SOLUTION-BASED FORMATION OF A NANOSTRUCTURED, CARBON-COATED, INORGANIC COMPOSITE

Abstract

A process for solution-based formation of a nanostructured, carbon-coated, inorganic composite includes selecting a supply of inorganic material in a solution, selecting a supply of a carbon-containing solution, and synthesizing the composite by causing the inorganic material to react in the carbon-containing solution. The synthesized composite may be conductive-carbon-coated, and may be for electrochemical applications such as battery cathodes and anodes. The selecting step may involve varying relative amounts of polar fluid, microblender and water components to synthesize a crystalline inorganic composite. There may be a step of retaining and reusing the supply of carbon-containing solution that remains after the synthesizing, and testing the supply of carbon-containing solution that remains to determine whether it can be used again. There may be steps of controlling the composite particle size and morphology and forming desired particle size as a function of the chemical composition of the carbon-containing solution.

Description

CROSS-REFERENCES TO RELATED APPLICATIONS

This application claims the benefit under 35 U.S.C. §119(e) of U.S. Provisional Patent Application Ser. No. 62/298,962, filed Feb. 23, 2016 and U.S. Provisional Patent Application Ser. No. 62/393,591, filed Sep. 12, 2016, each of which is hereby incorporated by reference in its entirety for all purposes.

TECHNICAL FIELD

The disclosure relates to the field of materials science and, more particularly, to solution-based methods of forming nanocomposites.

BACKGROUND

Lithium Ion Battery (LIB) composites are made using several conventional synthesizing methodologies, including: (i) solid-state reaction; (ii) carbothermal reduction; (iii) solution-based methods that employ hydrothermal/solvothermal, sol-gel, or co-precipitation; (iv) precipitation; and (v) emulsion drying. Each of the above methodologies has undesirable aspects that can be characterized generally as requiring relatively high cost raw materials, relatively high operating or reaction temperatures of >100° C., a relatively complex number of steps that includes a step of crushing, milling, grinding, mechanically mixing, or blending to produce the inorganic composite.

SUMMARY

The invention can be characterized as a process for solution-based formation of a nanostructured, carbon-coated, inorganic composite. That process includes selecting a supply of inorganic material in a solution, selecting a supply of a carbon-containing solution, and synthesizing the composite by causing the inorganic material to react in the carbon-containing solution.

The invention may also be characterized as the product made by the above process. The synthesized composite may be conductive-carbon-coated, and may be LFP or NMC for electrochemical applications such as cathodes. The selecting step may involve varying relative amounts of polar fluid, microblender and water components to synthesize a crystalline inorganic composite. There may be a step of retaining and reusing the supply of carbon-containing solution that remains after the synthesizing, and testing the supply of carbon-containing solution that remains to determine whether it can be used again. There may be steps of controlling the composite particle size and morphology and forming desired particle size as a function of the chemical composition of the carbon-containing solution.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a schematic block diagram illustrating the process of the invention.

FIG. 2 is a schematic block diagram that illustrates another version of the process of the invention.

FIG. 3 is a schematic block diagram that illustrates another version of the process of the invention.

FIG. 4 is a schematic diagram showing use of recycled blendstock.

FIG. 5 shows the LiFePO₄/C composite characterized using XRD and electrochemical performance.

FIG. 6 shows the LiFePO₄/C composite characterized using SEM and electrochemical performance.

FIG. 7 is a schematic diagram showing the cycling study of LiFePO₄/C material assembled into a coin cell.

FIG. 8 is a schematic diagram showing cell voltage versus lithium as a function of capacity for various C-rates.

DETAILED DESCRIPTION OF THE INVENTION

Referring to FIG. 1, an embodiment of the invention is shown at 100 and is a process for solution-based formation of a nanostructured, carbon-coated, inorganic composite. Process 100 includes at 102, selecting a supply of inorganic material in a solution, at 104, selecting a supply of a carbon-containing solution including renewable fatty acids and naturally derived alcohols and, at 106 synthesizing a nanostructured, carbon-coated, inorganic composite by, at 108, causing the supply of inorganic material to react in the presence of the carbon-containing solution.

Selecting step 102 may involve selecting a supply of the carbon-containing solution that includes a fatty acid. The selected carbon-containing solution may also include a polar fluid component, a microblender component and a water component, and each of those components are further described in co-pending U.S. patent application Ser. No. 14/318,365 (“the Co-Pending Application”), and will be described further below, after a discussion of FIGS. 1-3.

Still referring to FIG. 1, selecting step 104 may also involve varying the relative amounts of the polar fluid, microblender and water components so that synthesizing step 106 produces a crystalline inorganic composite. Synthesizing step 106 may also involve synthesizing a crystalline inorganic composite. After the synthesizing step is practiced, there remains an amount of the carbon-containing solution, which could be discarded using suitable methods. However, FIG. 2 shows an embodiment of the invention that provides an alternative to discarding the remaining amount of the carbon-containing solution.

Referring to FIG. 2, another embodiment of the invention is shown at 200, and is also a process like process 100, including selecting steps 202 and 204, like selecting steps 102 and 104 of FIG. 1, and a synthesizing step 206, like synthesizing step 106 of FIG. 1. However, unlike process 100, process 200 also includes at 208, retaining the supply of carbon-containing solution that remains after the synthesizing. Retaining step 208 may also include at 210, testing the supply of carbon-containing solution that remains to determine whether it can be used again. Such testing could including any suitable, commercially available method, including, for example, GC, GCMS, and LC. Process 200 also includes at 212, repeating the synthesizing by causing the inorganic materials to react in the presence of the retained carbon-containing solution.

Referring to FIG. 3, another embodiment of the invention is shown at 300, and is also a process like process 100, including selecting steps 302 and 304, like selecting steps 102 and 104 of FIG. 1. There is also a synthesizing step 306, like synthesizing step 106 of FIG. 1. However, synthesizing step 306 involves synthesizing a nanostructured, carbon-coated, crystalline inorganic composite.

Still referring to FIG. 3, synthesizing step 306 includes at 308, controlling the particle size and morphology of the composite. The controlling may involve, as at 310, forming desired particle size as a function of the chemical composition of the carbon-containing solution. Changes in the chemical composition of the carbon-containing solution produce changes in the particle size, morphology, and in some cases the composition of the synthesized composite.

Referring generally to FIGS. 1-3, the invention may also be characterized as a nanostructured, carbon-coated, inorganic composite formed by the above-described process. The process and the inorganic composite of the invention may have electrochemical applications, such as to synthesize a nanostructured, conductive-carbon-coated, inorganic composite that is suitable for electrochemical applications.

One of those applications could be for use as a cathode in a battery and, for that use, the process could be practiced to synthesize battery composites, such as battery-cathode or battery-anode composites. Battery-cathode composites may include Lithium Iron Phosphate (LFP)(LiFePO₄), Lithium Nickel Manganese Cobalt Oxide (NMC)(LiNiMnCoO₂), Lithium Cobalt Oxide (LCO)(LiCoO₂), Lithium Manganese Oxide (LMO)(LiMn₂O₄), and Lithium Nickel Cobalt Aluminum Oxide (NCAO)(LiNiCoAlO₂). Battery-anode composites could include Lithium Titanate (LTO)(Li₄Ti₅O₁₂).

For electrochemical applications, the selecting step 102, 202, 302 would involve selecting a supply of conductive-carbon-containing solution.

Referring generally to selecting steps 102, 202 and 302, the selected carbon-containing solution may, as noted above, also include a polar fluid component, a microblender component and a water component. A mixture of these three components is also referred to herein as a blendstock or microblend. As further described in the Co-Pending Application, the polar fluid component may include one or more polar fluids, such as alcohols like ethanol. For example, the polar fluid may include ethanol of a relatively low grade, and those low grades will also have a water component. Ethanols of a low grade have a water content of 5-20%, assuming water is the main contaminant.

The polar fluid component may involve selecting an alcohol from a group comprising (a) n-propyl alcohol, (b) iso-propyl alcohol, (c) n-butyl alcohol, a mixed alcohol formulation (e.g., ENVIROLENE®), methanol, and ethanol, and blending the alcohol and the water component to form the one or more polar fluids. Blending the alcohol and water may involve formulating the amount of water so that the amount of water comprises about 1-30% of the one or more polar fluids. Preferably, the amount of water comprises about 5-20% of the one or more polar fluids. Preferably, the alcohol component includes ethanol. ENVIROLENE® is a mixed alcohol formulation made by Standard Alcohol Company of America. Examples of suitable mixed alcohol formulations are described in U.S. Pat. No. 8,277,522 and published U.S. Patent Application No. 2013/0019519, which are hereby incorporated by reference.

The microblender component may be a fatty acid, such as one chosen from a group comprising saturated and/or unsaturated carboxylic acids and/or esters containing 14 to 24 carbons, such as oleic acid, elaidic acid, erucic acid, linoleic acid, lauric acid, myristic acid, and stearic acid. The microblender may also be a fatty acid chosen from a group comprising suitable unsaturated or saturated fatty acids.

A neutralizer may also be combined with the polar fluid, microblender and water components, and the neutralizer is chosen for its capability of neutralizing the microblender component. For example, the neutralizer may involve selecting a component of a lower pH than the microblender component. For example, if the microblender component includes an acidic component, then selecting the neutralizer may involve selecting a basic component. Preferably, the neutralizer includes an ammonia component, such as ammonium hydroxide.

EXAMPLE

An application of the process of the invention was made by synthesizing LiFePO₄/C lithium ion battery cathode materials in recyclable, reverse-micelle media. The process allows for control of particle size and morphology, lower reaction temperature, improves electrochemical performance, provides a carbon coating for improved electrical conductivity, and provides for a recyclable reaction medium.

The use of recycled blendstock is shown in FIG. 4.

General Procedure of Solution-Based Nanostructured Material Formation

An iron salt (may be Fe(II) or Fe(III); in this example FeCl₂.4H₂O was used) was dissolved in ethanol or ethanol/water mixtures at ˜0.5 mmol/mL The salt concentration affects the crystalline structure of the synthesized inorganic composite. To that solution, ˜2× by volume of blendstock was added and the mixture was heated at 60° C. for 1 hour. Separate solutions were prepared containing: (i) 85% H₃PO₄ (ammonium dihydrogen phosphate may also be used) at 1 mmol/mL in ethanol; and (ii) a lithium salt (e.g., lithium acetate, lithium acetylacetonate, lithium iodide, lithium chloride, lithium hydroxide) at 1 mmol/mL in ethanol or ethanol/water mixtures. The solutions were simultaneously added dropwise to the mixture containing the iron salt and blendstock with constant stirring, then heated to 120° C. for 2 hours, and then transferred to a Teflon® flask and heated to 250° C. for 4 hours. The flask was allowed to cool to room temperature, the resulting cake was washed with water, and allowed to dry in an oven at 120° C. for 8 hours.

The resulting solid was ground into a powder and placed in an alumina crucible and heated to 700° C. under Ar/H₂ for 4 hours to give LiFePO₄/C. The LiFePO₄/C composite was characterized using XRD, SEM, and electrochemical performance, and the results of those tests are shown in FIGS. 5 and 6.

Electrochemical Performance

The LiFePO₄/C composite was vacuum dried overnight at 100° C. and tape cast with binder and conductive additive and assembled into a coin cell with a lithium counter electrode. The cell was full charged and then discharged to 2.5 V versus Li at various C-rates. FIGS. 7-8 show respectively, a schematic diagram of the cycling study of LiFePO₄/C material assembled into a coin cell, and a schematic diagram of cell voltage versus lithium as a function of capacity for various C-rates.

The invention may also be described in the following number paragraphs.

1. A process for solution-based formation of a nanostructured, conductive-carbon-coated, inorganic, composite, cathode material, comprising:

selecting a supply of inorganic material in a solution;

selecting a supply of a conductive-carbon-containing solution; and

synthesizing a nanostructured, conductive-carbon-coated, inorganic, composite cathode material by causing the supply of inorganic material to react in the presence of the conductive-carbon-containing solution.

2. The process of 1, wherein the selecting step involves selecting a supply of the carbon-containing solution that includes a fatty acid.

3. The process of 2, wherein the selecting step involves selecting a supply of a carbon-containing solution that includes a polar fluid component, a microblender component and a water component.

4. The process of 2, wherein the synthesizing step involves synthesizing a crystalline inorganic composite.

5. The process of 4, wherein the selecting step also involves varying the relative amounts of the polar fluid, microblender and water components so that the synthesizing step produces a crystalline inorganic composite.

6. The process of 5, further including the step of retaining the supply of carbon-containing solution that remains after the synthesizing.

7. The process of 6, wherein the retaining step includes testing the supply of carbon-containing solution that remains to determine whether it can be used again.

8. The process of 7, further including the step of repeating the synthesizing by causing the inorganic materials to react in the presence of the retained carbon-containing solution.

9. The process of 1, wherein the synthesizing step includes controlling the particle size and morphology of the composite.

10. The process of 9, wherein the controlling involves forming desired particle size as a function of the chemical composition of the carbon-containing solution.

11. The process of 1, wherein the selecting step involves selecting a supply of conductive-carbon-containing solution.

12. The process of 11, wherein the synthesized composite is chosen from the group consisting of LFP, NMC, LCO, LMO, and NCA.

13. A nanostructured, conductive-carbon-coated, inorganic, composite cathode material formed from a solution-based reaction, comprising:

selecting a supply of inorganic material in a solution;

selecting a supply of a conductive-carbon-containing solution; and

synthesizing a nanostructured, conductive-carbon-coated, inorganic, composite cathode material by causing the supply of inorganic material to react in the presence of the conductive-carbon-containing solution.

14. The composite cathode material of 13, wherein the selecting step involves selecting a supply of the carbon-containing solution that includes a fatty acid.

15. The composite cathode material of 14, wherein the selecting step involves selecting a supply of a carbon-containing solution that includes a polar fluid component, a microblender component and a water component.

16. The composite cathode material of 14, wherein the synthesizing step involves synthesizing a crystalline, inorganic, composite, cathode material.

17. The composite cathode material of 16, wherein the selecting step also involves varying the relative amounts of the polar fluid, microblender and water components so that the synthesizing step produces a crystalline, inorganic, composite, cathode material.

18. The composite cathode material of 17, further including the step of retaining the supply of carbon-containing solution that remains after the synthesizing.

19. The composite cathode material of 18, wherein the retaining step includes testing the supply of carbon-containing solution that remains to determine whether it can be used again.

20. The composite cathode material of 19, further including the step of repeating the synthesizing by causing the inorganic materials to react in the presence of the retained carbon-containing solution.

21. The composite cathode material of 13, wherein the synthesizing step includes controlling the particle size and morphology of the composite cathode material.

22. The composite cathode material of 21, wherein the controlling involves forming desired particle size as a function of the chemical composition of the carbon-containing solution.

23. The composite cathode material of 13, wherein the selecting step involves selecting a supply of conductive-carbon-containing solution.

24. The composite cathode material of 23, wherein the synthesized composite cathode material is chosen from the group consisting of LFP and NMC.

In the preceding description, various aspects of claimed subject matter have been described. For purposes of explanation, specific numbers, systems and/or configurations were set forth to provide a thorough understanding of the claimed subject matter. However, it should be apparent to one skilled in the art having the benefit of this disclosure that claimed subject matter may be practiced without the specific details. In other instances, features that would be understood by one of ordinary skill were omitted and/or simplified so as not to obscure claimed subject matter. While certain features have been illustrated and/or described herein, many modifications, substitutions, changes and/or equivalents will now occur to those skilled in the art. It is, therefore, to be understood that the appended claims are intended to cover all such modifications and/or changes as fall within the true spirit of claimed subject matter.

Claims

1. A process for solution-based formation of a nanostructured, carbon-coated, inorganic composite, comprising:

selecting a supply of inorganic material in a solution;

selecting a supply of a carbon-containing solution; and

synthesizing a nanostructured, carbon-coated, inorganic composite by causing the supply of inorganic material to react in the presence of the carbon-containing solution.

2. The process of claim 1, wherein the selecting step involves selecting a supply of the carbon-containing solution that includes a fatty acid.

3. The process of claim 2, wherein the selecting step involves selecting a supply of a carbon-containing solution that includes a polar fluid component, a microblender component and a water component.

4. The process of claim 2, wherein the synthesizing step involves synthesizing a crystalline inorganic composite.

5. The process of claim 4, wherein the selecting step also involves varying the relative amounts of the polar fluid, microblender and water components so that the synthesizing step produces a crystalline inorganic composite.

6. The process of claim 5, further including the step of retaining the supply of carbon-containing solution that remains after the synthesizing.

7. The process of claim 6, wherein the retaining step includes testing the supply of carbon-containing solution that remains to determine whether it can be used again.

8. The process of claim 7, further including the step of repeating the synthesizing by causing the inorganic materials to react in the presence of the retained carbon-containing solution.

9. The process of claim 1, wherein the synthesizing step includes controlling the particle size and morphology of the composite.

10. The process of claim 9, wherein the controlling involves forming desired particle size as a function of the chemical composition of the carbon-containing solution.

11. The process of claim 1, wherein the selecting step involves selecting a supply of conductive-carbon-containing solution.

12. The process of claim 11, wherein the synthesizing produces a nanostructured, conductive-carbon-coated, inorganic composite that is suitable for electrochemical applications.

13. The process of claim 12, wherein the synthesized composite is suitable for use as a battery composite.

14. The process of claim 13, wherein the synthesized composite is chosen from the group of battery composites consisting of battery-cathode and battery-anode composites.

15. The process of claim 13, wherein the synthesized group of battery-cathode composites consisting of LFP, NMC, LMO, LCO and NCAO.

16. The process of claim 13, wherein the battery-anode composite is LTO.

17. A nanostructured, carbon-coated, inorganic composite formed from a solution-based reaction, comprising:

selecting a supply of inorganic materials in an aqueous solution;

selecting a supply of a carbon-containing solution; and

synthesizing a nanostructured, carbon-coated, inorganic composite by causing the supply of inorganic materials to react in the presence of the carbon-containing solution.

18. The composite of claim 17, wherein the selecting step involves selecting a supply of the carbon-containing solution that includes a fatty acid.

19. The composite of claim 18, wherein the selecting step involves selecting a supply of a carbon-containing solution that includes a polar fluid component, a microblender component and a water component.

20. The composite of claim 18, wherein the synthesizing step involves synthesizing a crystalline inorganic composite.

21. The composite of claim 20, wherein the selecting step also involves varying the relative amounts of the polar fluid, microblender and water components so that the synthesizing step produces a crystalline inorganic composite.

22. The composite of claim 21, further including the step of retaining the supply of carbon-containing solution that remains after the synthesizing.

23. The composite of claim 22, wherein the retaining step includes testing the supply of carbon-containing solution that remains to determine whether it can be used again.

24. The composite of claim 23, further including the step of repeating the synthesizing by causing the inorganic materials to react in the presence of the retained carbon-containing solution.

25. The composite of claim 17, wherein the synthesizing step includes controlling the particle size and morphology of the composite.

26. The composite of claim 25, wherein the controlling involves forming desired particle size as a function of the chemical composition of the carbon-containing solution.

27. The composite of claim 26, wherein the selecting step involves selecting a supply of conductive-carbon-containing solution.

28. The composite of claim 27, wherein the synthesizing produces a nanostructured, conductive-carbon-coated, inorganic composite that is suitable for electrochemical applications.

29. The composite of claim 28, wherein the synthesized composite is suitable for use in the group consisting of a battery cathode and battery anode.

30. The composite of claim 29, wherein the synthesized composite is chosen from the group consisting of LFP, NMC, LMO, LCO, NCAO, and LTO.