Preparation method of battery composite material and precursor thereof
10096832 ยท 2018-10-09
Assignee
Inventors
Cpc classification
C01B25/45
CHEMISTRY; METALLURGY
H01M4/5825
ELECTRICITY
Y02E60/10
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
C01P2002/72
CHEMISTRY; METALLURGY
C30B1/10
CHEMISTRY; METALLURGY
International classification
H01M4/58
ELECTRICITY
C30B1/10
CHEMISTRY; METALLURGY
C01B25/45
CHEMISTRY; METALLURGY
Abstract
A preparation method of a battery composite material includes steps of providing phosphoric acid, a first metal source, a second metal source and water, processing a reaction of the first metal source, the second metal source, the phosphoric acid and the water to produce a first product, calcining the first product to produce a first precursor or a second precursor, among which each of the first precursor and the second precursor is a solid-solution containing first metal and second metal, and processing a reaction of the first precursor or the second precursor, and a first reactant to obtain a reaction mixture, and then calcining the reaction mixture to produce the battery composite material. As a result, the battery product has two stable charging and discharging platforms, such that the present invention achieves the advantages of enhancing the stability and the electric performance.
Claims
1. A preparation method of a battery composite material, comprising steps of: (a) providing phosphoric acid, a first metal source, a second metal source and water, wherein the formula of the phosphoric acid is written by H.sub.3PO.sub.4, the first metal source is a ferric source, the second metal source is a manganese source, and the formula of the ferric source is written by Fe.sub.7(PO.sub.4).sub.6; (b) processing a reaction of the first metal source, the second metal source, the phosphoric acid and the water to produce a first product; (c) calcining the first product to produce a first precursor or a second precursor, wherein each of the first precursor and the second precursor is a solid-solution containing first metal and second metal, and the formula of the first precursor and the second precursor is written by (Mn.sub.xFe.sub.1-x).sub.2P.sub.2O.sub.7, and wherein x is greater than or equal to 0.5, and is less than or equal to 0.95; and (d) processing a reaction of the first precursor or the second precursor, and at least a first reactant to obtain a reaction mixture, and then calcining the reaction mixture to produce the battery composite material, wherein the formula of the battery composite material is written by LiMn.sub.xFe.sub.1-xPO.sub.4.
2. The preparation method according to claim 1, wherein the first reactant is lithium hydroxide, and the formula of which is written by LiOH.
3. The preparation method according to claim 1, wherein the step (b) further comprises sub-steps of: (b1) allowing a first quantity of the water to dissolve a second quantity of the first metal source and a third quantity of the phosphoric acid to produce a first solution; and (b2) processing a reaction of the first solution and the second metal source and waiting for at least a first time period to produce the first product.
4. The preparation method according to claim 3, wherein the weight ratio of the first metal of the second quantity to phosphoric acid of the third quantity is 1:1.
5. The preparation method according to claim 3, wherein the first quantity is 5 liters, the second quantity is 904.9 grams, the third quantity is 2772.7 grams, and the first time period is 8 hours.
6. The preparation method according to claim 1, wherein the step (c) further comprises a sub-step of: (c1) calcining the first product in air atmosphere to produce the first precursor; or (c2) calcining the first product in a protective atmosphere to produce the second precursor.
7. The preparation method according to claim 6, wherein the protective atmosphere is a nitrogen atmosphere or an argon atmosphere.
8. The preparation method according to claim 6, wherein the first precursor and the second precursor are ferric manganese pyrophosphate.
9. The preparation method according to claim 1, wherein the step (d) further comprises sub-steps of: (d1) mixing at least the first reactant, and the first precursor or the second precursor; (d2) performing a high-temperature calcination; and (d3) producing the battery composite material.
10. The preparation method according to claim 9, wherein the high-temperature calcination is processed in an environment with temperature greater than 500 C.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
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DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT
(17) The present disclosure will now be described more specifically with reference to the following embodiments. It is to be noted that the following descriptions of preferred embodiments of this disclosure are presented herein for purpose of illustration and description only. It is not intended to be exhaustive or to be limited to the precise form disclosed.
(18) Please refer to
(19) Next, processing a reaction of the first metal source, the second metal source, the phosphoric acid and the water to produce a first product as shown in step S200. In some embodiments, the step S200 is preferred to include two sub-steps. Please refer to
(20) Then, calcining the first product obtained in the step S200 to produce a first precursor or a second precursor as shown in step S300, among which each of the first precursor and the second precursor is a solid-solution containing first metal and second metal, and is preferred to be applied to prepare the lithium-ion anode battery composite material with olivine crystalline structure. For example, the second precursor is ferric manganese pyrophosphate, and the formula of ferric manganese pyrophosphate is written by (Mn.sub.xFe.sub.1-x).sub.2P.sub.2O.sub.7, but not limited thereto. In addition, in some embodiments, the step S300 further includes sub-steps. Please refer to
(21) Finally, as shown in step S400, processing a reaction of the first precursor or the second precursor, and a first reactant to obtain a reaction mixture, and then calcining the reaction mixture to produce the battery composite material. The battery composite material is for example lithium ferric manganese phosphate or lithium ferric manganese phosphate nano-co-crystalline olivine, the formula of lithium ferric manganese phosphate is written by LiMn.sub.xFe.sub.1-xPO.sub.4, x>0. Preferably, x is greater than or equal to 0.5, and is less than or equal to 0.95, such that the battery composite material has a better electric performance. It should be noted that the first precursor or the second precursor is reacted with at least the first reactant in the step S400. Certainly, the first precursor or the second precursor is not limited to be reacted only with the first reactant, or be reacted with the first reactant and other reactants.
(22) Please refer to
(23) In the step S200 or the step S400, metal oxide, such as V.sub.2O.sub.5, TiO.sub.2 or MgO, can be added into the reaction, so that a LiMn.sub.xFe.sub.1-xPO.sub.4-like material containing the metal oxide, which can be called or named lithium ferric manganese phosphate nano-co-crystalline olivine (LFMP-NCO), is produced.
(24) Under this circumstance, the present invention provides a preparation method of a battery composite material for reducing the number of times of reduction-oxidation reactions in manner of preparing the battery composite material through the precursor produced via reactions, so that the stability of the manufacturing processes is enhanced, and the difficulty of the manufacturing processes is reduced.
(25) The following embodiments are presented herein for purpose of illustration and description of the preparation method of the battery composite material of the present disclosure.
1st Embodiment
(26) At first, providing 904.9 grams of Fe.sub.7(PO.sub.4).sub.6, 2772.7 grams of phosphoric acid (Purity>85%), 5.0 liters of deionized water and manganese source, mixing Fe.sub.7(PO.sub.4).sub.6 and the deionized water as a first metal source or a secondary metal source, and then adding the phosphoric acid to process a reaction and stirring. Next, adding the manganese source as a second metal source or a primary metal source and waiting for at least 8 hours to fully process a reaction to produce a precursor solution. Then, calcining the precursor solution in air atmosphere or a protective atmosphere (e.g. nitrogen atmosphere or argon atmosphere) with temperature greater than 400 C. The calcined compounds in air atmosphere and in the protective atmosphere are analyzed in manner of X-ray diffraction, and the analysis diagrams are respectively shown as
(27) Next, take the preparation of 18 molecules of lithium ferric manganese phosphate for example. Adding 2059.6 grams of the first precursor or the second precursor obtained in the above-mentioned steps and 755 to 792.7 grams of lithium hydroxide (i.e. LiOH) into 10 liters of pure water to process a reaction, and then adding the appropriate carbon source. Performing a high-temperature calcination with temperature greater than 500 C. to the product of reaction. The calcined compounds are analyzed in manner of X-ray diffraction, and the analysis diagrams are respectively shown as
(28) Next, mixing LiMn.sub.0.73Fe.sub.0.27PO.sub.4 obtained in the above-mentioned steps, conductive material Super P and 4 weight percent of binder (PVDF+NMP) in a ratio of 8.5:0.5:1. First, mixing 0.5 grams of conductive carbon black (Super P) and 25 grams of binder (PVDF:NMP=40:960) for 10 minutes. The rotational speed is 1200 rpm. Then, adding 8.5 grams of LiMn.sub.0.73Fe.sub.0.27PO.sub.4 and mixing for another 10 minutes. Next, coating the dispersed slurry on an aluminum substrate with a blade coater, among which the coating thickness is 0.3 millimeters. Then, putting the coated aluminum substrate into an oven and baking the coated aluminum substrate at 110 C. for 1 hour. Finally, forming the aluminum substrate as a circular plate, among which the diameter of the circular plate is 1.3 centimeters, and making a coin-cell battery with this circular plate, lithium metal (as the negative electrode), 1 molar concentration of LiPF.sub.6 and a mixed electrolyte of EC and DMC (volume ratio=3:7). The electric characteristics of charging and discharging of the coin-cell battery are tested and analyzed through a charging and discharging machine. The test and the analysis are performed at 0.1 coulombs for two cycles and 2 coulombs for two cycles. The charging and discharging characteristic diagram is shown as
2nd Embodiment
(29) Adjusting the ratio of the ferric source to the manganese source of the first embodiment for finally obtaining the battery composite material with the ratio of Mn to Fe equal to 8:2. In other words, the battery composite material is adjusted as LiMn.sub.0.8Fe.sub.0.2PO.sub.4. The electric characteristics of charging and discharging are tested under the same environment, and the charging and discharging characteristic diagram is shown as
3rd Embodiment
(30) Adjusting the ratio of the ferric source to the manganese source of the first embodiment for finally obtaining the battery composite material with the ratio of Mn to Fe equal to 85:15. In other words, the battery composite material is adjusted as LiMn.sub.0.85Fe.sub.0.15PO.sub.4. The electric characteristics of charging and discharging are tested under the same environment, and the charging and discharging characteristic diagram is shown as
4th Embodiment
(31) Adjusting the ratio of the ferric source to the manganese source of the first embodiment for finally obtaining the battery composite material with the ratio of Mn to Fe equal to 9:1. In other words, the battery composite material is adjusted as LiMn.sub.0.9Fe.sub.0.1PO.sub.4. The electric characteristics of charging and discharging are tested under the same environment, and the charging and discharging characteristic diagram is shown as
5th Embodiment
(32) Adding metal oxide, such as V.sub.2O.sub.5, TiO.sub.2 or MgO, in the step S200 or the step S400 of the first embodiment, so that lithium ferric manganese phosphate nano-co-crystalline olivine is produced. The rest portion of this embodiment is similar with the first embodiment, and is not redundantly described herein.
6th Embodiment
(33) At first, providing 2445.6 grams of Fe.sub.2(C.sub.2O.sub.4).sub.3.5H.sub.2O, 3947.1 grams of phosphoric acid (Purity>85%), 5.0 liters of deionized water and manganese source, mixing Fe.sub.2(C.sub.2O.sub.4).sub.3.5H.sub.2O and the deionized water as a first metal source or a secondary metal source, and then adding the phosphoric acid to process a reaction and stirring. Next, adding the manganese source as a second metal source or a primary metal source and waiting for at least 8 hours to fully process a reaction to produce a precursor solution. Then, calcining the precursor solution in air atmosphere or a protective atmosphere (e.g. nitrogen atmosphere or argon atmosphere) with temperature greater than 400 C. to produce the first precursor or the second precursor.
(34) Next, take the preparation of 18 molecules of lithium ferric manganese phosphate for example. Adding 2059.6 grams of the first precursor or the second precursor obtained in the above-mentioned steps and 755 to 792.7 grams of lithium hydroxide (i.e. LiOH) into 10 liters of pure water to process a reaction, and then adding the appropriate carbon source. Performing a high-temperature calcination with temperature greater than 500 C. to the product of reaction. The calcined compounds are analyzed in manner of X-ray diffraction and are confirmed to be lithium ferric manganese phosphate LiMn.sub.0.73Fe.sub.0.27PO.sub.4.
7th Embodiment
(35) At first, providing 1789 grams of Fe(C.sub.2H.sub.3O.sub.2).sub.2, 3947.1 grams of phosphoric acid (Purity>85%), 5.0 liters of deionized water and manganese source, mixing Fe(C.sub.2H.sub.3O.sub.2).sub.2 and the deionized water as a first metal source or a secondary metal source, and then adding the phosphoric acid to process a reaction and stirring. Next, adding the manganese source as a second metal source or a primary metal source and waiting for at least 8 hours to fully process a reaction to produce a precursor solution. Then, calcining the precursor solution in air atmosphere or a protective atmosphere (e.g. nitrogen atmosphere or argon atmosphere) with temperature greater than 400 C. to produce the first precursor or the second precursor.
(36) Next, take the preparation of 18 molecules of lithium ferric manganese phosphate for example. Adding 2059.6 grams of the first precursor or the second precursor obtained in the above-mentioned steps and 755 to 792.7 grams of lithium hydroxide (i.e. LiOH) into 10 liters of pure water to process a reaction, and then adding the appropriate carbon source. Performing a high-temperature calcination with temperature greater than 500 C. to the product of reaction. The calcined compounds are analyzed in manner of X-ray diffraction and are confirmed to be lithium ferric manganese phosphate LiMn.sub.0.73Fe.sub.0.27PO.sub.4.
8th Embodiment
(37) At first, providing 821.3 grams of Fe.sub.2O.sub.3, 3947.1 grams of phosphoric acid (Purity>85%), 5.0 liters of deionized water and manganese source, mixing Fe.sub.2O.sub.3 and the deionized water as a first metal source or a secondary metal source, and then adding the phosphoric acid to process a reaction and stirring. Next, adding the manganese source as a second metal source or a primary metal source and waiting for at least 8 hours to fully process a reaction to produce a precursor solution. Then, calcining the precursor solution in air atmosphere or a protective atmosphere (e.g. nitrogen atmosphere or argon atmosphere) with temperature greater than 400 C. to produce the first precursor or the second precursor.
(38) Next, take the preparation of 18 molecules of lithium ferric manganese phosphate for example. Adding 2059.6 grams of the first precursor or the second precursor obtained in the above-mentioned steps and 755 to 792.7 grams of lithium hydroxide (i.e. LiOH) into 10 liters of pure water to process a reaction, and then adding the appropriate carbon source. Performing a high-temperature calcination with temperature greater than 500 C. to the product of reaction. The calcined compounds are analyzed in manner of X-ray diffraction and are confirmed to be lithium ferric manganese phosphate LiMn.sub.0.73Fe.sub.0.27PO.sub.4.
(39) Please refer to
(40) Please refer to
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(42) From the above description, the present invention provides a preparation method of a battery composite material and a precursor thereof for reducing the number of times of reduction-oxidation reactions in manner of preparing the battery composite material through the precursor produced via reactions, so that the stability of the manufacturing processes is enhanced, and the difficulty of the manufacturing processes is reduced. Furthermore, by preparing a solid-solution including first metal and second metal as a precursor for finally producing a battery composite material, the battery composite material and the battery product have two stable charging and discharging platforms, such that the advantages of enhancing the stability and the electric performance are achieved.
(43) While the disclosure has been described in terms of what is presently considered to be the most practical and preferred embodiments, it is to be understood that the disclosure needs not be limited to the disclosed embodiment. On the contrary, it is intended to cover various modifications and similar arrangements included within the spirit and scope of the appended claims, which are to be accorded with the broadest interpretation so as to encompass all such modifications and similar structures.