CN105261784B - A kind of aluminum secondary battery - Google Patents

A kind of aluminum secondary battery Download PDF

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Publication number
CN105261784B
CN105261784B CN201410336027.8A CN201410336027A CN105261784B CN 105261784 B CN105261784 B CN 105261784B CN 201410336027 A CN201410336027 A CN 201410336027A CN 105261784 B CN105261784 B CN 105261784B
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barium oxide
secondary battery
collector
aluminum secondary
anode
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CN105261784A (en
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白莹
吴锋
吴川
陈实
王华丽
吴伯荣
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Beijing Institute of Technology BIT
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Beijing Institute of Technology BIT
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
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    • Y02E60/10Energy storage using batteries

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Abstract

The invention discloses a kind of aluminum secondary batteries, the aluminum secondary battery includes anode, cathode, electrolyte and diaphragm, the anode is the combination for growing barium oxide and collector on a current collector, the preparation method of the anode obtains vanadium ion solution the following steps are included: (1) dissolves vfanadium compound;(2) vanadium ion solution and collector are subjected in closed container hydro-thermal reaction, reaction product is cleaned and is dried in vacuo after reaction, obtain combination.The anode of aluminum secondary battery of the invention, the barium oxide growth of nanoparticle structure is on a current collector, so that not only having electrical contact well between the two, addition conductive agent and binder are not needed, and it is capable of increasing the surface area of barium oxide electrode material, the contact area of electrode material and electrolyte is improved, meanwhile, aluminum secondary battery of the invention specific discharge capacity with higher and excellent stable circulation performance.

Description

A kind of aluminum secondary battery
Technical field
The present invention relates to aluminum secondary battery fields, and in particular, to a kind of aluminum secondary battery.
Background technique
Advanced high-energy density secondary battery is effective to the development of next-generation electric car and renewable energy power generation Using being vital.In recent years, the novel green secondary cell research based on new system, new material, new technology is constantly deep Change, by constructing for light element polyelectron reaction system, is expected that secondary cell is made to obtain energy more higher than conventional single electron system Metric density.Aluminium is the most abundant metallic element of content on the earth, it has many advantages, such as light weight, pollution-free, cheap, because of it Three electron transfer reactions can occur, theoretical electrochemistry specific capacity reaches 2980mAh/g, is only second to lithium in all metallic elements (3870mAh/g)。
Since aluminium is a kind of very active metal, standard electrode potential is -1.68V, is lower than standard hydrogen-evolution overpotential, because This aluminium ion is difficult to restore in aqueous solution, can generate strong evolving hydrogen reaction.So the electrolytic deposition and aluminium in aluminium are secondary In the research and application of battery, non-aqueous solution electrolysis plastidome is generallyd use.And aluminium is easy film forming in neutral and organic electrolyte And be passivated, lead to that electrode potential is substantially less than theoretical value and voltage behavior obviously lags, therefore aluminium is never successfully applied In electrochemical energy storage and switch technology.In the 1970s, it is found that electrochemistry can occur in molten salt electrolyte for aluminium Deposition, then using the aluminium electrode preparation research electrochemical behavior of secondary molten salt battery.Compared with aqueous electrolyte, fused salt tool There is the features such as conductivity is high, and decomposition potential is high, and polarizability is low, the high-temperature molten salt aluminum secondary battery constituted has good reversibility, The features such as theoretical specific energy is big.But high-temperature molten salt battery needs high temperature or to environmental requirement harshness, higher cost and is difficult to safeguard, Limit the development of aluminum secondary battery.
Ionic liquid at room temperature is the substance being made of ion being in a liquid state at a temperature of room temperature or near room temperature, generally by having Machine cation and inorganic anion composition.It not only has very low vapour pressure, has good dissolution to organic matter, inorganic matter Property, and thermal stability and good flame resistance, also there is good ionic conductivity, stable electrochemical window is expected to become one kind Safe and efficient secondary cell electrolyte.So far, ionic liquid has been widely studied as lithium-ion battery electrolytes. It is nearest the study found that aluminum chloride type ionic liquid can be good at being used in aluminum secondary battery as electrolyte, make room temperature aluminium The exploitation of secondary cell is possibly realized with application.The electrolyte being related in reported aluminum secondary battery is mainly aluminum chloride type Ionic liquid, including AlCl3/[EMIM]Cl、AlCl3/ [BMIM] Cl and AlCl3/ [BMIM] Br etc..Aluminum chloride type ionic liquid The characteristics of be itself contain aluminium ion, and form with the ratio of aluminium chloride and imidazolium halide salt change and change, already exist It is studied in the electrolytic deposition field of aluminium.Metallic aluminium can only be deposited from acid melt, because of AlCl4 -With high degree of symmetry Tetrahedral structure, electrochemically stable, the electrodeposition efficiency of aluminium is low.And Al in acid melt2Cl7 -Due to the asymmetry of its structure Property, electro-chemical activity is high, being capable of effectively electric deposition aluminum.But the Al in acid chlorization aluminium profiles ionic liquid2Cl7 -Can with it is common Binder PVDF reaction, therefore the ionic liquid of the type should not be used in the battery constituted using PVDF as the electrode of binder.
Barium oxide is the typical embedded type compound with layer structure, because it is high with theoretical specific capacity, resource is rich Rich, lower-price characteristic, becomes one of lithium ion battery electrode material of new generation.Recent studies have found that it is used as the secondary electricity of aluminium The insertion reaction of aluminium, specific discharge capacity with higher can occur for pond positive electrode.Cornell University Jayaprakash et al. will The barium oxide nano wire of hydro-thermal reaction synthesis is as positive electrode, by AlCl3With the molar ratio of [EMIm] Cl be 1.1:1 from Sub- liquid constitutes secondary aluminium ion battery as electrolyte, using metallic aluminium as cathode.Constant current charge-discharge survey is carried out to battery Examination, as a result, it has been found that, open-circuit voltage 1.8V, discharge voltage plateau is basically stable at 0.55V, and specific discharge capacity is within first week 305mAh/g.But when preparing anode electrode, barium oxide nano wire needs to add conductive agent, with binder mixed pulp Coated on anode electrode can just be prepared on collector, on the one hand, the adhesive property and electric conductivity of binder are to be improved, And the wellability of acid chlorization aluminium profiles il electrolyte is poor, it is incompatible with binder, be unfavorable for barium oxide nano wire with Electrical contact between conducting base is also unfavorable for keeping the stability of anode electrode;On the other hand, the barium oxide nano wire Conductivity is very low so that ion telescopiny slowly and only one layer of surface participations insertion reaction, be unfavorable for anode electrode and Contact between electrolyte.
Summary of the invention
The purpose of the invention is to overcome acid chlorization aluminium profiles ionic liquid in the aluminum secondary battery of the prior art to be electrolysed Liquid wellability is poor, incompatible with binder, the electrical contact being unfavorable between barium oxide nano wire and conducting base and vanadium oxygen Compound nano wire conductivity is low, is unfavorable for the defect of the contact between anode electrode and electrolyte, and it is secondary to provide a kind of new aluminium Battery all has in the aluminum secondary battery well between barium oxide and conducting base and between anode electrode and electrolyte Electrical contact, and aluminum secondary battery specific discharge capacity with higher and excellent stable circulation performance.
The present inventor has been surprisingly found that under study for action, (leads in the collector with large scale tridimensional network Electric matrix) on using hydro-thermal in-situ deposition barium oxide method (that is, allowing barium oxide directly to synthesize and being deposited on collector On) anode (combination for growing barium oxide and collector on a current collector) for preparing aluminum secondary battery, it can not only The channel for keeping collector netted is conducive to electrolyte and migrates and spread inside it, further increases vanadium oxide positive electrode material Material with the utilization rate of contact and positive electrode between electrolyte, and as the barium oxide of active material with as collector Conducting base between have well electrical contact, do not need to add any conductive agent and binder, and be able to maintain good The stability of anode electrode.Meanwhile so that the aluminum secondary battery being assembled into specific discharge capacity with higher and excellent circulation Stability.
Therefore, to achieve the goals above, the present invention provides a kind of aluminum secondary battery, the aluminum secondary battery includes just Pole, cathode, electrolyte and diaphragm, the anode is the combination for growing barium oxide and collector on a current collector, described Anode preparation method the following steps are included:
(1) vfanadium compound is dissolved, obtains vanadium ion solution;
(2) vanadium ion solution and collector are subjected in closed container hydro-thermal reaction, carry out reaction product after reaction Cleaning and vacuum drying, obtain growing the combination of barium oxide and collector on a current collector.
Aluminum secondary battery of the invention specific discharge capacity with higher and excellent stable circulation performance.
When the present invention prepares anode, by first preparing vanadium ion solution, the method for then using hydro-thermal in-situ deposition, by vanadium For solion heat resolve at the barium oxide nano particle and water of unformed shape, the nanoparticle structure made is grown in collection On fluid, addition conductive agent and binder are not needed, that is, may make not only has electrical contact well between the two, is able to maintain The stability of good anode electrode, and it is capable of increasing the surface area of vanadium oxide positive electrode materials, improve positive electrode and electricity The contact area of liquid is solved, diffusion length needed for shortening aluminium ion and electronics, so as to improve the specific discharge capacity of battery, and Improve its stable circulation performance.In a preferred embodiment of the invention, by the combination obtained after vacuum drying into Row heat treatment (condition of heat treatment includes: that temperature is 300-600 DEG C, time 1-6h), so that barium oxide is by amorphous state knot Structure turns to crystalline structure, is conducive to the raising of barium oxide crystallinity, can further increase the specific discharge capacity of battery and follow Ring stability.Meanwhile hydro-thermal reaction is carried out in closed container, it carries out reaction under relatively high temperature and pressure, reacts The viscosity of fast speed, hydrothermal solution is low compared with the viscosity under normal temperature and pressure, and the diffusion of reactive component is very fast, and crystal growth interface is attached Close diffusion region is narrower, is more advantageous to the growth of crystal.
Other features and advantages of the present invention will the following detailed description will be given in the detailed implementation section.
Detailed description of the invention
Fig. 1 is the XRD spectrum of barium oxide prepared by the embodiment of the present invention 1.
Fig. 2 is the SEM picture before vanadium oxide positive electrode materials calcining prepared by the embodiment of the present invention 1.
Fig. 3 is the calcined SEM picture of vanadium oxide positive electrode materials prepared by the embodiment of the present invention 1.
Fig. 4 is the calcined SEM picture of vanadium oxide positive electrode materials prepared by the embodiment of the present invention 2.
Fig. 5 is the calcined SEM picture of vanadium oxide positive electrode materials prepared by the embodiment of the present invention 3.
Fig. 6 is the calcined SEM picture of vanadium oxide positive electrode materials prepared by the embodiment of the present invention 4.
Specific embodiment
Detailed description of the preferred embodiments below.It should be understood that described herein specific Embodiment is merely to illustrate and explain the present invention, and is not intended to restrict the invention.
The present invention provides a kind of aluminum secondary battery, which includes anode, cathode, electrolyte and diaphragm, In, anode is the combination for growing barium oxide and collector on a current collector, and the preparation method of the anode includes following Step:
(1) vfanadium compound is dissolved, obtains vanadium ion solution;
(2) vanadium ion solution and collector are subjected in closed container hydro-thermal reaction, carry out reaction product after reaction Cleaning and vacuum drying, obtain growing the combination of barium oxide and collector on a current collector.
In aluminum secondary battery of the invention, when preparing anode, in step (1), under preferable case, vfanadium compound is dissolved Method includes: under stiring, the solution that can dissolve vfanadium compound to be added in vfanadium compound, and the time of stirring is 0.5-3h. It will be understood by those skilled in the art that the solution that can dissolve vfanadium compound can if vfanadium compound can be dissolved in water Think water;If vfanadium compound is not soluble in water, described can to dissolve the solution of vfanadium compound can be aqueous hydrogen peroxide solution, grass Aqueous acid, aqueous hydrochloric acid solution or ammonia spirit.Therefore, the solution that can dissolve vfanadium compound can be water, aquae hydrogenii dioxidi Solution, oxalic acid aqueous solution, aqueous hydrochloric acid solution or ammonia spirit.For aqueous hydrogen peroxide solution, oxalic acid aqueous solution, aqueous hydrochloric acid solution Or there is no particular limitation for the concentration of ammonia spirit, as long as vfanadium compound can be dissolved, in order to preferably dissolve vanadium Compound, under preferable case, the concentration of aqueous hydrogen peroxide solution is 15-30 weight %, and the concentration of oxalic acid aqueous solution is 5-12.5 Weight %, the concentration of aqueous hydrochloric acid solution are 15-37 weight %, and the concentration of ammonia spirit is 15-28 weight %.In vfanadium compound Prepared energy can be added when can dissolve solution (in the case where being not water, such as the oxalic acid solution) of vfanadium compound in addition The aqueous solution (such as oxalic acid aqueous solution) for enough dissolving vfanadium compound, can also be separately added into water and can dissolve the substance of vfanadium compound (such as oxalic acid).
In aluminum secondary battery of the invention, when preparing anode, the present inventor has found under study for action, uses peroxidating When aqueous solution of hydrogen dissolves vfanadium compound, the time of stirring has an impact to the deposition of barium oxide on collector, mixing time mistake It is long, the deposition of barium oxide on collector can be reduced, this may be because with stirring progress, hydrogen peroxide light-exposed and Having and is constantly catalytically decomposed in the presence of barium oxide, long agitation decomposes excessive hydrogen peroxide completely, and The pervanadic acid of generation is unstable, will be slow resolve into vanadic anhydride and oxygen at room temperature, eventually leads to vanadic anhydride analysis Out, vanadium ion solution concentration reduces, to reduce barium oxide in the deposition of collection liquid surface.In the case of it is therefore preferable that, stir The time mixed is 0.5-3h.
In aluminum secondary battery of the invention, when preparing anode, in step (1) when dissolution vfanadium compound, water is preferably Deionized water.For the method for stirring, there is no particular limitation, can be the method for various stirrings commonly used in the art, such as can Think electric stirring, magnetic agitation, glass bar stirring etc., under preferable case, the method for stirring is magnetic agitation.For stirring There is no particular limitation for speed, as long as vfanadium compound can be made to dissolve, such as can be 100-300rpm.For dissolving vanadium There is no particular limitation for temperature when compound, can be 10-40 DEG C.
In aluminum secondary battery of the invention, when preparing anode, for vfanadium compound, there is no particular limitation, can be this The common various vfanadium compound in field.Under preferable case, vfanadium compound is vanadic anhydride, vanadium dioxide, vanadium trioxide, grass One of sour vanadium, vanadyl oxalate and ammonium metavanadate are a variety of.
In aluminum secondary battery of the invention, when preparing anode, the present inventor is under study for action it has furthermore been found that work as The solution that can dissolve vfanadium compound being added is aqueous hydrogen peroxide solution, oxalic acid aqueous solution, aqueous hydrochloric acid solution or ammonia spirit When equal aqueous solutions, increase the amount that can dissolve the solute in the aqueous solution of vfanadium compound, allows to dissolve the water-soluble of vfanadium compound Solute in liquid is conducive to barium oxide in the uniform deposition of collection liquid surface relative to vfanadium compound excess.It is therefore preferable that feelings Under condition, vfanadium compound with can dissolve solute in the aqueous solution of vfanadium compound molar ratio be 1:5-25, further preferably 1: 10-24。
In aluminum secondary battery of the invention, prepare anode when, the present inventor under study for action it has furthermore been found that with Vanadium meter, when the concentration of the vanadium ion solution obtained in step (1) is 0.03-0.3mol/L, preferably 0.05-0.15mol/L, Be conducive to barium oxide in the uniform deposition of collection liquid surface.Therefore, when water is added in vfanadium compound, vfanadium compound is controlled With the amount of the water of addition, so that in terms of vanadium, the concentration of vanadium ion solution is 0.03-0.3mol/L, preferably 0.05-0.15mol/ L;When addition can dissolve aqueous solution (such as aqueous hydrogen peroxide solution, oxalic acid aqueous solution, the hydrochloric acid of vfanadium compound in vfanadium compound Aqueous solution or ammonia spirit) when, control vfanadium compound and the molar ratio that can dissolve solute in the aqueous solution of vfanadium compound are 1: 5-25, preferably 1:10-24, and the total volume of last solution is controlled, so that the concentration of vanadium ion solution is 0.03- in terms of vanadium 0.3mol/L, preferably 0.05-0.15mol/L.
In aluminum secondary battery of the invention, when preparing anode, collector plays the effect of conducting base, for collector There is no particular limitation, can be various collectors commonly used in the art.Under preferable case, collector be nickel foam, foam copper, Titanium foam, foam iron-nickel, stainless (steel) wire or carbon cloth.
In aluminum secondary battery of the invention, when preparing anode, for closed container, there is no particular limitation, can be for not With the various containers of vanadium ion solution reaction, such as can be polytetrafluoroethyllining lining stainless steel cauldron.
In aluminum secondary battery of the invention, when preparing anode, in order to be more advantageous to barium oxide in collection liquid surface Uniform deposition, under preferable case, the mass ratio of vanadium ion solution and collector is 200:1-10:1, further preferably 100:1- 20:1.The present inventor has found under study for action, as above controls the amount of the vanadium ion solution and collector in closed container, energy Enough make the deposition 1-30mg/cm of barium oxide on a current collector2, preferably 2-10mg/cm2
In aluminum secondary battery of the invention, when preparing anode, in order to keep hydro-thermal reaction more abundant, it is more advantageous to vanadium oxygen Compound is in the uniform deposition of collection liquid surface, and under preferable case, the condition of hydro-thermal reaction includes: that heating temperature is 180-205 DEG C, Heating time is 1-4 days.
In aluminum secondary battery of the invention, when preparing anode, in order to remove the water-solubility impurity and oil in reaction product Solubility impurity, under preferable case, the condition of cleaning includes: to be respectively washed reaction product with deionized water and organic solvent.For It is not particularly limited, can first be cleaned with deionized water with the sequence that deionized water and organic solvent clean, it can also be first with having Solvent cleaning.For organic solvent, there is no particular limitation, can be can to remove each of oil soluble impurity in reaction product Kind organic solvent, such as can be dehydrated alcohol.For the number of cleaning, there is no particular limitation, produces as long as reaction can be removed Water-solubility impurity and oil soluble impurity in object, such as can be 3-5 times.
In aluminum secondary battery of the invention, when preparing anode, under preferable case, vacuum drying condition includes: drying Temperature is 60-80 DEG C, drying time 12-24h.
In aluminum secondary battery of the invention, when preparing anode, in order to turn the amorphous structure of barium oxide preferably It to crystalline structure and is formed in active material barium oxide on collector strongerly, and further increases putting for battery Electric specific capacity and cyclical stability, under preferable case, the method for preparing anode further includes that the combination for obtaining step (2) carries out Heat treatment, it is further preferred that it is 300-600 DEG C that the condition of heat treatment, which includes: temperature, time 1-6h.Wherein, heat treatment Mode may include calcining in air or nitrogen or argon gas.
In aluminum secondary battery of the invention, when preparing anode, before heat treatment, what the present invention was prepared is grown in collection Barium oxide on fluid is the barium oxide (VO of undefined structureX, X 1.9-2.5), it may be possible to vanadic anhydride, dioxy Change one of vanadium, vanadium trioxide and vanadium oxide or a variety of mixtures;After heat treatment, barium oxide is by amorphous structure Crystalline structure is turned to, the barium oxide particle of high-crystallinity is obtained.
In aluminum secondary battery of the invention, cathode can be the various negative electrode materials that can be used in assembling aluminum secondary battery, It such as can be metallic aluminium or aluminium alloy.For the form of metal aluminum or aluminum alloy, there is no particular limitation, can be common Various forms, in order to make battery be easier to process, under preferable case, the form of metal aluminum or aluminum alloy be powder, silk, net, piece or Foam.
In aluminum secondary battery of the invention, for diaphragm, there is no particular limitation, can be for for assembling aluminum secondary battery Various diaphragms, in order to improve the wellability of ionic liquid, under preferable case, diaphragm is fibreglass diaphragm.
In aluminum secondary battery of the invention, under preferable case, electrolyte is the ionic liquid of aluminium containing salt, including by aluminum halide Halogen aluminic acid ionic liquid is formed by with any one in quaternary ammonium salt, quaternary alkylphosphonium salt, season sulfosalt, imidazolium halide salt and pyridinium halide salt Body, or including by BF containing anion4 -、PF6 -、CF3SO3 -Or TFSI-Imidazoles, pyridine, in piperidines and pyrrolidinium ion liquid There is the aluminium salt of identical anion to be formed by il electrolyte for any one dissolution.It is further preferred that electrolyte is The chlorine Ion-selective electrod that aluminium chloride and imidazolium halide salt are formed, wherein the molar ratio of aluminium chloride and imidazolium halide salt is 1- 1.5:1 more preferably 1.1:1;Still further preferably, electrolyte AlCl3/[BMIM]Cl、AlCl3/[EMIM]Cl、 AlCl3/ [BMIM] Br and AlCl3Any one in/[EMIM] Br.Present inventor has found under study for action, is preparing aluminium When secondary cell, when the imidazolium halide salt in electrolyte is appointing in [BMIM] Cl, [EMIM] Cl, [BMIM] Br and [EMIM] Br When anticipating a kind of, imidazolium halide salt such as chlorination 1- amyl -3- methylimidazole ([PMIM] Cl), the trialkyl replaced with long-chain replaces Imidazolium halide salt such as chlorination 1- butyl -2,3- methylimidazole ([BDiMIM] Cl) is compared, and the viscous of electrolyte can be substantially reduced Degree, raising conductivity significantly improve the electrochemistry of aluminum secondary battery to significantly improve the wellability of electrolyte and electrode material Performance.
In aluminum secondary battery of the invention, for the shape of the aluminum secondary battery being assembled into, there is no particular limitation, can be with For those skilled in the art it is conceivable that various shape, such as aluminum secondary battery can be button cell or cylindrical battery.
In the present invention, for the preparation method of aluminum secondary battery, there is no particular limitation, can be commonly used in the art each Kind preparation method, for example, using the combination of the barium oxide and collector that grow on a current collector as anode, metallic aluminium conduct Cathode, acid chlorization aluminium profiles ionic liquid can be assembled into argon gas glove box as electrolyte using fibreglass diaphragm Aluminum secondary battery.For the specific method of assembling, there is no particular limitation, can be various methods commonly used in the art, herein not It repeats again.
Embodiment
The present invention is further illustrated for embodiment below, but is not intended to limit the present invention.
In following embodiment, being scanned the scanning electron microscope used when Electronic Speculum observation is field emission scanning electron microscope (Hitachi Hitachi S-4800)。
Using the structural form of Rigaku DMAX2400 type X-ray diffractometer characterization barium oxide.
Using inductive coupling plasma emission spectrograph (Profile, Leeman company, the U.S.) analysis barium oxide Element composition.
Vanadium pentoxide powder, oxalic acid, vanadyl oxalate powder and ammonium metavanadate powder are purchased from Chinese medicines group chemical reagent Beijing Co., Ltd.
Fibreglass diaphragm is Whatman glass fiber filter paper GF/C (1822-047).
The measuring method of the deposition of barium oxide on a current collector are as follows: weigh the quality of collector before hydro-thermal reaction respectively With vacuum drying/calcined collector for being deposited with barium oxide quality, the quality difference value of the two and collector it is apparent (by taking embodiment 1 as an example, the apparent area of every nickel foam is 3 × 4cm to area2) ratio be barium oxide on a current collector Deposition.
Embodiment 1
The present embodiment is for illustrating aluminum secondary battery of the invention.
30ml deionized water is added at 25 DEG C in 0.364g vanadium pentoxide powder and passes through magnetic agitation (150rpm) It is mixed, aqueous hydrogen peroxide solution (vanadic anhydride and the hydrogen peroxide of 5ml30 weight % is added while magnetic agitation Molar ratio be 1:22), continuation stirs 0.5h at 150rpm, and obtaining concentration is that the transparent of 0.11mol/L orange red crosses vanadium Acid solution (concentration is in terms of vanadium).Then obtained pervanadic acid solution all (36.1g) is transferred to 50ml polytetrafluoroethyllining lining Stainless steel cauldron in, be added four 3 × 4cm2Nickel foam (aperture 110PPI, thickness 1mm, every quality is 0.4g), Heating reaction 3 days, are cooled to 25 DEG C after completion of the reaction at 190 DEG C, take out reaction product and are first washed 2 times with dehydrated alcohol, then It is washed with deionized 2 times, it is then 20 hours dry at 70 DEG C in a vacuum drying oven, finally forged at 500 DEG C in air 4h is burnt, the combination for obtaining being grown in barium oxide and nickel foam in nickel foam after the disk that diameter is 1cm is cut into.
After measured, deposition of the barium oxide in nickel foam is 2mg/cm2
The XRD spectrum of barium oxide prepared by embodiment 1 is as shown in Figure 1.Through inductive coupling plasma emission spectrograph (ICP) it tests, and combines Fig. 1 it is found that obtained barium oxide is the barium oxide (VO of undefined structure before heat treatmentX, X For 2.48), it may be possible to one of vanadic anhydride, vanadium dioxide, vanadium trioxide and vanadium oxide or a variety of mixtures;? After being heat-treated in air, the good V of crystallinity has been obtained2O5Particle.
The barium oxide being prepared before embodiment 1 is heat-treated is observed under scanning electron microscope, scanning electron microscope (SEM) photograph (SEM figure) is shown in Fig. 2.From figure 2 it can be seen that the barium oxide that embodiment 1 is prepared before being heat-treated is in Nanoparticulate shape Looks are grown in nickel foam substrate surface, partial size about 400nm.Fig. 3 is the barium oxide being prepared after embodiment 1 is heat-treated SEM figure, from figure 3, it can be seen that the pattern of the barium oxide after heat treatment is preceding almost the same with heat treatment.
It is secondary as aluminium using the combination of the barium oxide being grown in nickel foam being prepared of embodiment 1 and nickel foam Anode, using metal aluminium flake as cathode, with acid chlorization aluminium profiles imidazolium ionic liquid AlCl3/ [BMIM] Cl=1.1:1 (molar ratio) is assembled into aluminium secondary button cell (2025 types using fibreglass diaphragm for electrolyte in argon gas glove box Number).
Embodiment 2
The present embodiment is for illustrating aluminum secondary battery of the invention.
At 25 DEG C, 0.364g vanadium pentoxide powder is weighed according to the ratio that molar ratio is 1:10 and 1.8g oxalic acid directly adds Enter into 72ml deionized water, 3h is persistently stirred by magnetic agitation (200rpm) to transparent dark blue solution is formed, is obtained Concentration is the vanadyl oxalate solution of 0.056mol/L (concentration is in terms of vanadium).Then obtained solution all (74.1g) is transferred to In the stainless steel cauldron of 50ml polytetrafluoroethyllining lining, 3 × 4cm of two panels is added2Foam iron-nickel (aperture 110PPI, thickness 1mm, every quality are 0.4g), it is reacted 4 days in 180 DEG C of heating.It is cooled to 25 DEG C after completion of the reaction, it is first to take out reaction product It is washed 2 times with dehydrated alcohol, then is washed with deionized 2 times, it is then 24 hours dry at 60 DEG C in a vacuum drying oven, finally 6h is calcined at 300 DEG C in argon gas, is cut into diameter to obtain being grown in the barium oxide on foam iron-nickel after the disk of 1cm With the combination of foam iron-nickel.
After measured, deposition of the barium oxide on foam iron-nickel is 6mg/cm2
The barium oxide that embodiment 2 is prepared is through X-ray diffraction and inductive coupling plasma emission spectrograph (ICP) Test, learns, obtained barium oxide is the barium oxide (VO of undefined structure before heat treatmentX, X 1.9), it may be possible to five One of V 2 O, vanadium dioxide, vanadium trioxide and vanadium oxide or a variety of mixtures;After being heat-treated in argon gas, The good barium oxide particle (VO of crystallinity is obtainedX, X 1.9).
The barium oxide that embodiment 2 is prepared is observed under scanning electron microscope, wherein be prepared after heat treatment The SEM figure of barium oxide see Fig. 4, from fig. 4, it can be seen that the barium oxide particle that embodiment 2 is prepared after being heat-treated is in It is flower-shaped to be grown in foam iron-nickel matrix surface, partial size about 3um.It should be noted simultaneously that the vanadium before embodiment 2 is heat-treated aoxidizes Almost the same after the pattern of object and heat treatment, details are not described herein.
The combination of the barium oxide being grown on foam iron-nickel and foam iron-nickel that are prepared using embodiment 2 is as aluminium Anode of secondary battery, using Filamentous aluminium alloy as cathode, with chlorine Ion-selective electrod AlCl3/ [BMIM] Br=1.1:1 (mole Than) it is that electrolyte using fibreglass diaphragm is assembled into the secondary button cell of aluminium (2025 model) in argon gas glove box.
Embodiment 3
The present embodiment is for illustrating aluminum secondary battery of the invention.
At 25 DEG C, 0.702g ammonium metavanadate is weighed according to the ratio that molar ratio is 1:5 and 2.7g oxalic acid is added directly into In 40ml deionized water.1h is persistently stirred by magnetic agitation (150rpm) until forming clear solution, obtaining concentration is (the NH of 0.15mol/L4)2[(VO)2(C2O4)3] solution (concentration is in terms of vanadium).Then by all (43.4g) transfers of obtained solution Into the stainless steel cauldron of 50ml polytetrafluoroethyllining lining, four 3 × 4cm are added2Foam copper (aperture 110PPI, thickness 1mm, every quality are 0.4g), and heating reaction 1 day, is cooled to 25 DEG C after completion of the reaction at 205 DEG C, and it is first to take out reaction product It is washed with deionized 2 times, then washs 2 times with dehydrated alcohol, it is then 12 hours dry at 80 DEG C in a vacuum drying oven, finally Calcine 1h at 600 DEG C in nitrogen, be cut into after the disk that diameter is 1cm obtain being grown in barium oxide on foam copper with The combination of foam copper.
After measured, deposition of the barium oxide on foam copper is 10mg/cm2
The barium oxide that embodiment 3 is prepared is through X-ray diffraction and inductive coupling plasma emission spectrograph (ICP) Test, learns, obtained barium oxide is the barium oxide (VO of undefined structure before heat treatmentX, X 2.17), it may be possible to One of vanadic anhydride, vanadium dioxide, vanadium trioxide and vanadium oxide or a variety of mixtures;It is heat-treated in nitrogen Afterwards, the good barium oxide particle (VO of crystallinity has been obtainedX, X 2.17).
The barium oxide that embodiment 3 is prepared is observed under scanning electron microscope, wherein be prepared after heat treatment The SEM figure of barium oxide see Fig. 5, from fig. 5, it can be seen that the barium oxide particle that embodiment 3 is prepared after being heat-treated is in Palpus shape is grown in foam copper matrix surface.It should be noted simultaneously that the pattern and heat of the barium oxide before the heat treatment of embodiment 3 Almost the same after processing, details are not described herein.
The combination of the barium oxide being grown on foam copper and foam copper that are prepared using embodiment 3 is secondary as aluminium Anode, using net metal aluminium as cathode, with chlorine Ion-selective electrod AlCl3/ [EMIM] Cl=1.5:1 (molar ratio) is Electrolyte is assembled into aluminium secondary circle cylindrical cell (18650 model) using fibreglass diaphragm in argon gas glove box.
Embodiment 4
The present embodiment is for illustrating aluminum secondary battery of the invention.
At 25 DEG C, 40ml deionized water is added in 0.49g vanadyl oxalate powder and is held by magnetic agitation (150rpm) Continuous stirring 2h, obtains the blue vanadium ion solution that concentration is 0.05mol/L (concentration is in terms of vanadium).Then by solution whole (40.49g) is transferred in the stainless steel cauldron of 50ml polytetrafluoroethyllining lining, and four 3 × 4cm are added2Stainless (steel) wire (1000 Mesh, every quality are 0.5g), it is reacted 1 day in 180 DEG C of heating, is cooled to 25 DEG C after completion of the reaction, taken out reaction product and first use Dehydrated alcohol washs 2 times, then is washed with deionized 2 times, then 12 hours dry at 80 DEG C in a vacuum drying oven, finally exists Calcine 6h at 300 DEG C in air, be cut into after the disk that diameter is 1cm obtain being grown in barium oxide on stainless (steel) wire with The combination of stainless (steel) wire.
After measured, deposition of the barium oxide on stainless (steel) wire is 0.5mg/cm2
The barium oxide that embodiment 4 is prepared is through X-ray diffraction and inductive coupling plasma emission spectrograph (ICP) Test, learns, obtained barium oxide is the barium oxide (VO of undefined structure before heat treatmentX, X 1.95), it may be possible to One of vanadic anhydride, vanadium dioxide, vanadium trioxide and vanadium oxide or a variety of mixtures;It is heat-treated in air Afterwards, barium oxide has obtained the good V of crystallinity through oxidation2O5Particle.
The barium oxide that embodiment 4 is prepared is observed under scanning electron microscope, wherein be prepared after heat treatment The SEM figure of barium oxide see Fig. 6, from fig. 6, it can be seen that the barium oxide particle that embodiment 4 is prepared after being heat-treated is in Lamellar growth is in stainless (steel) wire matrix surface.It should be noted simultaneously that embodiment 4 be heat-treated before barium oxide pattern with Almost the same after heat treatment, details are not described herein.
The combination of the barium oxide being grown on stainless (steel) wire and stainless (steel) wire that are prepared using embodiment 4 is as aluminium Anode of secondary battery, using foamed metal aluminium as cathode, with chlorine Ion-selective electrod AlCl3/ [EMIM] Br=1:1 (mole Than) it is that electrolyte using fibreglass diaphragm is assembled into aluminium secondary circle cylindrical cell (18650 model) in argon gas glove box.
Embodiment 5
Anode and battery is prepared according to the method for embodiment 1, unlike, it is water-soluble that 1ml30 weight % hydrogen peroxide is added Liquid (molar ratio of vanadic anhydride and hydrogen peroxide is 1:4.4).
After measured, deposition of the barium oxide in nickel foam is 1mg/cm2
Embodiment 6
Anode and battery is prepared according to the method for embodiment 1, unlike, 100ml is added in vanadium pentoxide powder Deionized water obtains the transparent orange red pervanadic acid solution that concentration is 0.038mol/L (concentration is in terms of vanadium).
After measured, deposition of the barium oxide in nickel foam is 1mg/cm2
Embodiment 7
Anode and battery is prepared according to the method for embodiment 1, unlike, after aqueous hydrogen peroxide solution is added, continue to stir Mix 4h.
After measured, deposition of the barium oxide in nickel foam is 1mg/cm2
Embodiment 8
Anode and battery is prepared according to the method for embodiment 1, unlike, it is 1cm that 4 areas, which are added,2Nickel foam disk (aperture 110PPI, thickness 1mm, every quality is 0.03g).
After measured, deposition of the barium oxide in nickel foam is 20mg/cm2
Embodiment 9
Anode and battery is prepared according to the method for embodiment 1, unlike, it is added after nickel foam and is heated instead at 190 DEG C Answer 12h.
After measured, deposition of the barium oxide in nickel foam is 0.5mg/cm2
Embodiment 10
Anode and battery is prepared according to the method for embodiment 1, unlike, after 70 DEG C are 20 hours dry, without forging It burns, is directly cut into the disk that diameter is 1cm.
After measured, deposition of the barium oxide in nickel foam is 2mg/cm2
Embodiment 11
Anode and battery is prepared according to the method for embodiment 1, unlike, after 70 DEG C are 20 hours dry, in air 4h is calcined at 150 DEG C.
After measured, deposition of the barium oxide in nickel foam is 2mg/cm2
The XRD spectrum for the barium oxide that embodiment 5-9 and embodiment 11 are prepared is similar to Example 1, embodiment The XRD spectrum of 10 barium oxides being prepared is referring to the map before calcining in Fig. 1.And emit light through inductively coupled plasma body Spectrometer (ICP) test, learns, is unformed knot before the barium oxide heat treatment that embodiment 5-9 and embodiment 11 are prepared The barium oxide of structure, it may be possible to one of vanadic anhydride, vanadium dioxide, vanadium trioxide and vanadium oxide or a variety of mixing Object;After heat treatment, the good barium oxide of crystallinity has been obtained.The barium oxide that embodiment 10 is prepared still is without fixed The barium oxide of type structure.
The barium oxide being prepared before embodiment 5-11 heat treatment and after heat treatment is observed under scanning electron microscope, SEM figure is similar to Example 1 respectively, that is, barium oxide that embodiment 5-11 is prepared (including through Overheating Treatment and without The barium oxide of Overheating Treatment) collection liquid surface is grown in Nanoparticulate pattern.
Embodiment 12
Anode and battery is prepared according to the method for embodiment 1, unlike, with AlCl3/ [PMIM] Cl=1.1:1 (mole Than) it is electrolyte.
Embodiment 13
Anode and battery is prepared according to the method for embodiment 1, unlike, with AlCl3/ [BDiMIM] Cl=1.1:1 (rubs That ratio) it is electrolyte.
Test example
Respectively to embodiment 1-13 group on LAND CT2001A tester (being purchased from Wuhan Land Electronic Co., Ltd.) It fills obtained aluminum secondary battery and carries out constant current charge-discharge performance test, charging/discharging voltage range is 2.5-0.02V, charging and discharging currents Density is 44.2mA/g.Wherein, the first discharge specific capacity for the battery that embodiment 1-13 is assembled into is (with the quality of positive electrode Meter) and recycle 50 times after specific discharge capacity (in terms of the quality of positive electrode) be shown in Table 1.
Table 1
In aluminum secondary battery of the invention, barium oxide, which is grown directly upon on collector, forms anode, does not need addition and leads Electric agent and binder, that is, may make not only has electrical contact well between the two, is able to maintain the steady of good anode electrode It is qualitative, and it is capable of increasing the surface area of vanadium oxide positive electrode materials, the contact area of positive electrode and electrolyte is improved, is shortened Diffusion length needed for aluminium ion and electronics, meanwhile, aluminum secondary battery of the invention specific discharge capacity with higher and excellent Stable circulation performance.
Embodiment 1 and embodiment 5 are compared it is found that when preparing anode vfanadium compound and vfanadium compound can be dissolved When the molar ratio of solute is 1:10-24 in aqueous solution, barium oxide is more advantageous in the uniform deposition of collection liquid surface, and can Further increase the specific discharge capacity and stable circulation performance of battery.
Embodiment 1 and embodiment 6 are compared it is found that in terms of vanadium, the concentration of vanadium ion solution is when preparing anode When 0.05-0.15mol/L, barium oxide is more advantageous in the uniform deposition of collection liquid surface, and can further increase battery Specific discharge capacity and stable circulation performance.
Embodiment 1 and embodiment 7 are compared it is found that when preparing anode, with hydrogen peroxide aqueous dissolution vfanadium compound, And when the time of stirring is 0.5-3h, barium oxide is more advantageous in the uniform deposition of collection liquid surface, and can be further Improve the specific discharge capacity and stable circulation performance of battery.
Embodiment 1 and embodiment 8 are compared it is found that the mass ratio of vanadium ion solution and collector is when preparing anode When 100:1-20:1, the specific discharge capacity and stable circulation performance of battery can be further increased.
Embodiment 1 and embodiment 9 are compared it is found that prepare anode when, extend in closed container hydro-thermal reaction when Between, when heated between when being 1-4 days so that react more abundant, be more advantageous to barium oxide in the uniform deposition of collection liquid surface, And the specific discharge capacity and stable circulation performance of battery can be further increased.
Embodiment 1 and embodiment 10-11 are compared it is found that when preparing anode, the combination that will be obtained after vacuum drying It is heat-treated and the temperature being heat-treated is 300-600 DEG C, when the time is 1-6h, although not will increase barium oxide in collector On deposition be still but conducive to the raising of the crystallinity of barium oxide, the specific discharge capacity of battery can be further increased And stable circulation performance.
Embodiment 1-11 (especially embodiment 1) and embodiment 12-13 are compared it is found that when preparing aluminum secondary battery, When electrolyte is AlCl3/[BMIM]Cl、AlCl3/[EMIM]Cl、AlCl3/ [BMIM] Br and AlCl3It is any in/[EMIM] Br When a kind of, the specific discharge capacity and stable circulation performance of battery can be further increased.
The preferred embodiment of the present invention has been described above in detail, still, during present invention is not limited to the embodiments described above Detail within the scope of the technical concept of the present invention can be with various simple variants of the technical solution of the present invention are made, this A little simple variants all belong to the scope of protection of the present invention.
It is further to note that specific technical features described in the above specific embodiments, in not lance In the case where shield, can be combined in any appropriate way, in order to avoid unnecessary repetition, the present invention to it is various can No further explanation will be given for the combination of energy.
In addition, various embodiments of the present invention can be combined randomly, as long as it is without prejudice to originally The thought of invention, it should also be regarded as the disclosure of the present invention.

Claims (6)

1. a kind of aluminum secondary battery, which is characterized in that the aluminum secondary battery includes anode, cathode, electrolyte and diaphragm, described Electrolyte is AlCl3/[BMIM]Cl、AlCl3/[EMIM]Cl、AlCl3/ [BMIM] Br and AlCl3It is any one in/[EMIM] Br Kind, the anode is the combination for growing barium oxide and collector on a current collector, and the preparation method of the anode includes Following steps:
(1) vfanadium compound is dissolved, obtains the vanadium ion solution that concentration is 0.05-0.15mol/L;
(2) vanadium ion solution and collector are subjected in closed container hydro-thermal reaction, clean reaction product after reaction And vacuum drying, obtain growing the combination of barium oxide and collector on a current collector;
(3) combination that step (2) obtains is calcined, the condition of the calcining includes: that temperature is 300-600 DEG C, the time For 1-6h;
Wherein, in step (2), the mass ratio of the vanadium ion solution and the collector is 100:1-20:1, and the water The condition of thermal response includes: that heating temperature is 180 DEG C to less than 205 DEG C, and heating time is 1-4 days, and the barium oxide is in institute Stating the deposition on collector is 2-10mg/cm2
2. aluminum secondary battery according to claim 1, wherein in step (2), the vacuum drying condition includes: dry Dry temperature is 60-80 DEG C, drying time 12-24h.
3. aluminum secondary battery according to claim 1 or 2, wherein in step (1), the method for dissolving vfanadium compound includes: Under stiring, the solution that can dissolve vfanadium compound is added in vfanadium compound;The solution that vfanadium compound can be dissolved is Water, aqueous hydrogen peroxide solution, oxalic acid aqueous solution, aqueous hydrochloric acid solution or ammonia spirit.
4. aluminum secondary battery according to claim 1 or 2, wherein the vfanadium compound is vanadic anhydride, titanium dioxide One of vanadium, vanadium trioxide, vanadium oxalate, vanadyl oxalate and ammonium metavanadate are a variety of.
5. aluminum secondary battery according to claim 1 or 2, wherein the collector be nickel foam, foam copper, titanium foam, Foam iron-nickel, stainless (steel) wire or carbon cloth.
6. aluminum secondary battery according to claim 1 or 2, wherein the cathode is metal aluminum or aluminum alloy;The diaphragm For fibreglass diaphragm.
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