The present invention relates to a preparation method, and more particularly to a preparation method of battery composite material and a precursor thereof.
With the rapid development of global economy, the exhaustion of resources increases day by days. Recently, the concept of environmental protection becomes much more important. In order to overcome the problems of energy shortages and also focus on the sustainable management at the same time, looking for eco-friendly, clean and effective alternative energies has become an important development direction in the industry. Among varieties of alternative energies, the research and development of chemical battery is actively invested by related industries, such that the technology of battery preparation is improved, and the battery efficiency is enhanced. Furthermore, the chemical batteries are also widely used in our daily life, such as consuming electronics, medical equipment, electric bicycles, electric motorcycles, electric cars and electric buses.
In kinds of chemical batteries, lithium batteries are widely accepted in the market and become popular because of its characteristics of high energy density, no memory effect, long cycle life and non-pollution. In addition, the batteries applying lithium manganese phosphate (LiMnPO4) as the cathode material have higher energy density, higher charging and discharging capacity, stability and safety, and advantages of rich source of raw materials and lower price, so the lithium manganese phosphate has become a cathode material of lithium batteries with high potential in development.
However, in the conventional preparation methods of lithium manganese phosphate, hydrothermal method and organic solution method are usually adopted, in which steps are more complicated. Furthermore, the preparation temperatures and the energy consumption are high in those methods, and the phase of manganese lithium phosphate is also unstable. In addition, the manganese lithium phosphate is often deemed as reactants of transition state.
Therefore, there is a need of providing a preparation method of a battery composite material and a precursor thereof to solve the drawbacks in prior arts, simplify the steps of the preparation, reduce the energy consumption, and achieve the advantages of making the phase of manganese lithium phosphate stable.
It is an object of the present invention to provide a preparation method of a battery composite material and a precursor thereof in order to solve the drawbacks of prior art.
The present invention provides a preparation method of a battery composite material and a precursor thereof. Through simple aqueous solution method, the precursor is produced by reacting in acidic environment to prepare the battery composite material. The steps of the preparation method are less complicated, such that the preparation time is reduced, and the preparation effectiveness is enhanced.
The present invention also provides a preparation method of a battery composite material and a precursor thereof. By producing the precursor at low temperature within a short time period in the process of a low-temperature phase method, the energy consumption is reduced, the phase of the precursor is more stable, and the advantages of reducing the cost of preparation and enhancing the quality of products are achieved.
In accordance with an aspect of the present invention, there is provided a preparation method of a battery composite material. The preparation method of a battery composite material at least comprises steps of: (a) providing a manganese-contained compound, phosphoric acid, a lithium-contained compound, a carbon source, and deionized water, wherein the chemical formula of the phosphoric acid is written by H3PO4; (b) processing a reaction of the manganese-contained compound, the phosphoric acid, and a portion of the deionized water to produce a first product; (c) placing the first product at a first temperature for at least a first time period to produce a first precursor, wherein the chemical formula of the first precursor is written by Mn5(HPO4)2(PO4)2(H2O)4; and (d) processing a reaction of at least the first precursor, the lithium-contained compound, and another portion of the deionized water, adding the carbon source, and then calcining to produce the battery composite material.
In accordance with an aspect of the present invention, there is provided a preparation method of a precursor of a battery composite material. The preparation method of a precursor of a battery composite material at least comprises steps of: (a) providing a manganese-contained compound, phosphoric acid, and deionized water, wherein the chemical formula of the phosphoric acid is written by H3PO4; (b) processing a reaction of the manganese-contained compound, the phosphoric acid, and the deionized water to produce a first product; and (c) placing the first product at a first temperature for at least a first time period to produce a first precursor, wherein the chemical formula of the first precursor is written by Mn5(HPO4)2(PO4)2(H2O)4.
In accordance with an aspect of the present invention, there is provided a preparation method of a battery composite material. The preparation method of a battery composite material at least comprises steps of processing a reaction of a precursor, a lithium-contained compound, and deionized water, adding a carbon source, and then calcining to produce the battery composite material, wherein the chemical formula of the precursor is written by Mn5(HPO4)2(PO4)2(H2O)4, and the chemical formula of the battery composite material is written by LiMnPO4.
In accordance with an aspect of the present invention, there is provided a preparation method of a battery composite material. The preparation method of a battery composite material at least comprises steps of: (a) providing a manganese-contained compound, an iron-contained compound, phosphoric acid, a lithium-contained compound, a carbon source, and deionized water, wherein the chemical formula of the phosphoric acid is written by H3PO4; (b) processing a reaction of the manganese-contained compound, the iron-contained compound, the phosphoric acid, and a portion of the deionized water to produce a second product; (c) placing the second product at a first temperature for at least a first time period to produce a second precursor, wherein the chemical formula of the second precursor is written by (Mnx,Fe1-x)5(HPO4)2(PO4)2(H2O)4, and wherein x is larger than 0.5 and less than or equal to 1; and (d) processing a reaction of at least the second precursor, the lithium-contained compound, and another portion of the deionized water, adding the carbon source, and then calcining to produce the battery composite material, wherein the chemical formula of the battery composite material is written by LiMnxFe1-xPO4.
The above contents of the present invention will become more readily apparent to those ordinarily skilled in the art after reviewing the following detailed description and accompanying drawings, in which:
The present invention 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 invention 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.
Please refer to
Next, in a step S200, a reaction of the manganese-contained compound, the phosphoric acid, and a portion of the deionized water is processed to produce a first product. The step S200 further comprises a step of performing a grinding and dispersing action and a drying action to the first product. The grinding action can be implemented by a ball mill, and the drying action can be implemented by rolling dehydration or spray drying, but not limited herein. In addition, the drying method of rolling dehydration can perform drying action to the first product abundantly and rapidly, so that the productivity of the dried first product produced by rolling dehydration is high.
Then, in a step S300, the first product is placed at a first temperature for at least a first time period to produce a first precursor, and the chemical formula of the first precursor is written by Mn5(HPO4)2(PO4)2(H2O)4. In some embodiments, the first temperature is larger than or equal to 60° C., and less than or equal to 100° C., which means 60° C.≦the first temperature≦100° C. The first time period is larger than or equal to 18 hours, that is to say, the first time period 18 hours.
Lastly, in a step S400, a reaction of at least the first precursor, the lithium-contained compound, and another portion of the deionized water is processed, then the carbon source is added and then calcined to produce the battery composite material such as lithium manganese phosphate (LiMnPO4).
In some embodiments, in the step S400, a reaction of the first precursor, an iron-contained compound, the lithium-contained compound, and another portion of the deionized water can be processed, and the iron-contained compound is heptairon hexaphosphate (Fe7(PO4)6), iron(III) phosphate dihydrate (FePO4.2H2O) or other compound containing iron-ion. Then, the carbon source is added and then calcined to produce the battery composite material such as lithium iron manganese phosphate, which is written by LiMnxFe1-xPO4, and x is larger than 0.5 and less than or equal to 1.
That is to say, in the preparation method of battery composite material and a precursor thereof of the present invention, through simple aqueous solution method, the precursor is produced by reacting in acidic environment to prepare the battery composite material. The steps of the preparation method are less complicated, such that the preparation time is reduced, and the preparation effectiveness is enhanced. Meanwhile, by producing the precursor at low temperature within a short time period in the process of a low-temperature phase method, the energy consumption is reduced, the phase of the precursor is more stable, and the advantages of reducing the cost of preparation and enhancing the quality of products are achieved.
Please refer to
In the step S403, the spray drying action can be performed by a rotary disk spray dryer, but not limited herein. In addition, the thermal treatment is performed to the spray-dried product at a temperature larger than 600° C. for at least 5 hours, such as sintering to phase at 600° C. for 5 hours, but not limited thereto.
Please refer to
Next, in a step S600, a reaction of the manganese-contained compound, the iron-contained compound, the phosphoric acid, and a portion of the deionized water is processed to produce a second product. The step S600 further comprises a step of performing a grinding and dispersing action and a drying action to the second product.
Then, in a step S700, the second product is placed at a first temperature for at least a first time period to produce a second precursor. The chemical formula of the second precursor is written by (Mnx,Fe1-x)5(HPO4)2(PO4)2(H2O)4, and 0.5<x≦1. Furthermore, the first temperature≦100° C., and the first time period≧18 hours.
Lastly, in a step S800, a reaction of at least the second precursor, the lithium-contained compound, and another portion of the deionized water is processed, then the carbon source is added so as to be calcined for producing the battery composite material. The chemical formula of the battery composite material is written by LiMnxFe1-xPO4.
The following embodiments are presented herein for purpose of illustration and description of the preparation method of the battery composite material and the precursor thereof of the present disclosure.
Firstly, 574.7 grams of manganese carbonate (MnCO3), 575.61 grams of phosphoric acid (H3PO4) with weight percentage concentration equal to 85.1%, and 2 liters of deionized water are provided to process a reaction in order to produce a first product. Next, the first product is grinded and dispersed by the ball mill, and then placed at the temperature of 60° C. to 100° C. to dry for at least 18 hours to produce the precursor by the process of a low-temperature phase method. The precursor is analyzed in manner of X-ray diffraction, and the analysis diagram is shown as
Firstly, 574.7 grams of manganese carbonate (MnCO3), 575.61 grams of phosphoric acid (H3PO4) with weight percentage concentration equal to 85.1%, and 2 liters of deionized water are provided to process a reaction in order to produce a first product. Next, the first product is grinded and dispersed by the ball mill, then dried through the rolling dehydration, and placed at the temperature of 60° C. to 100° C. for at least 18 hours to produce the precursor by the process of a low-temperature phase method. The precursor is analyzed in manner of X-ray diffraction, and the analysis diagram is shown as
Firstly, 574.7 grams of manganese carbonate (MnCO3), 575.61 grams of phosphoric acid (H3PO4) with weight percentage concentration equal to 85.1%, and 2 liters of deionized water are provided to process a reaction in order to produce a first product. Next, the first product is grinded and dispersed by the ball mill, then dried through the spray drying method, and placed at the temperature of 60° C. to 100° C. for at least 18 hours to produce the precursor by the process of a low-temperature phase method. The precursor is analyzed in manner of X-ray diffraction, and the analysis diagram is shown as
Firstly, 894.9 grams of manganese nitrate (Mn(NO3)2), 575.61 grams of phosphoric acid (H3PO4) with weight percentage concentration equal to 85.1%, and 2 liters of deionized water are provided to process a reaction. Then, the PH value is adjusted to 7-8 by ammonia solution (NH4OH), and the solution is precipitated to produce a first product. Next, the first product is grinded and dispersed by the ball mill, and then placed at the temperature of 60° C. to 100° C. to dry for at least 18 hours to produce the precursor by the process of a low-temperature phase method. The precursor is analyzed in manner of X-ray diffraction, and the analysis diagram is shown as
Firstly, 754.9 grams of manganese sulfate (MnSO4), 575.61 grams of phosphoric acid (H3PO4) with weight percentage concentration equal to 85.1%, and 2 liters of deionized water are provided to process a reaction. Then, the PH value is adjusted to 7-8 by ammonia solution (NH4OH), and the solution is precipitated to produce a first product. After filtering, the first product is grinded and dispersed by the ball mill, and then placed at the temperature of 60° C. to 100° C. to dry for at least 18 hours to produce the precursor by the process of a low-temperature phase method. The precursor is analyzed in manner of X-ray diffraction, and the analysis diagram is shown as
Firstly, 402.3 grams of manganese carbonate (MnCO3), 260.9 grams of iron(II) acetate (Fe(CH3COOH)2), 571.61 grams of phosphoric acid (H3PO4) with weight percentage concentration equal to 85.1%, and 2 liters of deionized water are provided to process a reaction in order to produce a second product. Next, the second product is grinded and dispersed by the ball mill, and then placed at the temperature of 60° C. to 100° C. to dry for at least 18 hours to produce the precursor by the process of a low-temperature phase method. The precursor is analyzed in manner of X-ray diffraction, and the analysis diagram is shown as
Firstly, 402.3 grams of manganese carbonate (MnCO3), 269.8 grams of iron(II) oxalate dihydrate (FeC7O4.2H2O), 571.61 grams of phosphoric acid (H3PO4) with weight percentage concentration equal to 85.1%, and 2 liters of deionized water are provided to process a reaction in order to produce a second product. Next, the second product is grinded and dispersed by the ball mill, and then placed at the temperature of 60° C. to 100° C. to dry for at least 18 hours to produce the precursor by the process of a low-temperature phase method. The precursor is analyzed in manner of X-ray diffraction, and the analysis diagram is shown as
799.88 grams of the precursor, Mn5(HPO4)2(PO4)2(H2O)4, obtained in the above-mentioned embodiments, 184.7 grams of lithium carbonate (Li7CO3), and 2 liters of deionized water are provided to process a reaction. Next, after dispersing and grinding, carbon source is added to obtain precursor solution. Then, the precursor solution is dried by the spray drying method, and sintered to phase at 600° C. for 5 hours to produce the battery composite material. The battery composite material is analyzed in manner of X-ray diffraction, and the analysis diagram is shown as
799.88 grams of the precursor, Mn5(HPO4)2(PO4)2(H2O)4, obtained in the above-mentioned embodiments, 209.7 grams of lithium hydroxide (LiOH), and 2 liters of deionized water are provided to process a reaction. Next, after dispersing and grinding, carbon source is added to obtain precursor solution. Then, the precursor solution is dried by the spray drying method, and sintered to phase at 600° C. for 5 hours to produce the battery composite material. The battery composite material is analyzed in manner of X-ray diffraction, and the analysis diagram is shown as
559.92 grams of the precursor, Mn5(HPO4)2(PO4)2(H2O)4, obtained in the above-mentioned embodiments, 226.23 grams of heptairon hexaphosphate (Fe7(PO4)6), 184.7 grams of lithium carbonate (Li2CO3), and 2 liters of deionized water are provided to process a reaction. Next, after dispersing and grinding, carbon source is added to obtain precursor solution. Then, the precursor solution is dried by the spray drying method, and sintered to phase at 600° C. for 5 hours to produce the battery composite material. The battery composite material is analyzed in manner of X-ray diffraction, and the analysis diagram is shown as
559.92 grams of the precursor, Mn5(HPO4)2(PO4)2(H2O)4, obtained in the above-mentioned embodiments, 226.23 grams of iron(III) phosphate dihydrate (FePO4.2H2O), 184.7 grams of lithium carbonate (Li2CO3), and 2 liters of deionized water are provided to process a reaction. Next, after dispersing and grinding, carbon source is added to obtain precursor solution. Then, the precursor solution is dried by the spray drying method, and sintered to phase at 600° C. for 5 hours to produce the battery composite material. The battery composite material is analyzed in manner of X-ray diffraction, and the analysis diagram is shown as
The lithium manganese phosphate (LiMnPO4) obtained in the above-mentioned embodiments is mixed with carbon black (Super P) and binder (NVDF+NMP) as the proportion of 8.5:0.5:1, and the weight percentage concentration of the binder is 4%. For example, firstly, 0.5 grams of carbon black (Super P) and 25 grams of binder (NVDF:NMP=40:960) are mixed at 1200 rpm for 10 minutes. Then, 8.5 grams of lithium manganese phosphate (LiMnPO4) is added and mixed for another 10 minutes. Next, the dispersed slurry is coated with thickness of 0.3 mm on an aluminum substrate by a blade coater, and the coated pole piece is put into the oven, dried at 110° C. for 1 hour and then taken out. Then, a round pole plate is made with lithium as the negative electrode, and a diameter of the round pole plate is 1.3 cm. Then, lithium hexafluorophosphate (LiPF6) with molarity as 1M, EC and EMC are mixed as electrolyte, among which the volume ratio of EC and EMC is 3:7. Lastly, the coated pole piece, the round pole plate and the electrolyte are made into a coin-cell battery. The electric characteristics of charging and discharging 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
The lithium iron manganese phosphate (LiMnxFe1-xPO4) obtained in the above-mentioned embodiments is mixed with carbon black (Super P) and binder (NVDF+NMP) as the proportion of 8.5:0.5:1, and the weight percentage concentration of the binder is 4%. For example, firstly, 0.5 grams of carbon black (Super P) and 25 grams of binder (NVDF:NMP=40:960) are mixed at 1200 rpm for 10 minutes. Then, 8.5 grams of lithium iron manganese phosphate (LiMnxFei,PO4) is added and mixed for another 10 minutes. Next, the dispersed slurry is coated with thickness of 0.3 mm on an aluminum substrate by a blade coater, and the coated pole piece is put into the oven, dried at 110° C. for 1 hour and then taken out. Then, a round pole plate is made with lithium as the negative electrode, and a diameter of the round pole plate is 1.3 cm. Then, lithium hexafluorophosphate (LiPF6) with molarity as 1M, EC and EMC are mixed as electrolyte, among which the volume ratio of EC and EMC is 3:7. Lastly, the coated pole piece, the round pole plate and the electrolyte are made into a coin-cell battery. The electric characteristics of charging and discharging 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
From the above description, the present invention provides a preparation method of battery composite material and a precursor thereof. Through simple aqueous solution method, the precursor is produced by reacting in acidic environment to prepare the battery composite material. The steps of the preparation method are less complicated, such that the preparation time is reduced, and the preparation effectiveness is enhanced. Meanwhile, by producing the precursor at low temperature within a short time period in the process of a low-temperature phase method, the energy consumption is reduced, the phase of the precursor is more stable, and the advantages of reducing the cost of preparation and enhancing the quality of products are achieved.
While the invention 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 invention 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.
This application claims the benefit of PCT application No. PCT/CN2016/070382 filed Jan. 7, 2016 which claims priority to U.S. Provisional Application No. 62/101,054 filed Jan. 8, 2015, and entitled “Method for Preparing Metal (II) Phosphate Used as Precursors of LiMnPO4 and LiMnxFe1-xPO4”, the entire contents of which are incorporated herein by reference for all purposes.
Filing Document | Filing Date | Country | Kind |
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PCT/CN2016/070382 | 1/7/2016 | WO | 00 |
Number | Date | Country | |
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62101054 | Jan 2015 | US |