Patent Application
20200392014
The present disclosure relates to synthesis methods. More particularly, the present disclosure relates to systems, methods, and compositions for cubic aluminum-doped lithium lanthanum zirconium oxide.
All-solid-state batteries (“ASSBs”) have been regarded as a replacement for their liquid counterpart in terms of high volumetric energy density, safe and environmentally-benign materials, and high electrochemical stability. Up to now, the reported solid state electrolytes (“SSEs”) are based on garnets, perovskites, sulfides, and hydrides. Among them, garnet-type lithium lanthanum zirconium oxide (Li7La3Zr2O12; “LLZO”) is the most applicable one due to its high ionic conductivity, extraordinary chemical stability towards electrode materials, and wide operating voltage windows. LLZO occurs in two phases tetragonal and cubic, with the tetragonal phase being the stable room temperature form and cubic being an unquenchable high temperature polymorph. The cubic phase of LLZO (“c-LLZO”) is the desired phase as it provides a very high Li-ion conductivity while maintaining very low electronic conductivity. A dopant, such as Al or Ga, will stabilize the cubic phase at room temperature.
Numerous methods for LLZO synthesis have been reported. The original method (see Murugan, et al., “Fast Lithium Ion Conduction in Garnet-Type Li7La3Zr2O12,” Angewandte Chemie 46(41), pp. 7778-7781 (2007)) involves mechanical mixing of the oxides of La and Zr along with Li(OH) or Li2CO3 followed by calcination up to 1230° C. It was later determined (see GEIGER, et al., “Crystal Chemistry and Stability of ‘Li7La3Zr2O12’ Garnet: A Fast Lithium-Ion Conductor,” Inorganic Chemistry 50(3), pp. 1089-1097 (2011)) that during calcination, inadvertent diffusion of Al from the calcination crucibles provided Al doping that is required to stabilize the cubic form of LLZO, which is otherwise an unquenchable high temperature form of LLZO. Subsequently, Al was deliberately added to provide a controlled amount of the dopant. In all prior work, due to the high volatility of elemental Li, excess Li up to 50% is added to balance the Li loss that occurs during the high temperature calcination. An alternate method (see Jin & McGinn, “Al-doped Li7La3Zr2O12 synthesized by a polymerized complex method,” Journal of Power Sources 196(20), pp. 8683-8687 (2011)) of LLZO production is based on the Pechini process utilizes a liquid solution of La, Al, and Li nitrates, ZrOCl2 and the chelating agents ethylene glycol and citric acid. Green powder from this method is calcined at 1200° C. in order to obtain a well-crystallized c-LLZO material. Aerosol processing was first (see Yi, “Aerosol Combustion Synthesis of Nanopowders and Processing to Functional Thin Films,” Ph.D. Thesis, University of Michigan Horace H. Rackham School of Graduate Studies, 97 pages (2017)) demonstrated using flame spray pyrolysis (“FSP”) to produce a green powder that requires calcination at 1050° C. to obtain cubic LLZO.
The scalability of prior art faces challenges due to the high temperature calcination requirement and challenge to manage the Li loss. In particular, a processing temperature below the stability of common lithium nickel manganese cobalt oxide (“NMC”) cathode material phases is desirable (˜800° C.) so that co-sintering of the LLZO with cathode phase powders becomes possible. By reducing the calcination temperature to below ˜800° C., the issue of Li loss is largely avoided and the co-sintering with the common NMC cathode phases is enabled.
At least one embodiment relates to a method comprising preparation of a combustible liquid feed of metal salts comprising lanthanum precursor, lithium precursor, zirconium precursor, and aluminum precursor with a prescribed enthalpy of combustion; combusting a spray of the combustible liquid feed at a FSP temperature; and collecting of the resulting green powder whose properties enable the formation of well crystallized c-LLZO powder at a calcination temperature of 670° C.
Another embodiment relates to a method comprising preparation of a combustible liquid feed of metal salts comprising lanthanum precursor, lithium precursor, zirconium precursor, and aluminum precursor with a enthalpy of combustion known to not produce green powder with the desired low-temperature access to c-LLZO; and combusting a spray of the combustible liquid feed in the FSP apparatus modified with flame guide to provide intensification of the combustion thereby achieving the equivalent effect of a higher enthalpy solution.
Yet another embodiment relates to a method comprising preparation of an aqueous liquid feed of metal salts comprising lanthanum precursor, lithium precursor, zirconium precursor, and aluminum precursor; processing of the aqueous solution in a spray pyrolysis apparatus completing the decomposition reactions of the precursor salts to obtain a green powder comprised of oxides of La, Zr, Al and Li(OH); and calcinating of the green powder at 700° C. to obtain well crystallized c-LLZO.
This summary is illustrative only and is not intended to be in any way limiting. Other aspects, inventive features, and advantages of the devices or processes described herein will become apparent in the detailed description set forth herein, taken in conjunction with the accompanying figures, wherein like reference numerals refer to like elements.
Before turning to the figures, which illustrate certain exemplary embodiments in detail, it should be understood that the present disclosure is not limited to the details or methodology set forth in the description or illustrated in the figures. It should also be understood that the terminology used herein is for the purpose of description only and should not be regarded as limiting.
Previously published literature suggests that at least 1000° C. is required when using the method published by Eongyu Yi (Yi, “Aerosol Combustion Synthesis of Nanopowders and Processing to Functional Thin Films,” Ph.D. Thesis, University of Michigan Horace H. Rackham School of Graduate Studies, 97 pages (2017)) for production of c-LLZO. The published literature establishes that the cubic phase of LLZO (specifically, Li7La3Zr2O12) is the desired phase as it provides a very high Li ion conductivity while maintaining very low electronic conductivity. Thermodynamically, tetragonal is stable at low temperature and cubic is an unquenchable high temperature phase of LLZO. A dopant is used to stabilize the cubic phase to exist at room temperature. Previous work has shown that Al and Ga are successful at stabilizing the cubic phase of LLZO. Apart from the efficiency of being able to anneal at lower temperature (sub 1000° C., including sub 800° C.), a far more important feature is that the green-body particles could be co-sintered with active cathode phases, such as NMC811 or LCO, without requiring those materials to be subjected to the higher temperature (e.g., 1000° C.), which could destroy the required phase for those materials. Typically, temperatures of 750-850° C. are used to prepare the cathode phases, so LLZO cubic synthesis falling into this window would match thermal budgets for both materials. The co-sintering is a potential manufacturing strategy for making the cathode/solid-state electrolyte in an all solid-state battery.
As used herein, “sintering” refers to a process where powders (such as “green powder”) is heated, below the melting point, and pressed into a solid object (powder metallurgy). “Calcination” refers to heating in the presence of air or oxygen to perform solid state reaction needed to transform green powder into the desired final product. “Green-body powders” refer to the ceramic precursor powders produced by the aerosol processes which require calcination to form the target phases, typically the powder prepared for sintering.
In general, the examples provided herein utilized aerosol synthesis, namely flame spray pyrolysis (“FSP”), spray pyrolysis (“SP”), and spray drying (“SD”), as shown in
The aerosol processes utilize a dopant material. In one embodiment, dopant is selected from Al, Ga, Ta, and Ba. In one embodiment, the aerosol processes utilize an aluminum dopant and result in a material having the nominal formula Li(7-3xLa2Zr3O7Alx where x=0.25 is the nominal optimum and upon which are research is based; in certain embodiments, x=0.19-0.389. Note that data with both tetragonal and cubic phases present after and 800° C. calcination that supports the partitioning of Al. The activation energy of the dopant may impact the amount of atomic mixing that results.
In the FSP process, a combustible liquid feed containing metal salt is atomized (turned into droplet dispersion) by a gas-assisted spray nozzle. The spray is ignited by a flame, such as methane-oxygen pilot flames. The FSP process ideally utilizes flame that is continuously maintained to assure continuous combustion that also incidentally provides additional heat energy to the products of the spray combustion. Optionally, another embodiment uses a confining ceramic tube as a flame guide and provides a radiation shield that helps maintain a higher sustained flame temperature. Similar to the higher enthalpy solution (such as due to the solvent selection) resulting in an increased flame temperature in the FSP process and achieving atomic mixing, the use of a flame tube or guide provides higher boundary temperature, achieving the desired atomic mixing as seen in one experiment example described herein.
In the SP process, a non-combustible liquid feed is atomized and transported by carrier gas through a high temperature reaction zone. It has been found that either the FSP process or the SP process can be tuned to obtain atomically mixed green powders. These atomically mixed green powders can be calcined to attain the cubic-LLZO phase at lower calcination temperature than previously reported and as understood previously for general green powder resulting from LLZO formation.
SD can also be utilized as the aerosol method for formation of c-LLZO. In SD, a non-combustible liquid feed is atomized and transported by carrier gas through a low temperature drying zone.
The amount of precursor and dopant loaded into the solution prior to the formation of the green powder may vary depending on the selected aerosol process and the other selected process criteria. For example, the loading may be 3-9%. Loading is the ceramic loading (i.e., the percentage of solution weight that converts into thee solid product).
In various embodiments, aerosol technologies are optimized to deliver particles with tunable mixing extent in the green-body particles by controlling the solution composition or reaction processing temperature, as illustrated in
Experiments were performed as detailed further below. One set of experiments utilized aerosol process recipes as shown below.
For FSP, a green powder material is prepared comprised of the precursor materials for Al-doped LLZO, lanthanum, lithium, zirconium and aluminum. As an alternate chemistry to this prior art path to LLZOs, described herein are methods and compositions based on ethylhexanoic salts of lanthanum, lithium, and zirconium may be utilized. The powdered material may further include dopants, such as aluminum. The dopant is preferably selected to aid in the emergence of the c-LLZO structure at lower temperatures than without the dopant, such as by facilitating atomic mixing of the components. In one embodiment, solvents for the FSP process are selected to be high enthalpy solvents.
High enthalpy solvents may be selected for their compatibility with the aerosol process, such as flammability for FSP, as well as for their compatibility with precursors for the metals. For example, the solvent's viscosity may be negatively associated with the process (higher viscosity resulting in lower levels of atomic mixing.
As used herein, atomically mixed means the dopant (e.g., Al) and metals (e.g., La and Zr) are uniformly distributed. Atomically mixed solid particles (such as following initial conversion via FSP, SP or SD) have uniform distribution of the dopant and metals in the particles. The atomically mixed green powder is disposed to form the cubic phase LLZO at a low temperature (<1000° C.). This is in contrast to the situation where the dopant, such as Al, exists as separate particles whereby a high temperature (>1000° C.) is required to allow alumina breakdown and incorporation into the LLZO by diffusion during calcination. As described below, in one embodiment these methods and compositions can utilize alumatrane as an aluminum (dopant) source. Embodiments herein relate to combustion synthesis of aluminum doped lithium lanthanum zirconium oxide with annealing onset of cubic LLZO at 700° C. In contrast to the prior art methods, in the embodiments described herein, the cubic phase of the LLZO was observed to form at temperatures as low as 700° C. The resultant LLZO may be doped with the dopant included with the metal salt.
It is believed that the FSP parameters may be adjusted to produce a volcano-like optimum where the results begin to revert to higher and higher amounts of segregated phases of LLZO. For example, the experiments described herein include results showing the “breaking” of the desired result of c-LLZO at sub 1000° C. temperatures by altering parameters of the process, such as in SOL40, by doubling the solute concentration. It is believed that this results in the retardation of solute combustion so that the metal atoms/molecule sample a much wider range of flame conditions.
The FSP process may utilize a range of precursors. The precursors should be those deployable as atomizable solutions and the resultant solution must be compostable in the flame and, preferable, provide a stable efficient flame (pyrolysis). In particular, the precursors (and dopant) should be soluable at the 2-10% ceramic yield level.
In one embodiment, the FSP proceeds with a nozzle selected to achieve the atomic mixing. In the experimental examples described herein, the nozzle was a SHLICK MOD. 970 S 8 D4.1016/1. This is a two-fluid nozzle where fluid one is gaseous oxygen at a typical flow of 10 LPM and fluid two is the liquid solution at a corresponding flow of 8 mL/min. Additional gaseous oxygen at 25 LPM is provided as “sheath” oxygen is provided to complete combustion oxidizer needs. The burner design is one based on burners described by Pratsinis and others using an axisymmetric radial nesting of the atomized liquid, sheath flow, pilot flame array and finally quench gas nitrogen. The choice of 8 ml/min and 10 LPM flow rates are based on a starting point of the manufacturers operating instructions. It should be appreciated that these numbers may be and then optimized using combustion characteristics, primarily qualitative evaluation of flame stability and brightness indicating efficient combustion, for a particular FSP device and its operating environment. Rather than having the atomized flow be detached from pilot torch so that their combustion only starts at the point of convergence of the spray and pilots, the FSP setup used for the described experiments maintains a combusting spray which could potentially operate without pilot flame support.
Described further below are experiments using various materials prepared according to the designated methods. “SOLXX” refers to precursor solution XX as it was combusted in accordance with standard procedures. Note, for the samples indicated as following prior art protocol, the prior work indicated solutes were to be dissolved into pure ethanol however such as not found to occur, so organic acids were utilized to achieve dissolution and a clear solution. The precursor solutions are mixtures of metal salts and flammable solvents that are combusted in the FSP.
SOL33, 34, and 35 are solution formulations based on the thesis work of Eongyu Yi, which provides a reference synthesis. It should be noted that samples made from SOL33-35 provide a standard basis for comparison as these materials produced by the prior method of Yi were produced in the same facility as examples of methods described herein. One such method was utilized in the experiments utilizing SOL40. SOL40 is believed to be cheaper to make and easier to burn than prior methods such as those of Yi. SOL40 is based on ethylhexanoic acid salts of Lanthanum, Lithium, and Zirconium, along with alumatrane as the Al source.
SOL38 is a variant of SOL33 wherein the solvent was comprised of 50% propionic acid and 50% ethanol in contrast to 90% ethanol and 10% acetic acid used in SOL33. The solutes and their concentrations were same. Thus, SOL38 represents a higher enthalpy version of SOL33. The calcination of SOL38 green powder at 800° C. yielded cubic-LLZO.
During combustion synthesis, the TSI Scanning Mobility Particle Sizer was used to measure the primary particle size. These data are shown in
Table 3 shows weight loss during annealing for SOL26, 33-35, and 40. This weight loss is due to the conversion of Li2CO3 into CO2 and LiO incorporation into LZO to form LLZO. The theoretical weight loss is also shown, calculated to be 24%. The prior art method (SOL26, 33-35) closely follows the theoretical weight loss assuming all Li is in the LiCO3 form. However, as can be seen in the data, one embodiment, SOL40, falls short of the expected weight loss, possibly due to other forms of Li.
In general, hollow spheres indicated a droplet-particle synthesis pathway. In this case, the droplets diminish in size by solvent evaporation and solute precipitation, often leaving a shell of precipitant which then undergoes pyrolysis in a hot environment. Frequently, both modes are observed. The SOL33-35 samples show primarily gas-to-particle mode combustion with some lesser indication of droplet-to-particle mode. These are notably absent in SOL40 consistent with the higher temperature flame which promotes total vaporization and suppresses the droplet-to-particle morphology. These SOL33-35 materials utilized acetic acid and water mixed with ethanol to achieve the clear solutions.
In a further embodiment, a low enthalpy FSP solution, SOL127, was prepared using ethanol and nitrate salts of La, Zr, Li and aluminum. 5% water was added to facilitate dissolution of the nitrate salts. Due to the low solution enthalpy and non-flammability of the solute this sample was combusted primarily by the droplet to particle mode explained above. Sample, S132 produced by FSP processing of SOL127, produced a green powder with droplet to particle morphology but retaining the general XRD signature of all FSP samples. This sample calcined to cubic-LLZO at 800° C. The state of atomic mixing of the dopant in the LZO phase is believed to drive the positive outcome. The mode exhibited in this sample can also be characterized as Flame-Assisted-Spray-Pyrolysis and possesses many similarities to the SP experiments described below.
A nitrogen-flushed 500 ml 3 neck flask was charged with Al(OCHMeCH2CH3)3 (170 ml, Alfa A13044 lot N20A025) and stirred magnetically. Triethanolamine (89 ml, Alfa L04486 lot X31D703) was added dropwise via an additional funnel at room temperature. The addition time was 4 hours. The reaction is exothermic, keeping the reaction mixture at 25-30° C. throughout the addition. The initial clear yellow reaction turned cloudy white during the addition and re-clarified near the end. All stages are viscous. The liquid was then transferred under nitrogen to an amber bottle. 249.72 g was transferred as a 43.8% solution of alumatrane in sec-butanol. Over a period of several days, the alumatrane crystallized in the bottle. Mild heating is expected to re-dissolve the product, but this has not been tested.
A nitrogen-flushed 1000 ml 3 neck flask with overhead stirring and a distillation head was charged with propionic acid (500 ml, EMD 654833 lot 57363405 710). Lithium hydroxide hydrate (113.16 g, Alfa 13409 lot Q13D018) was added in one portion, causing an exotherm from 20-70° C. The mixture was not completely soluble, and was initially heated to 150° C. with distillation of water to try and solubilize. No clear solution was obtained, and the reaction mass was cooled overnight. The mixture was recombined with the collected distillate and re-heated. This time, a clear solution was obtained around 100° C. The reaction was heated under nitrogen to remove water. As the water distilled, lithium propionate separated as a foamy suspension. The mixture was heated to reach a final temperature of 130° C. Water distilled out between 110-120° C. The reaction was held 2 hours at 130° C. and cooled. The solid mixture was filtered. The waxy material was washed with heptane to remove most of the residual propionic acid and air-dried 24 for hours under a nitrogen flow to yield 121 g.
The collected filtrate, containing substantial product, was re-charged to a 1 L flask along with 111 g of lithium hydroxide hydrate and 200 ml fresh propionic acid. This mixture completely solubilized at 106-109° C. Water was distilled as the mixture was heated to 130° C., with precipitation of the product.
The same isolation procedure returned 231 g of lithium propionate. Additional crops totaling ca. 50 g were obtained by rotary evaporation and precipitation with heptanes. FTIR of all collected solids were superimposable. The solids were combined as a free-flowing slightly waxy powder with a faint odor of propionic acid.
TD7-752. A 2 L 4-necked flask was charged with lanthanum oxide (130.17 g, TCI L0235 lot YFJJKBS) and isobutyric acid (550 ml, Aldrich W222208 lot MKCF1895). The mixture was heated slowly with overhead mechanical stirring to ˜50° C. The reaction then began to self-heat and the water evolution caused a loss of material. After cooling, the solid mixture was re-heated to 140° C. to form a clear solution. Upon cooling, this formed a solid block. Heptane was added to disperse the solids. Filtration, washing and drying returned 211 g.
TD7-758. A 1 L 3-necked flask was charged with lanthanum oxide (65.07 g, TCI L0235 lot YFJJKBS) and isobutyric acid (300 mL, Aldrich W222208 lot MKCF1895). The mixture was heated slowly with magnetic stirring to ˜50° C. The reaction then began to self-heat. An ice bath was immediately applied to control the exotherm. Upon cooling back to 70° C., the heating was resumed, in stages to 117° C., when water began to distill from the reaction, and further to 125° C., when a clear solution was obtained. The final temperature was 135° C., and held for 1 hour. Upon cooling, a solid block of material was obtained. This was dispersed in 200 ml heptane, filtered, and dried to give 176 g of lanthanum isobutyrate. The FTIR was identical to TD7-752 and these lots were combined.
TD7-759. Isobutyric acid (60 ml, Aldrich W222208 lot MKCF1895) was charged to the 150 ml EasyMax reactor under a nitrogen purge. Lanthanum oxide (65.07 g, TCI L0235 lot YFJJKBS) was added in 5 portions, monitoring the temperature each time. The first addition showed a significant incubation period, while subsequent additions were much faster to react. Overall, the heat of reaction is estimated at ˜370 kJ/mol, although the final addition showed a proportionately larger and extended exotherm. Taking this into account, however, only lessened the estimate to 320 kJ/mol.
TD7-753. A 1 L 3-necked flask was charged with zirconium basic carbonate (43.22 g, Alfa 43245 lot W11D012) under a nitrogen purge. Isobutyric acid (190 mL, Aldrich W222208 lot MKCF1895) and isobutyric anhydride (175 mL, Alfa L13240 lot 10195627) were added, causing bubbling and a slight temperature drop of 20-15° C. The mixture was heated slowly with magnetic stirring to ˜55° C., when upon a clear solution was obtained. The heating was continued in stages to a final temperature of 144° C. Water distilled out from ca. 125-140° C. Upon cooling, a clear colorless solution was obtained, contrary to the literature description.
The solution was then re-heated to 157° C. to distill excess isobutyric acid. Upon cooling, no precipitate appeared, so the isobutryic anhydride was distilled off under full vacuum at 70° C. to give a solid material. The solids were maintained at 70° C. for 90 minutes under full vacuum to give 51.78 g of material, far short of Zr(isobutyrate)4, which should yield 116 g. This yield may corresponds to a MW of 52/0.265=196 for a monomeric form, similar to (Me2CHCO2)Zr(OH)3, which is 229.34. Expected yield of this form, based on moles of zirconium basic carbonate, would be 61 g.
TD7-754. A 1 L 3-necked flask was charged with isobutryic acid (300 mL, Aldrich W222208 lot MKCF1895), to which zirconium basic carbonate (150.74 g, Alfa 43245 lot W11D012) was added in portions under a nitrogen purge. Bubbling and a slight temperature drop of 20-15° C. were observed. The mixture was stirred 30 minutes to allow bubbling to cease. A second charge of 100 ml of isobutyric acid was added to thin out the suspension. The mixture was heated slowly with magnetic stirring to ca. 80° C., when isobutyric anhydride (100 mL, Alfa L13240 lot 10195627) was added. The heating was continued in stages to a final temperature of 144° C. Water distilled out from ca. 105-140° C. Upon cooling, a clear colorless solution was obtained, contrary to the literature description.
The solution was then re-heated to 157° C. to distill excess isobutyric acid. Upon cooling, no precipitate appeared, so the isobutryic anhydride was distilled off under full vacuum at 80° C. to give a solid material. The solids were maintained at 80° C. for 90 minutes under full vacuum to give 211 g of material. The FTIR of the two samples were identical, and the materials were combined.
TD7-765. A 500 mL 3-necked flask was charged with isobutryic acid (190 mL, Aldrich W222208 lot MKCF1895), to which zirconium basic carbonate (43.17 g, Alfa 43245 lot W11D012) was added in portions under a nitrogen purge. Bubbling and a slight temperature drop were observed. The mixture was stirred 30 minutes to allow bubbling to cease. The mixture was heated slowly with magnetic stirring to ca. 80° C., when the solids fully dissolved. The heating was continued in stages to a final temperature of 145° C., and held for 1 hour. Water distilled out from ca. 105-145° C. Upon cooling, a clear colorless solution (158 g) was obtained, which was transferred under nitrogen to an amberbottle.
2-Ethylcaprylic acid (60 ml, TCI E0120 lot OQPPK EC) was charged to the 150 ml EasyMax reactor under a nitrogen purge. A single scoop of lanthanum oxide (13.36 g, TCI L0235 lot YFJJKBS) was added. No exothermic event was noted. Additional heating did not produce a reaction. The reaction was cooled and acetic acid (30 mL) was added, and then heated to 110° C. The material slowly solubilized. Portionwise addition of the remaining oxide showed exothermic reactions at each addition. The reaction was then heated to remove acetic acid. The solution clarified at ˜170° C., but even after holding for an hour, solids precipitated on cooling. The reaction mass was transferred to a 100 mL 3-neck flask and heated to 215° C. for 30 minutes under a slow nitrogen purge. Upon cooling, a think yellowish solution was obtained. This was transferred to an amber bottle under nitrogen: 66 g.
2-Ethylcaprylic acid (100 ml, TCI E0120 lot OQPPK EC) was charged to a 500 mL 3-neck flask. Zirconium basic carbonate (19.98 g, Alfa 43245 lot W11D012) was added in portions under a nitrogen purge. The suspension bubbled mildly, then was heated to 100° C. under nitrogen to form a clear solution. The solution was then heated in stages to 150° C. to remove water whilst purging strongly with nitrogen. The solution was held at 150° C. for 1 hour, then cooled to ambient. A slightly yellow solution was obtained (103.00 g), which was transferred to a 250 mL jar.
2-Ethylcaprylic acid (99.79 g, TCI E0120 lot OQPPK EC) was charged to a 250 mL 3-neck flask. Lithium hydroxide hydrate (10.05 g, Alfa 13409 lot Q13D018) was added under a nitrogen purge. The suspension was heated to 100° C. under nitrogen to form a mostly clear solution; this required 1-2 hours at 100° C. The solution was then heated in stages to 160° C. to remove water whilst purging strongly with nitrogen. The solution was held at 160° C. for 1 hour, then cooled to ambient. A colorless viscous solution was obtained (91.46 g), which was transferred, to ajar and stored under nitrogen.
SP utilizes non-flammable solutions, typically aqueous solution with inorganic salts. Similar to the FSP embodiments described previously, the SP process provides a pathway for the formation of c-LLZO at sub-1000° C. temperatures. The SP process forms atomically mixed green powder. In one embodiment, SP produces green powder for cubic LLZO using aqueous solution of nitrate salts of Li, La, Zr, and Al. For this process the mode driving the atomically mixed state of the resultant green powder is entirely different than FSP, with the critical phenomena being the precipitation sequence of the individual solutes. For example, if one of the solutes (precursors or dopant) has exceptional solubility compared to the others, then that component will remain in solution longer and thus segregate at the dried particle stage (i.e., will not possess the atomically mixed state). Thus, the solvent and solute materials and the solute concentrations should be selected to achieve the desired atomic mixing, such as where the metals precipitate nearly simultaneously.
It is believed that in one embodiment, a molten state intermediate during the pyrolysis phase could remedy the situation by diffusion.
The SP process may utilize a range of precursors. The precursors should be those deployable as atomizable solutions. In particular, the precursors (and dopant) should be soluable at the 2-10% ceramic yield level.
During the operation of SP, the solution was fed into atomizer where ultrasonic transducer converts the solution into droplets. The droplets were transported by carrier gas into the reaction zone maintained at 700° C. where the droplets were converted into particles followed by decomposition of the nitrates into oxide particle and then collected by bag house. The carrier gas was air.
The method of Spray Drying was demonstrated using a Buchi unit. The solution was transported to an atomizer where droplets will be generated. The droplets were carried by preheated gas into chamber. The gas temperature has the lower limit determined the vapor pressure of the solution (e.g., 100° C. for aqueous solutions, 78° C. for ethanol-based solutions). They are numbered under standard condition. For conditions with different pressures, the lower limit will be even lower. The higher limit of the temperature range is determined by the gas-heating unit. The carrier gas can be inert gases (N2 and Ar), oxidative gases (air and O2), or reductive gases (H2 and CO). The particle collection unit we used here is bag house. However, it can also be the filter pad, cyclones, or any instruments that can handle solid-gas separation. Cyclone was used as an example.
No claim element herein is to be construed under the provisions of 35 U.S.C. § 112(f), unless the element is expressly recited using the phrase “means for.”
As utilized herein, the terms “approximately,” “about,” “substantially”, and similar terms are intended to have a broad meaning in harmony with the common and accepted usage by those of ordinary skill in the art to which the subject matter of this disclosure pertains. It should be understood by those of skill in the art who review this disclosure that these terms are intended to allow a description of certain features described and claimed without restricting the scope of these features to the precise numerical ranges provided. Accordingly, these terms should be interpreted as indicating that insubstantial or inconsequential modifications or alterations of the subject matter described and claimed are considered to be within the scope of the disclosure as recited in the appended claims.
It should be noted that the term “exemplary” and variations thereof, as used herein to describe various embodiments, are intended to indicate that such embodiments are possible examples, representations, or illustrations of possible embodiments (and such terms are not intended to connote that such embodiments are necessarily extraordinary or superlative examples).
The term “coupled” and variations thereof, as used herein, means the joining of two members directly or indirectly to one another. Such joining may be stationary (e.g., permanent or fixed) or moveable (e.g., removable or releasable). Such joining may be achieved with the two members coupled directly to each other, with the two members coupled to each other using a separate intervening member and any additional intermediate members coupled with one another, or with the two members coupled to each other using an intervening member that is integrally formed as a single unitary body with one of the two members. If “coupled” or variations thereof are modified by an additional term (e.g., directly coupled), the generic definition of “coupled” provided above is modified by the plain language meaning of the additional term (e.g., “directly coupled” means the joining of two members without any separate intervening member), resulting in a narrower definition than the generic definition of “coupled” provided above. Such coupling may be mechanical, electrical, or fluidic. For example, circuit A communicably “coupled” to circuit B may signify that the circuit A communicates directly with circuit B (i.e., no intermediary) or communicates indirectly with circuit B (e.g., through one or more intermediaries).
The term “or,” as used herein, is used in its inclusive sense (and not in its exclusive sense) so that when used to connect a list of elements, the term “or” means one, some, or all of the elements in the list. Conjunctive language such as the phrase “at least one of X, Y, and Z,” unless specifically stated otherwise, is understood to convey that an element may be either X, Y, Z; X and Y; X and Z; Y and Z; or X, Y, and Z (i.e., any combination of X, Y, and Z). Thus, such conjunctive language is not generally intended to imply that certain embodiments require at least one of X, at least one of Y, and at least one of Z to each be present, unless otherwise indicated.
References herein to the positions of elements (e.g., “top,” “bottom,” “above,” “below”) are merely used to describe the orientation of various elements in the FIGURES. It should be noted that the orientation of various elements may differ according to other exemplary embodiments, and that such variations are intended to be encompassed by the present disclosure.
Although the figures and description may illustrate a specific order of method steps, the order of such steps may differ from what is depicted and described, unless specified differently above. Also, two or more steps may be performed concurrently or with partial concurrence, unless specified differently above.
This invention was made with government support under Contract No. DE-AC02-06CH11357 awarded by the United States Department of Energy to UChicago Argonne, LLC, operator of Argonne National Laboratory. The government has certain rights in the invention.
| Number | Date | Country | |
|---|---|---|---|
| 62861898 | Jun 2019 | US |
