 17 provides the method of any one of Aspects 1-16, wherein the carbonizing further comprises allowing the temperature to cool to 0° C. to 40° C.
Aspect 18 provides the method of any one of Aspects 1-17, wherein the carbonizing further comprises allowing the temperature to cool (e.g., under inert conditions) at a rate of 1° C./min to 50° C./min.
Aspect 19 provides the method of any one of Aspects 1-18, wherein the carbonizing further comprises allowing the temperature to cool at a rate of 10° C./min to 30° C./min.
Aspect 20 provides the method of any one of Aspects 1-19, wherein the heating comprises:
Aspect 21 provides the method of any one of Aspects 1-20, wherein the upgraded coal is an upgraded lignite coal, and upgraded subbituminous coal, an upgraded bituminous coal, an upgraded anthracite coal, or a combination thereof.
Aspect 22 provides the method of any one of Aspects 1-21, wherein the upgraded coal is an upgraded lignite coal, an upgraded subbituminous coal, or a combination thereof.
Aspect 23 provides the method of any one of Aspects 1-22, wherein the yield of the carbonized upgraded coal from the upgraded coal is 30% to 99%.
Aspect 24 provides the method of any one of Aspects 1-23, wherein the yield of the carbonized upgraded coal from the upgraded coal is 40% to 60%.
Aspect 25 provides the method of any one of Aspects 1-24, wherein the carbonized upgraded coal has an ash content of 1 wt % to 20 wt %.
Aspect 26 provides the method of any one of Aspects 1-25, wherein the carbonized upgraded coal has an ash content of 2 wt % to 12 wt %.
Aspect 27 provides the method of any one of Aspects 1-26, wherein the carbonized upgraded coal has a fixed carbon (FC) content of 80 wt % to 99 wt %.
Aspect 28 provides the method of any one of Aspects 1-27, wherein the carbonized upgraded coal has a fixed carbon (FC) content of 85 wt % to 98 wt %.
Aspect 29 provides the method of any one of Aspects 1-28, wherein the carbonized upgraded coal comprises graphitic carbon and non-graphitic carbon.
Aspect 30 provides the method of any one of Aspects 1-29, wherein the upgraded coal comprises:
Aspect 31 provides the method of any one of Aspects 1-30, further comprising forming the upgraded coal.
Aspect 32 provides the method of Aspect 31, wherein forming the upgraded coal comprises
Aspect 33 provides the method of Aspect 32, wherein the coal that is cleaned is a crushed coal, a particulate coal, a coal waste (e.g., weathered overburden, underburden, coal fines, and/or coal processing reject materials), or a combination thereof.
Aspect 34 provides the method of Aspect 33, wherein the crushed or particulate coal has a largest dimension of 25 mm or less.
Aspect 35 provides the method of any one of Aspects 33-34, wherein the crushed or particulate coal has a largest dimension of 1 micron to 25 mm.
Aspect 36 provides the method of any one of Aspects 33-35, wherein the crushed or particulate coal has a largest dimension of 1 micron to 10 mm.
Aspect 37 provides the method of any one of Aspects 32-36, wherein the cleaning of the coal comprises cleaning the coal with a mineral acid, cleaning the coal with a base, physically cleaning the coal, or a combination thereof.
Aspect 38 provides the method of any one of Aspects 32-37, wherein the cleaning of the coal comprises cleaning the coal with a base.
Aspect 39 provides the method of any one of Aspects 32-38, wherein the cleaning of the coal comprises physically cleaning the coal.
Aspect 40 provides the method of Aspect 39, wherein the physical cleaning comprises suspending the coal in an aqueous solution.
Aspect 41 provides the method of any one of Aspects 39-40, wherein the aqueous solution comprises a cesium chloride solution.
Aspect 42 provides the method of any one of Aspects 39-41, wherein the aqueous solution has a specific gravity of 1-2.
Aspect 43 provides the method of any one of Aspects 39-42, wherein the aqueous solution has a specific gravity of 1.4 to 1.6.
Aspect 44 provides the method of any one of Aspects 32-43, wherein the cleaning of the coal comprises cleaning the coal with a mineral acid.
Aspect 45 provides the method of Aspect 44, wherein the cleaning with the mineral acid removes one or more inorganic elements, thereby reducing the ash content of the coal.
Aspect 46 provides the method of any one of Aspects 44-45, wherein the mineral acid comprises phosphoric acid, sulfuric acid, boric acid, hydrofluoric acid, hydrobromic acid, perchloric acid, hydrochloric acid, nitric acid, or a combination thereof.
Aspect 47 provides the method of any one of Aspects 44-46, wherein the mineral acid comprises hydrochloric acid, nitric acid, or a combination thereof.
Aspect 48 provides the method of any one of Aspects 44-47, wherein the mineral acid comprises hydrochloric acid.
Aspect 49 provides the method of any one of Aspects 44-48, wherein the mineral acid comprises nitric acid.
Aspect 50 provides the method of any one of Aspects 44-49, wherein the mineral acid is 0.1 M to 10 M.
Aspect 51 provides the method of any one of Aspects 44-50, wherein the mineral acid is 1 M to 5 M.
Aspect 52 provides the method of any one of Aspects 44-51, wherein the mineral acid is 1 M to 1.5 M.
Aspect 53 provides the method of any one of Aspects 44-52, wherein a ratio of a volume of the mineral acid to a weight of the coal is 1:10 to 10:1.
Aspect 54 provides the method of any one of Aspects 44-53, wherein a ratio of a volume of the mineral acid to a weight of the coal is 2:1 to 4:1.
Aspect 55 provides the method of any one of Aspects 44-54, wherein the coal is cleaned with the mineral acid at a temperature of 30° C. to 100° C.
Aspect 56 provides the method of any one of Aspects 44-55, wherein the coal is cleaned with the mineral acid at a temperature of 60° C. to 80° C.
Aspect 57 provides the method of any one of Aspects 44-56, wherein the coal is cleaned with the mineral acid for a duration of 1 h to 72 h.
Aspect 58 provides the method of any one of Aspects 44-57, wherein the coal is cleaned with the mineral acid for a duration of 12 h to 36 h.
Aspect 59 provides the method of any one of Aspects 44-58, wherein the coal is cleaned with the mineral acid at atmospheric pressure.
Aspect 60 provides the method of any one of Aspects 44-59, wherein the method further comprises washing the cleaned coal residue with an aqueous liquid after the acid washing to wash the acid from the cleaned coal residue.
Aspect 61 provides the method of any one of Aspects 32-60, wherein the method further comprises drying the cleaned coal residue to remove water therefrom.
Aspect 62 provides the method of any one of Aspects 32-61, wherein the method further comprises crushing the cleaned coal residue to a smaller size than the coal prior to cleaning, wherein the smaller size comprises a largest dimension of 500 microns or less.
Aspect 63 provides the method of Aspect 62, wherein the smaller size comprises a largest dimension of 1 micron to 100 microns.
Aspect 64 provides the method of any one of Aspects 32-63, wherein the reacting of the cleaned coal residue with the oxidizable inorganic metallic agent is performed.
Aspect 65 provides the method of Aspect 64, wherein the reacting of the cleaned coal residue with the oxidizable inorganic metallic agent removes heteroatoms therefrom.
Aspect 66 provides the method of Aspect 65, wherein the heteroatoms comprise oxygen, sulfur, or a combination thereof.
Aspect 67 provides the method of any one of Aspects 64-66, wherein the reacting of the cleaned coal residue with the oxidizable inorganic metallic agent is performed in an autoclave.
Aspect 68 provides the method of any one of Aspects 64-67, wherein the oxidizable inorganic metallic agent comprises a salt comprising iron(II), cerium(III), manganese(II), cobalt(II), chromium(III), copper(I), tin(II), or a combination thereof.
Aspect 69 provides the method of any one of Aspects 64-68, wherein the oxidizable inorganic metallic agent comprises iron sulfate or a hydrate thereof.
Aspect 70 provides the method of any one of Aspects 64-69, wherein the oxidizable inorganic metallic agent comprises iron (II) sulfate heptahydrate (FeSO4.7H2O).
Aspect 71 provides the method of any one of Aspects 64-70, wherein the oxidizable inorganic metallic agent comprises iron chloride or a hydrate thereof.
Aspect 72 provides the method of any one of Aspects 64-71, wherein the oxidizable inorganic metallic agent comprises iron (II) chloride tetrahydrate (FeCl.4H2O).
Aspect 73 provides the method of any one of Aspects 64-72, wherein the reaction of the cleaned coal residue with the oxidizable inorganic metallic agent is performed at 100° C. to 500° C.
Aspect 74 provides the method of any one of Aspects 64-73, wherein the reaction of the cleaned coal residue with the oxidizable inorganic metallic agent is performed at 250° C. to 350° C.
Aspect 75 provides the method of any one of Aspects 64-74, wherein the reaction of the cleaned coal residue with the oxidizable inorganic metallic agent is performed in an aqueous solvent.
Aspect 76 provides the method of any one of Aspects 64-75, wherein the reaction of the cleaned coal residue with the oxidizable inorganic metallic agent is performed under an inert gas.
Aspect 77 provides the method of any one of Aspects 64-76, wherein the reaction of the cleaned coal residue with the oxidizable inorganic metallic agent is performed under argon.
Aspect 78 provides the method of any one of Aspects 64-77, wherein the reaction of the cleaned coal residue with the oxidizable inorganic metallic agent is performed in an environment that has been evacuated and flushed with an inert gas one or more times.
Aspect 79 provides the method of any one of Aspects 64-78, wherein the reaction of the cleaned coal residue with the oxidizable inorganic metallic agent is performed in the substantial absence of oxygen.
Aspect 80 provides the method of any one of Aspects 64-79, wherein the reaction of the cleaned coal residue with the oxidizable inorganic metallic agent is performed for a duration of 30 min to 5 h.
Aspect 81 provides the method of any one of Aspects 64-80, wherein the reaction of the cleaned coal residue with the oxidizable inorganic metallic agent is performed for a duration of 1 h to 3 h.
Aspect 82 provides the method of any one of Aspects 64-81, wherein after the reaction of the cleaned coal residue with the oxidizable inorganic metallic agent, the reaction mixture is actively or passively cooled to room temperature.
Aspect 83 provides the method of any one of Aspects 64-82, wherein after the reaction of the cleaned coal residue with the oxidizable inorganic metallic agent, the cleaned coal residue is washed with water one or more times.
Aspect 84 provides the method of any one of Aspects 64-83, wherein after the reaction of the cleaned coal residue with the oxidizable inorganic metallic agent, the cleaned coal residue is dried to remove water therefrom.
Aspect 85 provides the method of any one of Aspects 32-84, wherein the reacting of the cleaned coal residue with the reducing agent is performed.
Aspect 86 provides the method of Aspect 85, wherein the reacting of the cleaned coal residue with the reducing agent removes organic functional groups from the cleaned coal residue.
Aspect 87 provides the method of Aspect 86, wherein the organic functional groups comprise carboxylic acids, carbonyl groups, ethers, aliphatic groups, or a combination thereof.
Aspect 88 provides the method of any one of Aspects 85-87, wherein the reacting of the cleaned coal residue with the reducing agent reduces C═O groups in the cleaned coal residue.
Aspect 89 provides the method of any one of Aspects 85-88, wherein the reducing agent comprises lithium aluminum hydride, sodium borohydride, diborane, 9-BBN, aluminum hydride, lithium borohydride, diisobutylaluminum hydride, or a combination thereof.
Aspect 90 provides the method of any one of Aspects 85-89, wherein the reducing agent comprises lithium aluminum hydride (LAH).
Aspect 91 provides the method of any one of Aspects 85-90, wherein the reacting of the cleaned coal residue with the reducing agent is conducted at 0° C. to 50° C.
Aspect 92 provides the method of any one of Aspects 85-91, wherein the reacting of the cleaned coal residue with the reducing agent is conducted at room temperature.
Aspect 93 provides the method of any one of Aspects 85-92, wherein the reacting of the cleaned coal residue with the reducing agent is conducted for a duration of 1 min to 24 h.
Aspect 94 provides the method of any one of Aspects 85-93, wherein the reacting of the cleaned coal residue with the reducing agent is conducted for a duration of 10 min to 30 min.
Aspect 95 provides the method of any one of Aspects 85-94, wherein the reacting of the cleaned coal residue with the reducing agent is performed in an organic solvent.
Aspect 96 provides the method of any one of Aspects 85-95, wherein the reacting of the cleaned coal residue with the reducing agent is performed in diethylether.
Aspect 97 provides the method of any one of Aspects 85-96, further comprising working up the product of the reacting of the cleaned coal residue with the reducing agent with water.
Aspect 98 provides the method of any one of Aspects 85-97, further comprising drying the cleaned coal residue after performing the reacting of the cleaned coal residue with the reducing agent.
Aspect 99 provides the method of any one of Aspects 32-98, wherein both the reacting of the cleaned coal residue with the oxidizable inorganic metallic agent and the reacting of the cleaned coal residue with the reducing agent are performed.
Aspect 100 provides the method of Aspect 99, wherein the reacting of the cleaned coal residue with the oxidizable inorganic metallic agent is performed before the reacting of the cleaned coal residue with the reducing agent.
Aspect 101 provides the method of any one of Aspects 99-100, wherein the reacting of the cleaned coal residue with the oxidizable inorganic metallic agent is performed after the reacting of the cleaned coal residue with the reducing agent.
Aspect 102 provides the method of any one of Aspects 32-101, wherein the upgraded coal comprises an ash content of less than 5 wt %.
Aspect 103 provides the method of any one of Aspects 32-102, wherein the upgraded coal comprises an ash content of 0.5 to 2 wt %.
Aspect 104 provides the method of any one of Aspects 32-103, wherein the upgraded coal comprises an ash content that is 4 wt % to 15 wt % lower than an ash content of the coal prior to the cleaning.
Aspect 105 provides the method of any one of Aspects 32-104, wherein the upgraded coal comprises an oxygen content that is lower than an oxygen content of the coal prior to the cleaning.
Aspect 106 provides the method of any one of Aspects 32-105, wherein the upgraded coal comprises 1% to 50% less oxygen concentration than the coal prior to the cleaning.
Aspect 107 provides the method of any one of Aspects 32-106, wherein the upgraded coal comprises 15% to 25% less oxygen concentration than the coal prior to the cleaning.
Aspect 108 provides the method of any one of Aspects 32-107, wherein the upgraded coal comprises an oxygen concentration of 10 wt % to 25 wt %.
Aspect 109 provides the method of any one of Aspects 32-108, wherein the upgraded coal comprises 1% to 30% higher carbon concentration than the coal prior to the cleaning.
Aspect 110 provides the method of any one of Aspects 32-109, wherein the upgraded coal comprises 5% to 15% higher carbon concentration than the coal prior to the cleaning.
Aspect 111 provides the method of any one of Aspects 32-110, wherein the upgraded coal comprises a carbon concentration of 40 wt % to 75 wt %.
Aspect 112 provides the method of any one of Aspects 32-111, wherein the method comprises:
Aspect 113 provides a method of carbonizing an upgraded coal, the method comprising:
Aspect 114 provides a carbonized upgraded coal formed by the method of any one of Aspects 1-113.
Aspect 115 provides a carbonized upgraded coal comprising:
Aspect 116 provides the method of any one of Aspects 1-113, wherein the method is a method of forming graphite, the method further comprising:
Aspect 117 provides the method of Aspect 116, wherein the graphitizing comprises heating the carbonized upgraded coal in an inert environment, to form the graphite.
Aspect 118 provides the method of Aspect 117, wherein the inert environment comprises argon.
Aspect 119 provides the method of any one of Aspects 117-118, wherein the heating comprises heating to a graphitization temperature in the range of 2500° C. to 3500° C. for a graphitization duration of 10 min to 10 h.
Aspect 120 provides the method of any one of Aspects 117-119, wherein the heating comprises heating to a graphitization temperature in the range of 2700° C. to 3000° C. for a duration of 30 min to 3 h.
Aspect 121 provides the method of any one of Aspects 119-120, wherein the heating comprises
Aspect 122 provides the method of Aspect 121, wherein the temperature below the graphitization temperature is 0° C. to 50° C.
Aspect 123 provides the method of any one of Aspects 121-122, wherein the temperature below the graphitization temperature is 0° C. to 1000° C.
Aspect 124 provides the method of any one of Aspects 117-123, wherein the heating comprises heating to a first graphitization temperature for a first graphitization duration, wherein the first graphitization temperature is in the range of 700° C. to 1700° C., and wherein the first graphitization duration is in the range of 0.01 s to 4 h.
Aspect 125 provides the method of Aspect 124, wherein the first graphitization temperature is in the range of 1000° C. to 1500° C., and wherein the first graphitization duration is in the range of 0.1 s to 10 min.
Aspect 126 provides the method of any one of Aspects 124-125, wherein the heating comprises heating to the first graphitization temperature at a rate of 5° C./min to 100° C./min.
Aspect 127 provides the method of any one of Aspects 124-126, wherein the heating comprises heating to the first graphitization temperature at a rate of 40° C./min to 80° C./min.
Aspect 128 provides the method of any one of Aspects 124-127, wherein the heating further comprises heating to a second graphitization temperature higher than the first graphitization temperature for a second graphitization duration, wherein the second graphitization temperature is in the range of 1500° C. to 3000° C., and wherein the second graphitization duration is in the range of 0.01 s to 4 h.
Aspect 129 provides the method of Aspect 128, wherein the second graphitization temperature is in the range of 2200° C. to 2800° C., and wherein the second graphitization duration is in the range of 0.1 s to 10 min.
Aspect 130 provides the method of any one of Aspects 128-129, wherein the heating comprises heating from the first graphitization temperature to the second graphitization temperature at a lower rate than heating to the first graphitization temperature.
Aspect 131 provides the method of any one of Aspects 128-130, wherein the heating comprises heating from the first graphitization temperature to the second graphitization temperature at a rate of 1° C./min to 50° C./min.
Aspect 132 provides the method of any one of Aspects 128-131, wherein the heating comprises heating from the first graphitization temperature to the second graphitization temperature at a rate of 10° C./min to 30° C./min.
Aspect 133 provides the method of any one of Aspects 128-132, wherein the heating further comprises heating to a third graphitization temperature higher than the second graphitization temperature for a third graphitization duration, wherein the third graphitization temperature is in the range of 2500° C. to 3500° C., and wherein the third graphitization duration is in the range of 0.01 s to 4 h.
Aspect 134 provides the method of Aspect 133, wherein the third graphitization temperature is in the range of 2700° C. to 3000° C., and wherein the third graphitization duration is in the range of 30 min to 3 h.
Aspect 135 provides the method of any one of Aspects 133-134, wherein the heating comprises heating from the second graphitization temperature to the third graphitization temperature at a lower rate than heating from the first graphitization temperature to the second graphitization temperature.
Aspect 136 provides the method of any one of Aspects 133-135, wherein the heating comprises heating from the second graphitization temperature to the third graphitization temperature at a rate of 1° C./min to 30° C./min.
Aspect 137 provides the method of any one of Aspects 133-136, wherein the heating comprises heating from the first graphitization temperature to the third graphitization temperature at a rate of 2° C./min to 20° C./min.
Aspect 138 provides the method of any one of Aspects 117-137, wherein the method further comprises allowing the graphite to cool to 0° C. to 40° C.
Aspect 139 provides the method of any one of Aspects 117-138, wherein the method further comprises allowing the graphite to cool (e.g., under inert conditions) at a rate of 1° C./min to 50° C./min.
Aspect 140 provides the method of any one of Aspects 117-139, wherein the method further comprises allowing the graphite to cool at a rate of 10° C./min to 30° C./min.
Aspect 141 provides the method of any one of Aspects 117-140, wherein the heating comprises
Aspect 142 provides the method of any one of Aspects 116-141, wherein the graphite has a moisture content of about 0 wt %.
Aspect 143 provides the method of any one of Aspects 116-142, wherein the graphite has a moisture content of 0 wt % to 0.03 wt %.
Aspect 144 provides the method of any one of Aspects 116-143, wherein the graphite has an ash content of 0 wt % to 2 wt %.
Aspect 145 provides the method of any one of Aspects 116-144, wherein the graphite has an ash content of 0.0001 wt % to 0.03 wt %.
Aspect 146 provides the method of any one of Aspects 116-145, wherein the graphite has a fixed carbon (FC) content of 98 wt % to 100 wt %.
Aspect 147 provides the method of any one of Aspects 116-146, wherein the graphite has a fixed carbon (FC) content of 99 wt % to 99.9999 wt %.
Aspect 148 provides the method of any one of Aspects 116-147, wherein the graphite has a volatile matter (VM) content of 0.01 wt % to 2 wt %.
Aspect 149 provides the method of any one of Aspects 116-148, wherein the graphite has a volatile matter (VM) content of 0.1 wt % to 1.2 wt %.
Aspect 150 provides the method of any one of Aspects 116-149, wherein the graphite has an oxygen concentration of 0 wt % to 2 wt %.
Aspect 151 provides the method of any one of Aspects 116-150, wherein the graphite has an oxygen concentration of 0.001 wt % to 0.5 wt %.
Aspect 152 provides the method of any one of Aspects 116-151, wherein the graphite has a nitrogen concentration of 0 wt % to 2 wt %.
Aspect 153 provides the method of any one of Aspects 116-152, wherein the graphite has a nitrogen concentration of 0.001 wt % to 0.5 wt %.
Aspect 154 provides the method of any one of Aspects 116-153, wherein the graphite has a sulfur concentration of 0 wt % to 2 wt %.
Aspect 155 provides the method of any one of Aspects 116-154, wherein the graphite has a sulfur concentration of 0.001 wt % to 0.5 wt %.
Aspect 156 provides the method of any one of Aspects 116-155, wherein the graphite has a heteroatom content of 0 wt % to 2 wt %.
Aspect 157 provides the method of any one of Aspects 116-156, wherein the graphite comprises croissant graphite, needle-like graphite, isotropic blocky graphite, flake graphite, or a combination thereof.
Aspect 158 provides the method of any one of Aspects 116-157, wherein the graphite comprises croissant graphite that comprises a croissant-like texture and shape.
Aspect 159 provides the method of any one of Aspects 116-158, wherein the graphite comprises croissant graphite that comprises 2D-graphene sheets spiral-wound or folded into ribbon-like structures.
Aspect 160 provides the method of any one of Aspects 116-159, wherein the croissant graphite comprises crystallinity comparable to that of natural flake graphite as measured by XRD.
Aspect 161 provides a method of forming graphite, the method comprising:
Aspect 162 provides a method of forming graphite, the method comprising:
Aspect 163 provides a method of forming graphite, the method comprising:
Aspect 164 provides a method of forming graphite, the method comprising:
Aspect 165 provides a method of forming graphite, the method comprising:
Aspect 166 provides a method of forming graphite, the method comprising:
Aspect 167 provides a graphite formed from the method of any one of Aspects 116-166.
Aspect 168 provides a graphite comprising:
Aspect 169 provides a graphite comprising:
Aspect 170 provides an electrochemical cell comprising:
Aspect 171 provides an electrochemical cell comprising:
Aspect 173 provides a lithium-ion battery comprising the electrochemical cell of any one of Aspects 171-172.
Aspect 173 provides the method, carbonized upgraded coal, graphite, electrochemical cell, or lithium-ion battery of any one or any combination of Aspects 1-172 optionally configured such that all elements or options recited are available to use or select from.
This application is a continuation-in-part of, and claims the benefit of priority to, U.S. patent application Ser. No. 17/445,870 filed Aug. 25, 2021, which claims the benefit of priority to U.S. Provisional Patent Application Ser. No. 62/706,620 filed Aug. 28, 2020, the disclosures of which are incorporated herein in its entirety by reference.
This invention was made with Government support under Contract No. DE-FE0031881 awarded by the U.S. Department of Energy. The U.S. Government has certain rights in this invention.
| Number | Date | Country | |
|---|---|---|---|
| 62706620 | Aug 2020 | US |
| Number | Date | Country | |
|---|---|---|---|
| Parent | 17445870 | Aug 2021 | US |
| Child | 17931720 | US |
