CN1812166A - Preperative method for ferrous phosphate radical lithium salt of lithium ion secondary cell active material - Google Patents
Preperative method for ferrous phosphate radical lithium salt of lithium ion secondary cell active material Download PDFInfo
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Abstract
This invention provides a kind of producing method of lithium ionic cell anode active materials phosphoric acid ferrous-base lithium. The method concludes: mix evenly lithium compound, iron compound, phosphorus compound according to mole ratio of Li:Fe:P=(0.95-1.3):1:(1-1.5). Then the mixed materials are tablet compressed under pressure range of 2.5-11MPa. Then, they are high temperature roasted and dropped to home temperature spontaneously under the protection of inert or reducing atmosphere. As the acquired phosphoric acid ferrous-base lithium has high tap density, the lithium ionic cell has high discharging specific volume when using this invention.
Description
[technical field]
The present invention relates to a kind of preparation method of anode active material of lithium ion battery ferrous phosphate base lithium salts.
[background technology]
At present, transition metal lithium intercalation compound LiMO
2(M represents metallic elements such as Co, Ni, Mn, Fe) and LiM
2O
4(M represents metallic elements such as Mn, Co) is the research emphasis of lithium ion secondary battery anode material always.LiCoO
2Be the positive electrode that present most commercialization lithium rechargeable battery uses, but cobalt resource is limited, costs an arm and a leg and poisonous; LiNiO
2Synthetic difficulty and under full-charge state poor stability; LiMn
2O
4Capacity under high temperature decay rapidly makes it also have certain distance from practicability.Therefore, lithium battery industry, particularly high-power power lithium-ion battery needs a kind of cost lower, the big and safer positive electrode of capacity.
Report that since 1997 lithium ion is at LiFePO
4In electrochemistry to take off the embedding process be reversible and ferrous phosphate base lithium salts LiFePO
4Multicrystal theoretical specific discharge capacity can reach since the 170mAh/g, has the olivine-type positive electrode LiMPO of ordered structure
4Just be subjected to paying attention to widely, be considered to have the lithium ion secondary battery anode material of application potential.
Ferrous phosphate base lithium salts LiFePO
4Though have broad application prospects, also there are the following problems at present: its conductivity at room temperature is very low, so can only discharge and recharge under minimum electric current; Its tap density is little, is unfavorable for improving the volume and capacity ratio of electric core; In synthetic iron be easy to from+divalent is oxidized to+3 valencys, and the product germination is wayward in the high temperature building-up process.These problems have limited its application in actual battery.
If LiFePO
4With LiMn
2O
4Compare, the former bulk density is 3.6g/cm
3, average voltage is 3.4V, and the latter's bulk density is 4.2g/cm
3, average voltage is 3.9V, capacity is 120mAh/g; Like this, for realizing identical energy density, LiFePO
4Just need higher capacity, just need to improve its bulk density for this reason.
At preparation ferrous phosphate base lithium salts LiFePO
4The time, people generally take to use lithium salts, ferrous salt, the method for roasting at high temperature after phosphate mixes.CN 1300449A discloses a kind of lithium carbonate, ammonium dihydrogen phosphate, ferrous oxalate of using and has been raw material, carries out roasting under 450-700 ℃ after mixing in inertia or reducing atmosphere and prepares ferrous phosphate base lithium salts LiFePO
4The method of material is wherein mentioned in raw mix and to be added reducing agent such as metal iron powder ferrous iron when preventing high temperature sintering and be oxidized to ferric iron, and mentions and can add conductive agent to improve the electric conductivity of product in reaction raw materials.
A kind of synthetic ferrous phosphate base lithium salts LiFePO is disclosed among the day disclosure special permission communique 2003-157845
4Method, this method comprises prepares the colloidal sol shape liquid phase reactor thing that contains lithium compound, iron compound, phosphoric acid and a kind of solvent earlier, heating removes and desolvates, and roasting is carried out in heat treatment under lower temperature in inert atmosphere then under higher temperature in inert atmosphere.The advantage of this method mainly is can remove the oxygen that may exist in reaction system ferrous iron when preventing high temperature sintering to be oxidized to ferric iron before high-temperature roasting, thereby can obtain single-phase olivine-type LiFePO
4Crystal.
Be used for synthetic ferrous phosphate base lithium salts LiFePO above
4Method still have the low shortcoming of products therefrom tap density, thereby the electric core volume specific capacity of producing is undesirable.
[summary of the invention]
The purpose of this invention is to provide a kind of anode active material of lithium ion secondary battery ferrous phosphate base lithium salts LiFePO
4The preparation method.The LiFePO that uses the inventive method to prepare
4The tap density of material is big, and the lithium rechargeable battery that contains this positive active material has good electrochemical, the specific discharge capacity height.
The invention provides a kind of preparation method of anode active material of lithium ion battery ferrous phosphate base lithium salts, may further comprise the steps:
(1) lithium compound, iron compound, phosphorus compound are mixed, preferably carry out ball milling and mix;
(2) step (1) gained mixture being carried out compressing tablet handles;
(3) material behind step (2) the gained compressing tablet is carried out high-temperature roasting in inertia or reducing atmosphere, and in inertia or reducing atmosphere protection, reduce to room temperature naturally.
The Li in lithium compound, iron compound and the phosphorus compound described in the step (1) wherein: the mol ratio of Fe: P can be determined according to prior art, the present invention has no particular limits it, and the mol ratio of preferred Li: Fe: P is (0.95-1.3): 1: (1-1.5).
Described lithium compound can be determined according to prior art, the present invention has no particular limits it, can be, for example, this area routines such as lithium carbonate, lithium nitrate, lithium hydroxide, lithium oxalate, lithium acetate, lithium phosphate, lithium hydrogen phosphate, lithium dihydrogen phosphate and available lithium compound.Wherein preferably lithium phosphate, lithium hydrogen phosphate or lithium dihydrogen phosphate, this moment, lithium and phosphorus derived from same raw material, can reduce reactant species.
Described iron compound can be determined according to prior art, there is no particular limitation to it in the present invention, can for, for example, at least a in ferrous oxalate, ferrous phosphate, ferrous oxide and the di-iron trioxide, wherein at least a in ferrous oxalate, ferrous phosphate and the ferrous oxide preferably.
Described phosphorus compound can determine that according to prior art there is no particular limitation to it in the present invention, can for, for example, at least a in phosphoric acid, lithium phosphate, lithium hydrogen phosphate, lithium dihydrogen phosphate and the ferrous phosphate.
Preferably, can adopt lithium phosphate, lithium hydrogen phosphate or lithium dihydrogen phosphate as the lithium source and the phosphorus source of mixing, and/or adopt ferrous phosphate as the phosphorus source and the source of iron of mixing, can be adjusted to required scope with the mol ratio with lithium, iron, phosphorus this moment by adding other suitable raw material.
In the blend step of step (1), can also add a kind of conductive agent, there is no particular limitation for this conductive agent, for example can be in sucrose, carbon black, metal nano level powder and the acetylene black at least a.The consumption of described conductive agent can be the 1-25 weight % of step (1) gained mixture total weight amount.
In the method for the present invention, can also be included in and carry out described step (2) is carried out step (1) gained mixture heat pre-treatment before in inertia or reducing atmosphere step; Adopting this heat pre-treatment step is in order to remove the aqueous vapor that exists in the raw mix, air etc. in advance before high-temperature roasting, and before high-temperature roasting, for example heat decomposable reaction raw materials such as oxalates, carbonate, nitrate are carried out thermal decomposition in advance, and then carry out compressing tablet, preventing that the later reactant of compressing tablet from producing gas when the high-temperature roasting of carrying out subsequently, thereby can more effectively improve tap density.The condition optimization of described heat pre-treatment be in inertia or reducing atmosphere, to handle 5～30 hours under less than 500 ℃ temperature at 50 ℃, more preferably in inertia or reducing atmosphere, be warming up to 50 ℃ and kept this temperature then 5-30 hour to temperature less than 500 ℃ with 1-10 ℃/minute heating rate.
Inertia described in each step or reducing atmosphere can be at least a gas that contains in hydrogen, nitrogen, argon gas, carbon monoxide and the carbon dioxide, wherein preferably contain the reducing atmosphere of hydrogen or carbon monoxide.This inertia or reducing atmosphere can be static atmosphere, but preferably gas flow rate be the 0.01-40 liter/minute mobile atmosphere, more preferably gas flow rate be the 2-10 liter/minute mobile atmosphere.
The pressure that compressing tablet described in the step (2) is handled is 2.5-11MPa, is preferably 3.5-10MPa.Adopting this compressing tablet treatment step is in order to improve tap density.If this pressure is lower than 2.5MPa, there is the problem of compressing tablet DeGrain, can not effectively be increased to the set goal.On the other hand, if compressing tablet pressure greater than 11MPa, exists compressing tablet pressure excessive, can be cracked in sintering, influence improves the effect of its tap density.Therefore, by being not less than 2.5MPa and not being higher than under the pressure of 11MPa to ferrous phosphate base lithium salts LiFePO
4Parent carries out compressing tablet, can effectively improve its tap density.
The condition of high-temperature roasting described in the step (3) can adopt high-temperature roasting condition conventional in the prior art, preferably in inertia or reducing atmosphere, under 500～900 ℃ temperature, handled 8～48 hours, more preferably in inertia or reducing atmosphere, be warming up to 500-900 ℃ and kept this temperature then 8-48 hour with 1-10 ℃/minute heating rate.
The invention has the beneficial effects as follows:
Owing to comprise the described compressing tablet step of step (2) in the inventive method, can effectively improve the tap density of anode active material of lithium ion secondary battery by method of the present invention, thereby improve the battery specific capacity;
When adopting lithium phosphate as raw material, lithium and phosphorus derive from same raw material, can reduce reactant species, make that reactant is easier to mix, and is favourable to synthetic single-phase olivine-type crystal structure;
When the adding conductive agent directly burns till under reducing atmosphere, can obtain the ferrous phosphate base lithium salts powder that rigid carbon coats, coat the electron conduction that processing can improve material so need not carry out the later stage, discharge voltage plateau is also very steady.
[description of drawings]
Fig. 1 is X-ray diffraction (XRD) figure (CuK α target, the λ=0.15418nm) of the ferrous phosphate base lithium salts of embodiment 4 preparation.
Fig. 2 is the ferrous phosphate base lithium salts that prepared by the embodiment 4 charging and discharging curve figure as the lithium rechargeable battery of positive active material preparation.
[embodiment]
The following examples will the present invention is described further, but can not be interpreted as it is qualification to protection range of the present invention.
[embodiment 1]
With 0.32 mole of phosphoric acid lithium, 1 mole of ferrous oxalate and 0.66 mole of phosphoric acid and 7.37 gram sucrose mix, ball milling is dry after 3 hours, be under 3 liters/minute the nitrogen atmosphere at flow velocity, make the gained mixture be warming up to 60 ℃ with 3 ℃/minute heating rates, kept 28 hours in this temperature, reduce to room temperature, then mixture is pressed into the thin slice of the thick 3mm of diameter 15mm under the pressure of 3MPa, then under flow velocity is 3 liters/minute nitrogen atmosphere, with 3 ℃/minute heating rates described thin slice is warming up to 550 ℃ and kept 45 hours, reduce to room temperature then, obtain ferrous phosphate base lithium salts according to the inventive method.The tap density of products obtained therefrom is as shown in table 1.The method of measuring tap density is GB GB5162-85.
[embodiment 2]
With 0.98 mole of phosphoric acid dihydro lithium, 1 mole of ferrous oxalate and 0.4 mole of phosphoric acid and 31.35 gram sucrose mix, ball milling is dry after 3 hours, be under 3 liters/minute the nitrogen atmosphere at flow velocity, make the gained mixture be warming up to 225 ℃ with 8 ℃/minute heating rates, kept 13 hours in this temperature, reduce to room temperature, then mixture is pressed into the thin slice of the thick 3mm of diameter 15mm under the pressure of 7MPa, then under flow velocity is 3 liters/minute nitrogen atmosphere, with 6 ℃/minute heating rates described thin slice is warming up to 680 ℃ and kept 25 hours, reduce to room temperature then, obtain ferrous phosphate base lithium salts according to the inventive method.The tap density of products obtained therefrom is as shown in table 1.
[embodiment 3]
With 1.3 mole of phosphoric acid lithiums, 1 mole of ferrous oxalate and 0.2 mole of phosphoric acid and 6.5 gram carbon black (China Rubber Group Carbon Black Research ﹠ Design Institute's commodity, the trade mark is the V7 carbon black) mix, ball milling is dry after 3 hours, be under 3 liters/minute the nitrogen atmosphere at flow velocity, make the gained mixture be warming up to 450 ℃ with 10 ℃/minute heating rates, kept 5 hours in this temperature, reduce to room temperature, then mixture is pressed into the thin slice of the thick 3mm of diameter 15mm under the pressure of 10MPa, then under flow velocity is 3 liters/minute nitrogen atmosphere, with 8 ℃/minute heating rates described thin slice being warming up to 850 ℃ kept 10 hours, reduce to room temperature then, obtain ferrous phosphate base lithium salts according to the inventive method.The tap density of products obtained therefrom is as shown in table 1.
[embodiment 4]
With 0.34 mole of phosphoric acid lithium, 1 mole of ferrous oxalate and 0.66 mole of phosphoric acid and 10 gram sucrose mix, ball milling is dry after 3 hours, be under 3 liters/minute the nitrogen atmosphere at flow velocity, make the gained mixture be warming up to 400 ℃ with 3 ℃/minute heating rates, kept 10 hours in this temperature, reduce to room temperature, then mixture is pressed into the thin slice of the thick 3mm of diameter 15mm under the pressure of 4MPa, then under flow velocity is 3 liters/minute hydrogen atmosphere, with 3 ℃/minute heating rates described thin slice is warming up to 650 ℃ and kept 15 hours, reduce to room temperature then, obtain ferrous phosphate base lithium salts according to the inventive method.The tap density of products obtained therefrom is as shown in table 1.
The XRD figure of present embodiment products obtained therefrom proves that this product is the ferrous phosphate crystalline lithium as shown in Figure 1.The test result of other embodiment and Comparative Examples products therefrom is consistent with embodiment 4, does not therefore provide its concrete XRD figure.
[embodiment 5]
With 0.51 mole of lithium carbonate, 0.99 mole of phosphoric acid is ferrous and 0.1 mole of phosphoric acid and 10 gram sucrose mixing, ball milling is dry after 3 hours, be under 3 liters/minute the nitrogen atmosphere at flow velocity, make the gained mixture be warming up to 400 ℃ with 3 ℃/minute heating rates, kept 10 hours in this temperature, reduce to room temperature, then mixture is pressed into the thin slice of the thick 3mm of diameter 15mm under the pressure of 4MPa, then under flow velocity is 3 liters/minute nitrogen atmosphere, with 3 ℃/minute heating rates described thin slice is warming up to 650 ℃ and kept 15 hours, reduce to room temperature then, obtain ferrous phosphate base lithium salts according to the inventive method.The tap density of products obtained therefrom is as shown in table 1.
[embodiment 6]
1 mole of phosphoric acid dihydro lithium and 1 mole of ferrous oxalate and 10 gram sucrose are mixed, ball milling is dry after 3 hours, be under 3 liters/minute the nitrogen atmosphere at flow velocity, make the gained mixture be warming up to 400 ℃ with 3 ℃/minute heating rates, kept 10 hours in this temperature, reduce to room temperature, then mixture is pressed into the thin slice of the thick 3mm of diameter 15mm under the pressure of 4MPa, then under flow velocity is 3 liters/minute hydrogen atmosphere, with 3 ℃/minute heating rates described thin slice being warming up to 650 ℃ kept 15 hours, reduce to room temperature then, obtain ferrous phosphate base lithium salts according to the inventive method.The tap density of products obtained therefrom is as shown in table 1.
[Comparative Examples 1]
With 0.5 mole of lithium carbonate, 1 mole of ferrous oxalate and 1 mole of phosphoric acid hydrogen ammonium and 10 gram sucrose mix, ball milling was dried after 3 hours, be under 3 liters/minute the nitrogen atmosphere at flow velocity, rise to 400 ℃ with 3 ℃/minute, kept 10 hours, rise to 650 ℃ with 3 ℃/minute speed again and kept 15 hours in this temperature, reduce to room temperature then, obtain according to the ferrous phosphate base lithium salts that does not comprise the control methods of compressing tablet step.The tap density of products obtained therefrom is as shown in table 1.
[performance test]
The preparation of positive plate: get ferrous phosphate base lithium that the foregoing description 1-6 and Comparative Examples 1 obtain as positive active material (LFP), with itself and bonding agent polyvinylidene fluoride (PVDF), conductive agent carbon black, solvent N-methyl pyrrolidone (NMP) with LFP: carbon black: PVDF: NMP=80: 15: 5: 50 weight ratio mixes makes slurry, vacuum drying, then under the pressure of 4MPa, be on the nickel screen of 15mm mixture to be pressed into pie at diameter, make the positive plate that button cell is used.
The preparation of electrolyte: in ethylene carbonate (EC): the ratio of diethyl carbonate (DEC)=1: 1 is made solvent, adds LiPF
6Forming concentration is the electrolyte of 1mol/l.
Form battery battery core with above-mentioned positive plate and to electrode metal lithium sheet and polypropylene diaphragm paper, add electrolyte, make CR2016 type button cell, its nominal capacity is 140mAh.
The button cell of preparation is discharged and recharged experiment with the 0.1C electric current between 2.7-4.0V, obtain discharge capacity.Can calculate the reversible specific capacity of sample according to experimental result, the result is as shown in table 1.This test process and method specifically describe as follows:
The battery that embodiment and Comparative Examples are made is under 25 ℃, and with the current value of 0.1C (14mA), initial charge is to voltage 4.0V.Then, being discharged to voltage with the current value of 0.1C is 2.7V.The initial stage reversible capacity of positive active material can obtain according to following account form (weight of supposing the positive pole of given size is W, positive active material: binding agent: conductive agent=1: X: Y):
Initial stage reversible capacity=(discharge capacity of above-mentioned test)/{ W * [1/ (1+x+y)] }
Wherein the ferrous phosphate base lithium salts that is made by embodiment 4 as the charging and discharging curve figure of the lithium rechargeable battery of positive active material preparation as shown in Figure 2.
The tap density and the chemical property of each embodiment positive electrode of table 1
| The mol ratio of Li: Fe: P | The content of conductive agent | The pressure of compressing tablet step | *Tap density (g/cm 3) | Reversible specific capacity (mAh/g) | |
| Embodiment 1 | 0.96∶1∶1 | 3％ | 3MPa | 1.42 | 143.25 |
| | 0.98∶1∶1.38 | 11％ | 7MPa | 1.75 | 146.02 |
| Embodiment 3 | 1.3∶1∶1.5 | 23％ | 10MPa | 1.73 | 146.50 |
| Embodiment 4 | 1.02∶1∶1 | 5％ | 4MPa | 1.55 | 144.12 |
| Embodiment 5 | 1.02∶1∶1 | 5％ | 4MPa | 1.68 | 145.18 |
| Embodiment 6 | 1∶1∶1 | 5％ | 4MPa | 1.76 | 146.81 |
| Comparative Examples 1 | 1∶1∶1 | 4％ | No compressing tablet step | 1.05 | 130.09 |
*The tap density of product LiFePO 4.
By table 1 data as can be known, according to the ferrous phosphate base lithium that the inventive method makes, its tap density and electrical property are improved with respect to Comparative Examples 1.The raising of tap density promptly is to have improved the capacitance that the positive electrode unit volume is loaded, and has improved the charge/discharge capacity of lithium rechargeable battery.
Therefore, no matter the anode active material of lithium ion secondary battery ferrous phosphate base lithium salts synthetic by the inventive method is that tap density or all synthetic than the conventional method material of the same race of chemical property have had tangible improvement, thereby can prepare the electric core of high-volume and capacity ratio.Make the practical application of ferrous phosphate base lithium salts become possibility.
Claims (16)
1. the preparation method of an anode active material of lithium ion secondary battery ferrous phosphate base lithium salts is characterized in that this method comprises the steps:
(1) lithium compound, iron compound, phosphorus compound are mixed;
(2) step (1) gained mixture being carried out compressing tablet handles;
(3) material behind step (2) the gained compressing tablet is carried out high-temperature roasting in inertia or reducing atmosphere, and in inertia or reducing atmosphere protection, reduce to room temperature naturally.
2. the method for claim 1, the wherein Li in lithium compound, iron compound and the phosphorus compound described in the step (1): the mol ratio of Fe: P is (0.95-1.3): 1: (1-1.5).
3. the method for claim 1, wherein said lithium compound are at least a in lithium carbonate, lithium nitrate, lithium hydroxide, lithium oxalate, lithium acetate, lithium phosphate, lithium hydrogen phosphate, the lithium dihydrogen phosphate.
4. method as claimed in claim 3, wherein said lithium compound are lithium phosphate, lithium hydrogen phosphate or lithium dihydrogen phosphate.
5. the method for claim 1, wherein said iron compound are at least a in ferrous oxalate, ferrous phosphate, the ferrous oxide.
6. the method for claim 1, wherein said phosphorus compound are at least a in phosphoric acid, lithium phosphate, lithium hydrogen phosphate, lithium dihydrogen phosphate and the ferrous phosphate.
7. the method for claim 1 wherein adopts lithium phosphate, lithium hydrogen phosphate or lithium dihydrogen phosphate as the lithium source and the phosphorus source of mixing.
8. the method for claim 1 wherein in the blend step of step (1), also comprises adding a kind of conductive agent.
9. method as claimed in claim 8, wherein said conductive agent are at least a in sucrose, carbon black, metal nano level powder and the acetylene black, and the consumption of conductive agent is the 1-25 weight % of step (1) gained mixture total weight amount.
10. the method for claim 1, wherein this method also is included in and carries out described step (2) is carried out step (1) gained mixture heat pre-treatment before in inertia or reducing atmosphere step.
11. method as claimed in claim 10, the condition of wherein said heat pre-treatment are to handle 5-30 hour under less than 500 ℃ temperature at 50 ℃.
12. method as claimed in claim 11, the condition of wherein said heat pre-treatment are to be warming up to 50 ℃ with 1-10 ℃/minute heating rate to keep this temperature then 5-30 hour to the temperature less than 500 ℃.
13. as claim 1 or 10 described methods, wherein said inertia or reducing atmosphere are the atmosphere that contains at least a gas in hydrogen, nitrogen, argon gas, carbon monoxide and the carbon dioxide.
14. the method for claim 1, wherein the pressure of the processing of compressing tablet described in the step (2) is 2.5-11MPa.
15. the method for claim 1, wherein the condition of high-temperature roasting described in the step (3) is to handle 8-48 hour under 500-900 ℃ temperature.
16. method as claimed in claim 15, wherein the condition of high-temperature roasting described in the step (3) is to be warming up to 500-900 ℃ with 1-10 ℃/minute heating rate to keep this temperature then 8-48 hour.
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101850957A (en) * | 2010-05-21 | 2010-10-06 | 西安交通大学 | Method for preparing nano-lithium iron phosphate of cathode material of lithium ion battery |
| CN101200422B (en) * | 2006-12-15 | 2011-05-25 | 比亚迪股份有限公司 | Method for preparing lithium iron phosphate ferrous oxalate |
| CN101376626B (en) * | 2007-08-28 | 2011-05-25 | 比亚迪股份有限公司 | Preparation of iron oxalate hydrous salt crystal |
| CN101407318B (en) * | 2007-10-11 | 2012-05-02 | 比亚迪股份有限公司 | Method for preparing active substance lithium iron phosphate for lithium ion secondary battery anode |
| CN102969487A (en) * | 2012-11-23 | 2013-03-13 | 南开大学 | Carbon-sulfur composite material used for positive pole of lithium-sulfur battery and preparation method of material |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TW513822B (en) * | 2000-10-06 | 2002-12-11 | Sony Corp | Method for producing cathode active material and method for producing non-aqueous electrolyte cell |
| CN1401559A (en) * | 2002-10-18 | 2003-03-12 | 北大先行科技产业有限公司 | Method for preparing ferrous lithium phosphate, and lithium ion cell therewith |
| CN1233054C (en) * | 2003-12-17 | 2005-12-21 | 北京科技大学 | Method for preparing LiFeP04 material by microwave method |
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2005
- 2005-01-28 CN CNB2005100029000A patent/CN100418252C/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101200422B (en) * | 2006-12-15 | 2011-05-25 | 比亚迪股份有限公司 | Method for preparing lithium iron phosphate ferrous oxalate |
| CN101376626B (en) * | 2007-08-28 | 2011-05-25 | 比亚迪股份有限公司 | Preparation of iron oxalate hydrous salt crystal |
| CN101407318B (en) * | 2007-10-11 | 2012-05-02 | 比亚迪股份有限公司 | Method for preparing active substance lithium iron phosphate for lithium ion secondary battery anode |
| CN101850957A (en) * | 2010-05-21 | 2010-10-06 | 西安交通大学 | Method for preparing nano-lithium iron phosphate of cathode material of lithium ion battery |
| CN102969487A (en) * | 2012-11-23 | 2013-03-13 | 南开大学 | Carbon-sulfur composite material used for positive pole of lithium-sulfur battery and preparation method of material |
| CN102969487B (en) * | 2012-11-23 | 2014-09-03 | 南开大学 | Carbon-sulfur composite material used for positive pole of lithium-sulfur battery and preparation method of material |
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| CN100418252C (en) | 2008-09-10 |
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