WO2011079482A1 - Battery - Google Patents
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- WO2011079482A1 WO2011079482A1 PCT/CN2010/000177 CN2010000177W WO2011079482A1 WO 2011079482 A1 WO2011079482 A1 WO 2011079482A1 CN 2010000177 W CN2010000177 W CN 2010000177W WO 2011079482 A1 WO2011079482 A1 WO 2011079482A1
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- Prior art keywords
- battery
- positive electrode
- ion
- negative electrode
- electrolyte
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/052—Li-accumulators
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/38—Selection of substances as active materials, active masses, active liquids of elements or alloys
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/38—Selection of substances as active materials, active masses, active liquids of elements or alloys
- H01M4/42—Alloys based on zinc
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
- H01M4/485—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of mixed oxides or hydroxides for inserting or intercalating light metals, e.g. LiTi2O4 or LiTi2OxFy
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
- H01M4/50—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese
- H01M4/505—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese of mixed oxides or hydroxides containing manganese for inserting or intercalating light metals, e.g. LiMn2O4 or LiMn2OxFy
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
- H01M4/52—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron
- H01M4/525—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron of mixed oxides or hydroxides containing iron, cobalt or nickel for inserting or intercalating light metals, e.g. LiNiO2, LiCoO2 or LiCoOxFy
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/58—Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy; of polyanionic structures, e.g. phosphates, silicates or borates
- H01M4/5825—Oxygenated metallic salts or polyanionic structures, e.g. borates, phosphates, silicates, olivines
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
Definitions
- the invention belongs to the field of electrochemical energy storage, and particularly relates to a battery. Background technique
- Rechargeable batteries that have been commercially used in history include lead-acid batteries, nickel-cadmium batteries, nickel-hydrogen batteries, lithium-ion batteries, etc., as well as nickel-zinc batteries, zinc-bromine batteries, etc., which are not fully mature.
- lead-acid batteries and nickel-cadmium batteries are not accepted because of serious pollution and toxic.
- Nickel-hydrogen batteries are still too expensive, and nickel resources are not rich, which limits their development.
- Nickel-zinc batteries have been extensively studied in the 1960s and 1970s, but in alkaline environments, the dissolution of zinc anodes and the growth of dendrites are not effectively controlled, so it has been difficult to mature.
- the problems encountered by zinc-bromine batteries are the diffusion of bromine, self-discharge and other factors.
- batteries for electric vehicles are also fuel cells and metal air batteries.
- fuel cells have powerful power and energy density close to that of internal combustion engine systems.
- precious metal catalysts such as platinum.
- its expensive price and scarcity of platinum resources made it destined to be unusable for a short time. It can be said that the fuel economy has stalled, leading to the collapse of the US hydrogen economy.
- Other types of batteries, such as zinc-air batteries, are primary batteries that are difficult to use widely.
- Lithium-ion batteries have been widely used since they were commercialized in the early 1990s.
- the principle of such a battery is to obtain a potential difference by different deintercalation-insertion reaction potentials of lithium ions in the positive and negative active materials, and lithium ions flow between the positive and negative electrodes during charging and discharging, which is called a rocking chair battery.
- the electrolyte can only use an organic solution which is stable over a wide voltage range as an electrolyte, and accordingly a suitable electrolyte is also very limited.
- the improvement of rate discharge performance and the improvement of safety performance brought by new cathode materials lithium-ion batteries have gradually become more and more applicable in power tools, electric vehicles, and large-scale energy storage batteries.
- lithium-ion batteries with lithium iron phosphate or lithium manganate are still not fully mature, mainly because they are expensive, and the control of moisture during the manufacturing process also leads to additional cost and instability of product consistency. These two factors have greatly hindered the large-scale application of lithium-ion batteries.
- water-based lithium-ion batteries such as LiMn 2 O 4 as the positive electrode and vanadium oxide such as LiV 3 O 8 as the negative electrode.
- the battery has high energy density (up to 60%-80% of lithium ion battery), high power density (expected to reach 200% of lithium ion battery, or even higher), easy to manufacture (no water is needed in the manufacturing process) Control), completely non-toxic, environmentally friendly, easy to recycle and low cost (the same capacity of the battery, is expected to reach 60% of lead-acid batteries, 20% of lithium-ion batteries, or even lower).
- a battery comprising a positive electrode, a negative electrode and an electrolysis, wherein the active material of the positive electrode is one of a material capable of reversibly extracting-embeding ions or functional groups, and at least one of the metal elements is negatively used, and the electrolyte is capable of dissolving the electrolyte. At least one of a solvent which is ionized, wherein the electrolyte contains a metal ion of a positive electrode which can be eluted-embedded ions and a negative electrode active material.
- the reversibility of the positive electrode is achieved by the extraction or embedding of the detachable-embedded ions on the positive active material
- the reversibility of the negative electrode is achieved by electrochemical oxidation and reduction of the metal ion on the surface of the negative electrode.
- the battery of the present invention includes a positive electrode, a negative electrode and an electrolyte in its core structure.
- the active material of the positive electrode is a compound capable of eluting-intercalating lithium ions or sodium ions;
- the negative electrode is a pure metal plate/foil, or a formed metal powder, and the metal is an active material of a negative electrode and can also serve as a negative electrode
- the fluid is a solvent capable of dissolving the electrolyte and ionizing the electrolyte, such as water, an alcohol (such as methanol, ethanol), or the like, or another organic solvent capable of dissolving the electrolyte and ionizing the electrolyte, wherein the electrolyte A metal ion containing an ion-decomposing ion and a negative electrode active material which can be extracted in the positive electrode material.
- the positive electrode active material of the battery of the present invention is a compound capable of eluting-embedding ions
- the negative electrode active material is a metal having a different oxidation-reduction potential from the positive electrode active material deintercalation potential.
- the positive electrode acquires electrons and intercalates ions; the negative active material metal loses electrons and dissolves in the electrolyte.
- the electrolyte is a solution of multiple ions, Includes ions that can be deintercalated from the cathode material, to! a salt, a hydroxide, or other soluble corresponding metal compound of a metal contained in the negative electrode active material.
- the charging and discharging working principle of the battery of the invention is as follows:
- the positive electrode reaction is LiA a B e C — xe' - x
- the negative electrode reaction is M x+ + xe' ⁇ M, LiAaB P C 3 ⁇ 4 - the general formula of the ion intercalating compound, and M is a kind of gold, which is an ion form of one or several metals.
- Lithium ions or other detachable-embedded ions of the positive electrode are removed from the positive electrode active material, and the valence ions in the positive electrode active material are oxidized and lose electrons, and electrons pass from the positive electrode to the negative electrode via the external circuit.
- a metal ion contained in the electrolyte obtains electrons on the surface of the negative electrode and is electrodeposited on the surface of the negative electrode in a metal form to achieve charging.
- the discharge process is the opposite of the charging process.
- LiMn 2 O 4 /Zn battery as an example (see Figures 2B-1 and 2B-2), the inventors further explain the working principle of the battery of the present invention: charging battery with LiMn 2 O 4 as positive electrode and zinc as negative electrode, charging When Li + ions in LiMn 2 O 4 are removed from the crystal lattice, one trivalent manganese loses an electron to be oxidized, LiMn 2 O 4 becomes a form of Li ⁇ Mi ⁇ O, and at the same time, zinc ions in the electrolyte get electrons. It is reduced and deposited on the surface of the metal zinc.
- the positive reaction is
- the negative electrode reaction is Zn 2+ + xe' ⁇ (x/2) Zn.
- the discharge process is the reverse process of the charging process, that is, the zero-valent zinc of the negative electrode is oxidized and dissolved, and the positive electrode obtains electrons and is inserted into the lithium-ion ICP, and when discharged (as shown in FIG. 2B-2), the positive electrode reaction is
- the reversible de-intercalation-intercalating material comprises a compound capable of deintercalating-embedded lithium, sodium plasma.
- the positive electrode active material of the present invention is a compound capable of eluting-intercalating lithium ions, such as LiMn 2 O 4 , LiFePO 4 , LiCoO 2 Li xPO 4 , LiM x SiO y (wherein M is a variable metal) ) Binary materials or ternary material compounds.
- lithium ions can be extracted-incorporated into compounds such as LiV 3 0 8 , etc., sodium ion-extractable-embedded compounds such as NaVPO 4 F, and the like, and can be ejected-embedded.
- the ionic, functional group compounds all have similar functions and are also suitable for the positive electrode structure of the battery of the present invention.
- the battery according to the present invention wherein the extractable-intercalating lithium ion-containing compound is selected from the group consisting of a layered structural compound, a spinel structure compound or an olivine structure compound, and other lithium and sodium ions are detachable. At least one of the embedded compounds.
- a battery according to the present invention wherein the layered structural compound has a general formula of Wherein, 0 ⁇ x ⁇ 2, 0 ⁇ y ⁇ 0.5, M is at least one selected from the group consisting of Co, Ni, and Mn, and M' is at least one selected from the group consisting of Mg, Ti, Cr, V, Zn, Zr, Si, or Ai.
- M is at least one selected from the group consisting of Co, Ni, and Mn
- M' is at least one selected from the group consisting of Mg, Ti, Cr, V, Zn, Zr, Si, or Ai.
- LiFeSiO 4 or the like LiFeSiO 4 or the like.
- the battery according to the present invention wherein the spinel structure compound has a general formula of Li x Mn y M z O k , wherein 0.5 ⁇ x ⁇ 3, 0 ⁇ y ⁇ 3 0 ⁇ z ⁇ 3, 0 ⁇ k ⁇ 8, M is at least one selected from the group consisting of Mg, Ti, Cr, V, Zn, Zr, Si or Al.
- M is at least one selected from the group consisting of Mg, Ti, Cr, V, Zn, Zr, Si or Al.
- LiV 3 O 8 LiMnSiO 4 and the like.
- the battery of the olivine structure has a general formula of Li x M 2 _ y M' y (XO 4 ) n .
- M is a transition metal element
- M' is at least one selected from the group consisting of Mg, Ti, Cr, V or A1
- X is selected from S, P or Si.
- Li 3 V 2 (PO 4 ) 3 Li 3 V 2 (PO 4 ) 3 .
- the battery according to the present invention wherein the negative electrode is made of a metal element selected from the group consisting of
- Cu, Ag, Fe, Zn, Sn, Al or Ni may be specifically used as a negative electrode of a metal elementary plate, a foamed metal, or a shaped metal powder.
- the battery according to the present invention wherein the positive electrode of the battery comprises a current collector, which uses at least one of stainless steel, carbon fiber, graphite and other electrochemically stable electron good conductors.
- a current collector which uses at least one of stainless steel, carbon fiber, graphite and other electrochemically stable electron good conductors.
- the inventors have also found that with a completely chemically inert carbon-based material as the positive current collector, the cycle performance of the battery is much better than that of stainless steel as the positive current collector.
- the electrolyte is a chloride of lithium and a chloride of an anode active material.
- the electrolyte is a sulfate of lithium and a sulfate of a negative electrode active material.
- the electrolyte is water, and 1 M lithium ion and 5 M negative electrode active material ions are dissolved.
- the electrolytic solution is methanol, and 1 M lithium ion and 5 M negative electrode active material ion are dissolved.
- the electrolytic solution is ethanol, and 1 M lithium ion and 5 M negative electrode active material ion are dissolved.
- the battery of the present invention is made of inexpensive LiMn 2 O 4 , a conductive agent, and a binder, and is bonded to a graphite current collector, conductive carbon paper, or the like as a positive electrode; and the metal zinc or zinc powder is a negative electrode.
- the electrolyte includes lM Li + ions and 5M Zn 2+ ions.
- the conductive agent is graphite and the binder is a PTFE emulsion.
- the separator may not be used.
- the separator is an organic or inorganic porous material, and the separator has a pore diameter of 0.001-1 ⁇ m.
- the present invention has the following advantages:
- Cycle life unit energy energy density resource rich environment friendly (time) cost* * :* sex as a power battery lead-acid battery 300 30% 30% rich, lead toxic for the previous generation mass production battery
- NiMH battery 1000 80% 60% Nickel resources are not nickel for toxic and bare nickel-cadmium batteries 1000 50% 40% Nickel resources are not impossible Nickel-zinc battery 300 30% 50% Nickel resources are not temporarily unavailable Zinc-bromine battery 2000 30% 40% Rich, bromine corrosive can not be mass produced temporarily
- Lithium-ion battery 2000 100% 100% rich, relatively friendly
- the battery of the invention 1000 or more 20% 60%-70% rich, can be very friendly
- the unit energy cost is calculated based on the current lithium battery.
- the battery of the present invention is easy to manufacture, requires no moisture control during the manufacturing process, is easy to recycle, and is inexpensive.
- FIG. 1 is a schematic view showing the structure of a battery of the present invention, wherein 1 is a positive electrode current collector, 2 is a positive electrode active material, 3 is a negative electrode active material as a current collector, and 4 is an electrolyte solution.
- FIG. 2A is a schematic view showing the charging operation principle of the battery of the present invention in which the positive electrode material is LiA a B e C A .
- FIG. 2B-1 and 2B-2 are schematic diagrams showing the working principle of the LiMn 2 O 4 /Zn battery of the present invention, wherein FIG. 2B-1 is a schematic diagram of a battery charging process; and FIG. 2B-2 is a schematic diagram of a battery discharging process.
- FIG. 3 is a graph showing the first charge and discharge of a LiMn 2 O 4 /Zn battery according to Embodiment 1 of the present invention, wherein 1 is a charge profile and 2 is a discharge curve.
- Figure 4 is a graph showing the cycle performance of a LiMn 2 04/i3 ⁇ 4 battery of Example 1 of the present invention.
- Figure 5 is a graph showing the cycle performance of a LiFePO 4 /Zn battery according to Example 3 of the present invention.
- Fig. 6 is a graph showing the cycle performance of a NaVPO ⁇ /Zn battery of Example 4 of the present invention.
- Figure 7 is a graph showing the cycle performance of a LiMn 2 O 4 /foam nickel battery of Example 7 of the present invention.
- Figure 8 is a graph showing the cycle performance of a LiMn 2 O 4 /Zn battery according to Example 14 of the present invention.
- Figure 9 is a graph showing the relationship between charge and discharge efficiency and charge current multiplication of LiMn 2 O 4 /Zn battery in Example 20 of the present invention.
- LiMn 2 0 4 is used as the positive electrode active material, and is uniformly mixed according to the positive electrode active material 88 wt%: conductive carbon black 8 wt%: adhesive PTFE (polytetrafluoroethylene) 4 wt%, and cut into a diameter of 12 mm and a thickness of 0.1-0.2 mm. The wafer is pressed onto a graphite current collector to form a positive electrode.
- the negative electrode active material was metal zinc having a width of 15 mm and a thickness of 1 mm, and also served as a current collector.
- the positive and negative electrodes are separated by 5 mm and have no diaphragm.
- the electrolytic solution was a mixed aqueous solution of lithium chloride and zinc chloride containing 1 mol/L of lithium ion and 5 mol/L of zinc ion.
- the cycle test was carried out under a voltage range of U-2.05 V and a charge-discharge current of 0.5 C.
- Figure 1 shows the basic structure of a battery.
- the first charge and discharge curve is shown in Figure 3, and the battery cycle performance is shown in Figure 4. It can be seen that the charge and discharge curve of the battery is very similar to that of the lithium ion battery of the organic electrolyte system, except that the platform is lower. From the perspective of the test battery, the cycle performance is also excellent.
- a battery was fabricated in the same manner as in Example 1, except that LiCoO 2 was used as the positive electrode active material, and the cycle operating voltage ranged from 1.3-1.95 V.
- the battery cycle performance test results are shown in Table 1.
- a battery was fabricated in the same manner as in Example 1, except that LiFePO 4 was used as the positive electrode active material, and the cycle operating voltage ranged from 0.8 to 1.6 V.
- the battery cycle performance test results are shown in Table 1 and Figure 5.
- a battery was fabricated in the same manner as in Example 1, except that NaVPO 4 F was used as a positive electrode active material, and the cycle operating voltage ranged from 1.3 to 2.0 V.
- the battery cycle performance test results are shown in Table 1 and Figure 6.
- a battery was fabricated in the same manner as in Example 1, except that LiMn 2 0 4 and LiCo0 2 were mixed at a mass ratio of 1:1 as a positive electrode active material, and the cycle operating voltage ranged from 1.3 to 2.05 V.
- the test results of charge and discharge and battery cycle performance are shown in Table 1. Capacity retention test
- the batteries of the above Examples 1-5 were subjected to a cyclic charge discharge operation to detect the battery capacity retention rate after 30 cycles. First, the battery is charged at a fixed current of 0.5 C rate until the voltage reaches the upper limit, and then the battery is discharged at a fixed current of 0.5 C rate until the voltage reaches the lower limit. So repeating this week.
- Table 1 below shows the battery performance exhibited by several different positive electrode materials and metallic zinc as counter electrodes.
- LiMn 2 O 4 is used as the positive electrode active material, and the first charge and discharge curve of the metal zinc as the counter electrode is shown in FIG. 3 , and the cycle performance of the battery is shown in FIG. 4 .
- Table 1 it can be seen that for the more mature cathode materials (LiMn 2 0 4 , LiCo0 2 and LiMn 2 0 4 /LiCo0 2 ), the electrochemical performance is better than that of other materials (LiFeP0 4 , NaVP0 4 ). F) It is much better.
- LiMn 2 0 4 is used as the positive electrode active material, and is uniformly mixed according to the positive electrode active material 88 wt %: conductive carbon black 8 wt %: adhesive PTFE 4 wt%, and cut into discs having a diameter of 12 mm and a thickness of 0.1-0.2 mm, and pressed at On the graphite current collector, the positive electrode is formed;
- the negative electrode active material is a manganese-coated zinc plate having a width of 15 mm and a thickness of 0.5-lmm (wherein the reduction property of zinc is not as strong as that of manganese, and does not participate in the reaction during charge and discharge, but acts as a current collector).
- the positive and negative electrodes are separated by 5 mm and have no diaphragm.
- the electrolytic solution was a mixed aqueous solution of lithium chloride and manganese chloride containing 1 md/L of lithium ion and 5 mol/L of manganese ion.
- the cycle test was performed with a voltage range of 1.3-2.2 V and a charge-discharge current of 0.5 C.
- a battery was fabricated in the same manner as in Example 6, except that instead of a manganese-coated zinc plate as a negative electrode, a nickel chloride containing 5 mol/L of nickel ions was replaced by nickel chloride containing 5 mol/L of nickel ions.
- the aqueous solution was used as an electrolyte for a cycle test between a voltage range of 0.8-L5V and a charge-discharge current of 0.5C.
- the results of the battery cycle performance test are shown in Table 2 and Figure 7.
- a battery was fabricated in the same manner as in Example 6, except that an iron sheet was used instead of the manganese-coated zinc plate as the negative electrode, and accordingly, an aqueous solution of manganese chloride containing 5 mol of L manganese ions was replaced by ferric chloride containing 5 mol of iron ions.
- the liquid is subjected to a cycle test in a voltage range of 1.3 to 2.0 V and a charge and discharge current of 0.5 C.
- a battery was fabricated in the same manner as in Example 6, except that a cadmium sheet was used instead of the manganese-coated zinc sheet as a negative electrode, and a calcium chloride solution containing 5 mol/L of manganese ions was replaced by cadmium chloride containing 5 mol/L of cadmium ions.
- a cycle test was performed with a voltage range of 1.3 to 2.0 V and a charge and discharge current of 0.5 C.
- a battery was fabricated in the same manner as in Example 6, except that the pressed zinc powder was used instead of the manganese-coated zinc sheet as the negative electrode, and the test method was the same as in Example 2.
- a battery was fabricated in the same manner as in Example 6, except that zinc oxide was used instead of the manganese-coated zinc sheet as the negative electrode, and the test method was the same as in Example 2.
- the batteries in the above Examples 1 and 6-11 were subjected to a cyclic charge discharge operation to detect the capacity retention rate after 30 cycles. First, the battery is charged at a fixed current of 0.5 C rate until the voltage reaches the upper limit, and then the battery is discharged at a fixed current of 0.5 C rate until the voltage reaches the lower limit. So repeating this week.
- Table 2 below shows the battery performance exhibited by the negative electrodes of several different metals and LiMn 2 O 4 as the positive electrode active material counter electrode.
- a battery was fabricated in the same manner as in Example 1, except that an aqueous solution of lithium acetate containing 1 mol of lithium ion and zinc acetate containing 3 mol/L of zinc ion was used as an electrolytic solution, and the cycle operating voltage range was 1.3-2.05V.
- a battery was fabricated in the same manner as in Example 1, except that lithium acetate containing 1 mol/L of lithium ion and methanol solution of zinc acetate containing 3 mol/L of zinc ion were used as the electrolyte, and the cycle operating voltage range was 1.3-2.05V. .
- Example 14 A battery was fabricated in the same manner as in Example 1, except that lithium acetate containing 1 mol/L of lithium ion and ethanol solution of zinc acetate containing 3 mol/L of zinc ion were used as a solution, and the cycle operating voltage range was 1.3-2.05. V.
- the battery cycle performance test results are shown in Table 3 and Figure 8. ;
- a battery was fabricated in the same manner as in Example 1, except that an aqueous solution of lithium sulfate containing 1 mol/L of lithium ion and zinc sulfate containing 5 mol/L of zinc ion was used as an electrolytic solution, and the cycle operating voltage range was 1.3-2.05V.
- a battery was fabricated in the same manner as in Example 1, except that a 316L type stainless steel having a thickness of 1 mm was used instead of the graphite sheet as a positive electrode active material current collector.
- a battery was fabricated in the same manner as in Example 1, except that a 304 type stainless steel having a thickness of 1 mm was used instead of the graphite sheet as a positive electrode active material current collector. '
- a battery was fabricated in the same manner as in Example 1, except that a carbon fiber cloth (thickness of about 0.1 mm) was used instead of the graphite sheet as a positive electrode active material current collector.
- the inventors have also examined the electrical properties of a variety of other lithium ion-embedded compounds and metals as counter electrodes. Although the cycle performance of these combinations is quite different, they all form batteries and the charge and discharge mechanisms are basically the same, which are in accordance with the principle of charge and discharge of the battery of the present invention.
- Table 5 shows the discharge open circuit voltages of the batteries composed of various electrode compositions.
- Table 5 shows the open circuit voltage of the battery with different positive and negative poles
- the positive and negative electrodes listed in Table 5 are only a small portion of the positive and negative electrodes that may be used in the battery of the present invention. Since there are many possible forms of such batteries in accordance with the principles of the present invention, particularly positive electrode materials, it may include sodium ion intercalation compounds which are not yet matured, as well as certain functional group deintercalation compounds and the like.
- the battery may be accompanied by a series of side reactions such as decomposition of water, etc., while charging the battery.
- a battery was fabricated in the same manner as in Example 1 to operate the battery at different charge and discharge current rates to obtain different charge and discharge current efficiencies. As a result, as shown in Fig. 9, a charge and discharge efficiency of 91% or more can be obtained at a suitable charge rate.
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Abstract
Description
一种电池 技术领域 Battery technology field
本发明属于电化学储能领域, 具体涉及一种电池。 背景技术 The invention belongs to the field of electrochemical energy storage, and particularly relates to a battery. Background technique
化学能源越来越稀缺的今天, 开发电动汽车, 风能等迫在眉睫。 尽管电机, 螺旋 桨推进器等领域已经非常成熟, 但在储能领域一直没有得到突破, 限制了诸如电动汽 车和风能等的广泛应用。 Today, chemical energy is becoming scarcer, and the development of electric vehicles and wind energy is imminent. Although the fields of motors, propellers and the like are very mature, there has been no breakthrough in the field of energy storage, which limits the wide range of applications such as electric vehicles and wind energy.
历史上获得过商业化应用的可充电电池依次有铅酸电池, 镍镉电池, 镍氢电池, 锂离子电池等, 另外还有不完全成熟的镍锌电池, 锌溴电池等。 目前来说, 铅酸电池, 镍镉电池由于污染严重, 有毒等已经不为人们所接受, 镍氢电池仍然太贵, 并且镍资 源并不算丰富, 限制了其发展。 镍锌电池在上世纪 60-70年代得到了广泛的研究, 但 在碱性环境下,锌负极的溶解, 枝晶的生长等得不到有效的控制, 因此一直难以成熟。 而锌溴电池遇到的问题却是溴的扩散, 自放电等因素。 目前锌溴电池在发达国家已经 有了一定规模的示范性运作, 但距离实际应用还有很长的路要走。 同时, 这种为大型 储能项目设计的电池能量密度太低, 也不太适合类似于电动汽车这样的移动电源。 Rechargeable batteries that have been commercially used in history include lead-acid batteries, nickel-cadmium batteries, nickel-hydrogen batteries, lithium-ion batteries, etc., as well as nickel-zinc batteries, zinc-bromine batteries, etc., which are not fully mature. At present, lead-acid batteries and nickel-cadmium batteries are not accepted because of serious pollution and toxic. Nickel-hydrogen batteries are still too expensive, and nickel resources are not rich, which limits their development. Nickel-zinc batteries have been extensively studied in the 1960s and 1970s, but in alkaline environments, the dissolution of zinc anodes and the growth of dendrites are not effectively controlled, so it has been difficult to mature. The problems encountered by zinc-bromine batteries are the diffusion of bromine, self-discharge and other factors. At present, zinc-bromine batteries have already had a certain scale of demonstration operation in developed countries, but there is still a long way to go before practical applications. At the same time, the energy density of batteries designed for large-scale energy storage projects is too low, and it is not suitable for mobile power sources like electric vehicles.
目前, 为电动汽车而研究的电池还有燃料电池和金属空气电池等。 其中燃料电池 具有强大的功率和接近内燃机系统的能量密度,但燃料电池经过近 20年的研究也未能 在关键技术上取得突破,仍然需要使用铂之类的贵金属催化剂。在关键技术突破之前, 其昂贵的价格和铂资源的稀缺使其注定了短时间无法应用。 可以说, 由于燃料电池的 止步不前, 导致了美国的氢经济的破灭。 其他类型的电池, 诸如锌空气电池等属于一 次电池, 难以广泛应用。 At present, batteries for electric vehicles are also fuel cells and metal air batteries. Among them, fuel cells have powerful power and energy density close to that of internal combustion engine systems. However, after nearly 20 years of research on fuel cells, they have not made breakthroughs in key technologies, and still need to use precious metal catalysts such as platinum. Before the breakthrough of key technologies, its expensive price and scarcity of platinum resources made it destined to be unusable for a short time. It can be said that the fuel economy has stalled, leading to the collapse of the US hydrogen economy. Other types of batteries, such as zinc-air batteries, are primary batteries that are difficult to use widely.
锂离子电池自上世纪 90年代初商业化以来,得到了广泛的应用。这种电池的原理 是依靠锂离子在正负极活性物质中不同的脱嵌-插入反应电位取得电势差,充放电过程 中锂离子在正负极之间流动, 形象地被称为摇椅电池。 因为充电电压高, 其电解液只 能使用在宽电压范围内稳定的有机溶液作为电解液,相应地合适的电解质也非常有限。 随着能量密度的提高, 倍率放电性能的改善和新型正极材料带来的安全性能的提高, 锂离子电池在电动工具, 电动汽车, 大型储能电池方面逐渐有了应用的可能。 当前最 有可能在电动汽车和储能项目应用的錄,暴以磷酸铁锂或锰酸锂为正极材料的锂离子电 池。 但这种电池仍然没有完全成熟, 主要是成本昂贵, 另外在制造过程中对水分的控 制也导致额外的成本和产品一致性的不稳定。 以上两个因素极大地阻碍了锂离子电池 的大型化应用。 为了提高锂离子二次电池的安全性, 降低电池成本, 目前很多研究者 都致力于水系锂离子电池的研究, 例如以 LiMn2O4为正极, 钒的氧化物例如 LiV3O8 等为负极的摇椅原理电池出现, 但因其负极极差的循环性能和钒的毒性, 限制了此类 电池的发展。 截至目前, 已经提出的水系锂离子二次电池的结构都未摆脱基于锂离子 脱嵌原理的摇椅式结构, 比如已经有报道的 VO2/ LiMn2O4, LiV3O8/ LiNi 81Co。.19O2, TiP2O7/ LiMn2O4, LiTi2(PO4)3/ LiMn2O4, LiV3O8/ LiCoO2等等。 发明内容 Lithium-ion batteries have been widely used since they were commercialized in the early 1990s. The principle of such a battery is to obtain a potential difference by different deintercalation-insertion reaction potentials of lithium ions in the positive and negative active materials, and lithium ions flow between the positive and negative electrodes during charging and discharging, which is called a rocking chair battery. Since the charging voltage is high, the electrolyte can only use an organic solution which is stable over a wide voltage range as an electrolyte, and accordingly a suitable electrolyte is also very limited. With the increase of energy density, the improvement of rate discharge performance and the improvement of safety performance brought by new cathode materials, lithium-ion batteries have gradually become more and more applicable in power tools, electric vehicles, and large-scale energy storage batteries. Current most It is possible to use lithium-ion batteries with lithium iron phosphate or lithium manganate as cathode materials for applications in electric vehicles and energy storage projects. However, such batteries are still not fully mature, mainly because they are expensive, and the control of moisture during the manufacturing process also leads to additional cost and instability of product consistency. These two factors have greatly hindered the large-scale application of lithium-ion batteries. In order to improve the safety of lithium ion secondary batteries and reduce the cost of batteries, many researchers are currently working on the research of water-based lithium-ion batteries, such as LiMn 2 O 4 as the positive electrode and vanadium oxide such as LiV 3 O 8 as the negative electrode. The principle of the rocking chair battery appears, but the development of such batteries is limited by the poor cycle performance of the negative electrode and the toxicity of vanadium. Up to now, the structure of the water-based lithium ion secondary battery that has been proposed has not been shaken off from the rocker-type structure based on the principle of lithium ion deintercalation, such as VO 2 / LiMn 2 O 4 , LiV 3 O 8 / LiNi 81 Co which have been reported. 19 O 2 , TiP 2 O 7 /LiMn 2 O 4 , LiTi 2 (PO 4 ) 3 /LiMn 2 O 4 , LiV 3 O 8 /LiCoO 2 and the like. Summary of the invention
针对历史上所出现的电池的缺点和不足, 发明人的目的是研发出一种新的电池, 一种新的二次电池。 使所述的电池具有能量密度高(可达锂离子电池的 60%-80%), 功率密度大(可望达到锂离子电池的 200%, 甚至更高), 易于制造(制造过程不需要 水分控制), 完全无毒, 环保, 容易回收且成本低廉(同样容量的电池, 可望达到铅酸 电池的 60%, 锂离子电池的 20%, 甚至更低)等特点。 In view of the shortcomings and deficiencies of batteries that have historically appeared, the inventors aimed to develop a new battery, a new secondary battery. The battery has high energy density (up to 60%-80% of lithium ion battery), high power density (expected to reach 200% of lithium ion battery, or even higher), easy to manufacture (no water is needed in the manufacturing process) Control), completely non-toxic, environmentally friendly, easy to recycle and low cost (the same capacity of the battery, is expected to reach 60% of lead-acid batteries, 20% of lithium-ion batteries, or even lower).
为实现本发明的目的, 发明人提供如下技术方案: In order to achieve the object of the present invention, the inventors provide the following technical solutions:
一种电池, 包括正极、 负极和电解 , 所述的正极的活性物质采用能可逆脱出- 嵌入离子或官能团的材料中的一种, 负 采用金属单质中的至少一种, 电解液为能够 溶解电解质并使之电离的溶剂中的至少一种,其中所述的电解质含正极可脱出-嵌入的 离子和负极活性物质的金属离子。本发明所述的电池, 其正极的可逆性是依靠可脱出- 嵌入离子在正极活性材料上的脱出或嵌入来实现, 而负极的可逆是依靠金属离子在负 极表面的电化学氧化和还原来实现。 A battery comprising a positive electrode, a negative electrode and an electrolysis, wherein the active material of the positive electrode is one of a material capable of reversibly extracting-embeding ions or functional groups, and at least one of the metal elements is negatively used, and the electrolyte is capable of dissolving the electrolyte. At least one of a solvent which is ionized, wherein the electrolyte contains a metal ion of a positive electrode which can be eluted-embedded ions and a negative electrode active material. In the battery of the present invention, the reversibility of the positive electrode is achieved by the extraction or embedding of the detachable-embedded ions on the positive active material, and the reversibility of the negative electrode is achieved by electrochemical oxidation and reduction of the metal ion on the surface of the negative electrode. .
本发明的电池其核心结构中包括正极、 负极和电解液。 所述的正极的活性物质为 可脱出-嵌入锂离子或者钠离子的化合物; 负极为纯金属板 /箔, 或者是成型的金属粉 末, 所述的金属是负极的活性物质, 同时可兼作为负极集流体; 电解液为能够溶解电 解质并使电解质电离的溶剂, 如水、 醇类物质(如甲醇、 乙醇)等等, 或者其他能够 溶解电解质并使电解质电离的有机溶剂,'其中,所述的电解质含可在正极材料中脱出- 嵌入的离子和负极活性物质的金属离子。 The battery of the present invention includes a positive electrode, a negative electrode and an electrolyte in its core structure. The active material of the positive electrode is a compound capable of eluting-intercalating lithium ions or sodium ions; the negative electrode is a pure metal plate/foil, or a formed metal powder, and the metal is an active material of a negative electrode and can also serve as a negative electrode The fluid is a solvent capable of dissolving the electrolyte and ionizing the electrolyte, such as water, an alcohol (such as methanol, ethanol), or the like, or another organic solvent capable of dissolving the electrolyte and ionizing the electrolyte, wherein the electrolyte A metal ion containing an ion-decomposing ion and a negative electrode active material which can be extracted in the positive electrode material.
本发明电池的正极活性物质为可脱出-嵌入离子的化合物,负极活性物质为氧化还 原电位与正极活性物质脱嵌电位不同的金属。 在放电过程中, 正极得到电子并嵌入离 子; 负极活性物质金属失去电子, 并溶解在电解液中。 电解液为一种多元离子的溶液, 包括了正极材料所能够脱嵌的离子, 以!^负极活性物质中所包含的金属的盐类, 氢氧 化物, 或其他可溶的相应金属化合物。 ' The positive electrode active material of the battery of the present invention is a compound capable of eluting-embedding ions, and the negative electrode active material is a metal having a different oxidation-reduction potential from the positive electrode active material deintercalation potential. During discharge, the positive electrode acquires electrons and intercalates ions; the negative active material metal loses electrons and dissolves in the electrolyte. The electrolyte is a solution of multiple ions, Includes ions that can be deintercalated from the cathode material, to! a salt, a hydroxide, or other soluble corresponding metal compound of a metal contained in the negative electrode active material. '
本发明的电池, 其充放电的工作原理为: 充电时(可参见附图 2A, 图中, 正极反 应为 LiAaBeC — xe'— x 负极反应为 Mx++xe'→M, LiAaBPC ¾— 种离子嵌入化合物的通式, M为一种金 , 是一种或几种金属的离子形态。 ), 正 极的锂离子或者其他可脱出-嵌入离子从正极活性物质中脱出,正极活性物质中的变价 离子被氧化并失去电子, 电子从正极经由外电路到达负极。 电解液中所包含的一种金 属离子在负极表面获得电子, 并以金属形态电沉积在负极表面, 从而实现充电。 放电 过程与充电过程相反。 The charging and discharging working principle of the battery of the invention is as follows: When charging (see Fig. 2A, in the figure, the positive electrode reaction is LiA a B e C — xe' - x The negative electrode reaction is M x+ + xe' → M, LiAaB P C 3⁄4 - the general formula of the ion intercalating compound, and M is a kind of gold, which is an ion form of one or several metals. Lithium ions or other detachable-embedded ions of the positive electrode are removed from the positive electrode active material, and the valence ions in the positive electrode active material are oxidized and lose electrons, and electrons pass from the positive electrode to the negative electrode via the external circuit. A metal ion contained in the electrolyte obtains electrons on the surface of the negative electrode and is electrodeposited on the surface of the negative electrode in a metal form to achieve charging. The discharge process is the opposite of the charging process.
以 LiMn2O4/Zn 电池为例 (可参见附图 2B-1、 2B-2) , 发明人进一步说明本发明 电池的工作原理: 以 LiMn2O4为正极、 锌为负极组成电池, 充电时 LiMn2O4中的 Li+ 离子从晶格中脱出, 一个三价锰失去一个电子被氧化, LiMn2O4变成 Li^Mi^O 的形 态, 同时, 电解液中的锌离子得到电子被还原并沉积在金属锌表面。 充电时(如附图 2B-A所示), 正极反应为 负极反应为 Zn2++xe'→ (x/2)Zn。 放电过程为充电过程的逆过程 即负极 0价锌的氧化并溶解, 正极获得了电 子并伴随锂离子插入 li^M^OA中, 放电时(如附图 2B-2所示), 正极反应为 Taking LiMn 2 O 4 /Zn battery as an example (see Figures 2B-1 and 2B-2), the inventors further explain the working principle of the battery of the present invention: charging battery with LiMn 2 O 4 as positive electrode and zinc as negative electrode, charging When Li + ions in LiMn 2 O 4 are removed from the crystal lattice, one trivalent manganese loses an electron to be oxidized, LiMn 2 O 4 becomes a form of Li^Mi^O, and at the same time, zinc ions in the electrolyte get electrons. It is reduced and deposited on the surface of the metal zinc. When charging (as shown in Figure 2B-A), the positive reaction is The negative electrode reaction is Zn 2+ + xe' → (x/2) Zn. The discharge process is the reverse process of the charging process, that is, the zero-valent zinc of the negative electrode is oxidized and dissolved, and the positive electrode obtains electrons and is inserted into the lithium-ion ICP, and when discharged (as shown in FIG. 2B-2), the positive electrode reaction is
Li!.xMn2O4+ Li++xe'— LiMn2O4, 负极反应为 Zn— xe_→(x/2)Zn2+。 Li!. x Mn 2 O4+ Li + +xe'—LiMn 2 O 4 , and the negative electrode reacts with Zn—xe_→(x/2)Zn 2+ .
作为优选方案, 根据本发明所述的 ¾池, 其中, 所述的能可逆脱出-嵌入离子的材 料包括可脱出-嵌入锂、钠等离子的化合物。发明人研究发现, 本发明正极活性物质为 可脱出 -嵌入锂离子的化合物时, 可选用如 LiMn2O4、 LiFePO4、 LiCoO2 Li xPO4、 LiMxSiOy (其中 M为一种变价金属) 等二元材料或三元材料化合物。 此外, 发明人也 研究发现, 其他种类的锂离子可脱出-嵌:入化合物例如 LiV308等, 钠离子可脱出 -嵌入 化合物例如 NaVPO4F等, 以及具有类似功能的, 可脱出 -嵌入离子、 官能团的化合物 都具有类似的功能, 也都适用于本发明电池的正极结构。 Preferably, according to the invention, the reversible de-intercalation-intercalating material comprises a compound capable of deintercalating-embedded lithium, sodium plasma. The inventors have found that when the positive electrode active material of the present invention is a compound capable of eluting-intercalating lithium ions, such as LiMn 2 O 4 , LiFePO 4 , LiCoO 2 Li xPO 4 , LiM x SiO y (wherein M is a variable metal) ) Binary materials or ternary material compounds. In addition, the inventors have also found that other kinds of lithium ions can be extracted-incorporated into compounds such as LiV 3 0 8 , etc., sodium ion-extractable-embedded compounds such as NaVPO 4 F, and the like, and can be ejected-embedded. The ionic, functional group compounds all have similar functions and are also suitable for the positive electrode structure of the battery of the present invention.
作为优选方案, 根据本发明所述的电池, 其中, 所述的可脱出 -嵌入锂离子的化合 物选自层状结构化合物、 尖晶石结构化合物或橄榄石结构化合物以及其他锂、 钠离子 可脱嵌化合物中的至少一种。 Preferably, the battery according to the present invention, wherein the extractable-intercalating lithium ion-containing compound is selected from the group consisting of a layered structural compound, a spinel structure compound or an olivine structure compound, and other lithium and sodium ions are detachable. At least one of the embedded compounds.
作为更优选方案, 根据本发明所述的电池, 其中, 所述的层状结构化合物, 其通 式为 其中, 0<x≤2, 0<y<0.5, M选自 Co、 Ni、 Mn中至少一种, M' 选自 Mg、 Ti、 Cr、 V、 Zn、 Zr、 Si或 Ai中至少一种, 例如 LiFeSiO4等。 A battery according to the present invention, wherein the layered structural compound has a general formula of Wherein, 0<x≤2, 0<y<0.5, M is at least one selected from the group consisting of Co, Ni, and Mn, and M' is at least one selected from the group consisting of Mg, Ti, Cr, V, Zn, Zr, Si, or Ai. For example, LiFeSiO 4 or the like.
作为更优选方案, 根据本发明所述的电池, 其中, 所述的尖晶石结构化合物, 其 通式为 LixMny MzOk, 其中, 0.5<x≤3, 0<y<3 , 0≤z≤3, 0≤k≤8, M选自 Mg、 Ti、 Cr、 V、 Zn、 Zr、 Si或 Al中至少一种。 例如,, LiV3O8, LiMnSiO4等。 作为更优选方案, 根据本发明所述! ¾电池, 其中, 所述的橄榄石结构化合物, 其 通式为 LixM2_yM'y(XO4)n。 其中, 0<x≤3;、 0≤y≤2、 l≤n≤3, M是过渡金属元素, M'选 自 Mg、 Ti、 Cr、 V或 A1中至少一种, X选自 S、 P或 Si。 例如 Li3V2(PO4)3。 More preferably, the battery according to the present invention, wherein the spinel structure compound has a general formula of Li x Mn y M z O k , wherein 0.5<x≤3, 0<y<3 0 ≤ z ≤ 3, 0 ≤ k ≤ 8, M is at least one selected from the group consisting of Mg, Ti, Cr, V, Zn, Zr, Si or Al. For example, LiV 3 O 8 , LiMnSiO 4 and the like. As a more preferred embodiment, according to the invention, the battery of the olivine structure has a general formula of Li x M 2 _ y M' y (XO 4 ) n . Wherein, 0<x≤3 ; , 0≤y≤2, l≤n≤3, M is a transition metal element, and M' is at least one selected from the group consisting of Mg, Ti, Cr, V or A1, and X is selected from S, P or Si. For example, Li 3 V 2 (PO 4 ) 3 .
作为优选方案, 根据本发明所述的电池, 其中, 所述的负极采用的金属单质选自 Preferably, the battery according to the present invention, wherein the negative electrode is made of a metal element selected from the group consisting of
Cu、 Ag、 Fe、 Zn、 Sn、 Al或 Ni, 具体可采用金属单质板, 泡沬金属, 或者成型金属 粉末等作为负极。 Cu, Ag, Fe, Zn, Sn, Al or Ni may be specifically used as a negative electrode of a metal elementary plate, a foamed metal, or a shaped metal powder.
作为优选方案, 根据本发明所述的电池, 其中, 所述的电池的正极包括集流体, 其选用不锈钢、 碳纤维、 石墨及其他电化学稳定的电子良导体中的至少一种。 此外发 明人研究亦发现, 以完全化学惰性的碳系材料作为正极集流体, 电池的循环性能要比 不锈钢作为正极集流体的效果好的多。 Preferably, the battery according to the present invention, wherein the positive electrode of the battery comprises a current collector, which uses at least one of stainless steel, carbon fiber, graphite and other electrochemically stable electron good conductors. In addition, the inventors have also found that with a completely chemically inert carbon-based material as the positive current collector, the cycle performance of the battery is much better than that of stainless steel as the positive current collector.
作为更优选方案, 电解质为锂的氯化物和负极活性物质的氯化物。 As a more preferable embodiment, the electrolyte is a chloride of lithium and a chloride of an anode active material.
作为更优选方案, 电解质为锂的硫酸盐和负极活性物质的硫酸盐。 As a more preferable embodiment, the electrolyte is a sulfate of lithium and a sulfate of a negative electrode active material.
作为更优选方案, 电解液为水, 溶解有 1M的锂离子和 5M的负极活性物质离子。 作为更优选方案, 电解液为甲醇, 溶解有 1M的锂离子和 5M的负极活性物质离 子。 More preferably, the electrolyte is water, and 1 M lithium ion and 5 M negative electrode active material ions are dissolved. As a more preferable embodiment, the electrolytic solution is methanol, and 1 M lithium ion and 5 M negative electrode active material ion are dissolved.
作为更优选方案, 电解液为乙醇, 溶解有 1M的锂离子和 5M的负极活性物质离 子。 As a more preferable embodiment, the electrolytic solution is ethanol, and 1 M lithium ion and 5 M negative electrode active material ion are dissolved.
作为一个优选方案, 本发明的电池以廉价的 LiMn2O4、 导电剂、 粘接剂制成正极 片, 粘接在石墨集流体、 导电碳纸等上作为正极; 金属锌或锌粉为负极, 电解液中包 括了 lM Li+离子和 5M Zn2+离子。 导电剂为石墨, 粘结剂为 PTFE乳液。 As a preferred embodiment, the battery of the present invention is made of inexpensive LiMn 2 O 4 , a conductive agent, and a binder, and is bonded to a graphite current collector, conductive carbon paper, or the like as a positive electrode; and the metal zinc or zinc powder is a negative electrode. The electrolyte includes lM Li + ions and 5M Zn 2+ ions. The conductive agent is graphite and the binder is a PTFE emulsion.
作为优选方案, 本发明的电池中, 正极与负极之间间隔为 2-10mm时, 可以不 使用隔膜。 Preferably, in the battery of the present invention, when the interval between the positive electrode and the negative electrode is 2 to 10 mm, the separator may not be used.
作为优选方案, 本发明的电池中还包括隔膜时, 隔膜为有机或者无机多孔材料, 所述隔膜的孔径为 0.001-1微米。 Preferably, when the battery of the present invention further comprises a separator, the separator is an organic or inorganic porous material, and the separator has a pore diameter of 0.001-1 μm.
与现有技术相比, 本发明具有以下优点: Compared with the prior art, the present invention has the following advantages:
循环寿命 单位能量 能量密度 资源丰富 环境友好 是否能够 (次) 成本 * *=:* 性 性 做为动力 电池 铅酸电池 300 30% 30% 丰富, 可 铅有毒 为上一代 大量生产 动力电池 镍氢电池 1000 80% 60% 镍资源不 镍为有毒 勉强 镍镉电池 1000 50% 40% 镍资源不 不可能 镍锌电池 300 30% 50% 镍资源不 暂时不能 锌溴电池 2000 30% 40% 丰富, 可 溴腐蚀性 暂时不能 大量生产 强 Cycle life unit energy energy density resource rich environment friendly (time) cost* *=:* sex as a power battery lead-acid battery 300 30% 30% rich, lead toxic for the previous generation mass production battery NiMH battery 1000 80% 60% Nickel resources are not nickel for toxic and bare nickel-cadmium batteries 1000 50% 40% Nickel resources are not impossible Nickel-zinc battery 300 30% 50% Nickel resources are not temporarily unavailable Zinc-bromine battery 2000 30% 40% Rich, bromine corrosive can not be mass produced temporarily
锂离子电池 2000 100% 100% 丰富, 可 比较友好 可能 Lithium-ion battery 2000 100% 100% rich, relatively friendly
大量生产 Mass production
本发明电池 1000以上 20% 60%-70% 丰富, 可 非常友好 可能 The battery of the invention 1000 or more 20% 60%-70% rich, can be very friendly
大量生产 Mass production
*备注: 单位能量成本以目前锂电池为 100%计算。 *Remarks: The unit energy cost is calculated based on the current lithium battery.
**备注: 能量密度以目前锂电池为 100%计算。 **Remarks: The energy density is calculated as 100% of the current lithium battery.
此外, 本发明的电池易于制造, 制造过程不需要水分控制, 容易回收且成本低廉 In addition, the battery of the present invention is easy to manufacture, requires no moisture control during the manufacturing process, is easy to recycle, and is inexpensive.
(同样容量的电池, 可望达到铅酸电池的 60%, 锂离子电池的 20%, 甚至更低) 附图说明 (The same capacity battery is expected to reach 60% of lead-acid batteries, 20% of lithium-ion batteries, or even lower)
图 1是本发明电池的结构示意图, 其中, 1是正极集流体, 2是正极活性物质, 3 是负极活性物质兼做集流体, 4是电解液。 BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a schematic view showing the structure of a battery of the present invention, wherein 1 is a positive electrode current collector, 2 is a positive electrode active material, 3 is a negative electrode active material as a current collector, and 4 is an electrolyte solution.
图 2A是本发明正极材料为 LiAaBeCA的电池充电工作原理示意图。 2A is a schematic view showing the charging operation principle of the battery of the present invention in which the positive electrode material is LiA a B e C A .
图 2B-1和 2B-2是本发明 LiMn2O4/Zn 电池工作原理示意图,其中图 2B-1是电池 充电过程示意图; 图 2B-2是电池放电过程示意图。 2B-1 and 2B-2 are schematic diagrams showing the working principle of the LiMn 2 O 4 /Zn battery of the present invention, wherein FIG. 2B-1 is a schematic diagram of a battery charging process; and FIG. 2B-2 is a schematic diagram of a battery discharging process.
图 3是本发明实施例 1的 LiMn2O4/Zn 电池首次充放电曲线图, 其中 1是充电曲 线图, 2是放电曲线图。 " 3 is a graph showing the first charge and discharge of a LiMn 2 O 4 /Zn battery according to Embodiment 1 of the present invention, wherein 1 is a charge profile and 2 is a discharge curve. "
图 4是本发明实施例 1的 LiMn204/i¾电池循环性能图。 Figure 4 is a graph showing the cycle performance of a LiMn 2 04/i3⁄4 battery of Example 1 of the present invention.
图 5是本发明实施例 3的 LiFePO4/Zn电池循环性能图。 Figure 5 is a graph showing the cycle performance of a LiFePO 4 /Zn battery according to Example 3 of the present invention.
图 6 是本发明实施例 4的 NaVPO^/Zn电池循环性能图。 Fig. 6 is a graph showing the cycle performance of a NaVPO^/Zn battery of Example 4 of the present invention.
图 7是本发明实施例 7的 LiMn2O4/泡沫镍电池循环性能图。 Figure 7 is a graph showing the cycle performance of a LiMn 2 O 4 /foam nickel battery of Example 7 of the present invention.
图 8是本发明实施例 14的 LiMn2O4/Zn电池循环性能图。 Figure 8 is a graph showing the cycle performance of a LiMn 2 O 4 /Zn battery according to Example 14 of the present invention.
图 9是本发明实施例 20的 LiMn2O4/Zn电池充放电效率与充电电流倍率关系曲线 Figure 9 is a graph showing the relationship between charge and discharge efficiency and charge current multiplication of LiMn 2 O 4 /Zn battery in Example 20 of the present invention.
具体实施方式 detailed description
下面结合实施例, 更具体地说明本发明的内容。 应当理解, 本发明的实施并不局 限于下面的实施例,对本发明所做的任何形式上的变通和 /或改变都将落入本发明保护 范围。 The contents of the present invention will be more specifically described below with reference to the embodiments. It is to be understood that the invention is not limited to the embodiments described below, and any form of modifications and/or changes made to the invention are intended to fall within the scope of the invention.
在本发明中, 若非特指, 所有的份、 百分比均为重量单位, 所有的设备和原料等 均可从市场购得或是本行业常用的 实施例 1 In the present invention, unless otherwise specified, all parts and percentages are by weight, all equipment and raw materials, etc. Can be purchased from the market or commonly used in the industry example 1
以 LiMn204为正极活性物质, 按照正极活性物质 88wt%: 导电碳黑 8wt %: 粘接 剂 PTFE (聚四氟乙烯) 4wt %的比例混合均匀, 裁剪成直径 12mm、 厚度 0.1-0.2mm 的圆片, 压制在石墨集流体上, 做成正极。 负极活性物质为宽 15mm、厚度 lmm的金 属锌, 兼作集流体。 正、 负极之间间隔 5mm, 无隔膜。 电解液为含有 lmol/L锂离子 和 5mol/L锌离子的氯化锂和氯化锌的混合水溶液。 在电压范围 U-2.05V之间、 充放 电电流为 0.5C条件下进行循环测试。附图 1显示了电池的基本结构。其首次充放电曲 线图见附图 3, 电池循环性能图见附图 4。 可以看出该电池的充放电曲线与有机电解 液系的锂离子电池非常类似,只是平台低些。 从测试电池来看,循环性能也非常优异。 LiMn 2 0 4 is used as the positive electrode active material, and is uniformly mixed according to the positive electrode active material 88 wt%: conductive carbon black 8 wt%: adhesive PTFE (polytetrafluoroethylene) 4 wt%, and cut into a diameter of 12 mm and a thickness of 0.1-0.2 mm. The wafer is pressed onto a graphite current collector to form a positive electrode. The negative electrode active material was metal zinc having a width of 15 mm and a thickness of 1 mm, and also served as a current collector. The positive and negative electrodes are separated by 5 mm and have no diaphragm. The electrolytic solution was a mixed aqueous solution of lithium chloride and zinc chloride containing 1 mol/L of lithium ion and 5 mol/L of zinc ion. The cycle test was carried out under a voltage range of U-2.05 V and a charge-discharge current of 0.5 C. Figure 1 shows the basic structure of a battery. The first charge and discharge curve is shown in Figure 3, and the battery cycle performance is shown in Figure 4. It can be seen that the charge and discharge curve of the battery is very similar to that of the lithium ion battery of the organic electrolyte system, except that the platform is lower. From the perspective of the test battery, the cycle performance is also excellent.
实施例 2 Example 2
与实施例 1相同的方式制造电池,所不同的是以 LiCoO2作为正极活性物质,循环 操作电压范围为 1.3-1.95V。 其电池循环性能测试结果见表 1。 A battery was fabricated in the same manner as in Example 1, except that LiCoO 2 was used as the positive electrode active material, and the cycle operating voltage ranged from 1.3-1.95 V. The battery cycle performance test results are shown in Table 1.
实施例 3 Example 3
与实施例 1相同的方式制造电池, 所不同的是以 LiFePO4作为正极活性物质, 循 环操作电压范围为 0.8-1.6V。 其电池循环性能测试结果见表 1和附图 5。 A battery was fabricated in the same manner as in Example 1, except that LiFePO 4 was used as the positive electrode active material, and the cycle operating voltage ranged from 0.8 to 1.6 V. The battery cycle performance test results are shown in Table 1 and Figure 5.
实施例 4 Example 4
与实施例 1相同的方式制造电池,所不同的是以 NaVPO4F作为正极活性物质,循 环操作电压范围为 1.3-2.0V。 其电池循环性能测试结果见表 1和附图 6。 A battery was fabricated in the same manner as in Example 1, except that NaVPO 4 F was used as a positive electrode active material, and the cycle operating voltage ranged from 1.3 to 2.0 V. The battery cycle performance test results are shown in Table 1 and Figure 6.
实施例 5 , Example 5
与实施例 1相同的方式制造电池, 所不同的是以 LiMn204和 LiCo02以 1 : 1的质 量比例混合作为正极活性物质,循环操作电压范围为 1.3-2.05V。其充放电和电池循环 性能测试结果见表 1。 容量保持率测试 A battery was fabricated in the same manner as in Example 1, except that LiMn 2 0 4 and LiCo0 2 were mixed at a mass ratio of 1:1 as a positive electrode active material, and the cycle operating voltage ranged from 1.3 to 2.05 V. The test results of charge and discharge and battery cycle performance are shown in Table 1. Capacity retention test
将上述实施例 1-5的电池做循环的充电放电操作,以检测 30个周期之后的电池容 量保持率。首先, 在 0.5C倍率的固定电流下对电池进行充电, 直到电压达到上限, 接 着在 0.5C倍率的固定电流下对电池进行放电, 直到电压达到下限值。 如此周而复始。 The batteries of the above Examples 1-5 were subjected to a cyclic charge discharge operation to detect the battery capacity retention rate after 30 cycles. First, the battery is charged at a fixed current of 0.5 C rate until the voltage reaches the upper limit, and then the battery is discharged at a fixed current of 0.5 C rate until the voltage reaches the lower limit. So repeating this week.
下面的表 1表示了几种不同的正极材料与金属锌作为对电极所展示的电池性能。 Table 1 below shows the battery performance exhibited by several different positive electrode materials and metallic zinc as counter electrodes.
表 1 正极活性 负极活性 作电压 开路电压 首次平均 30周保 物质 物质 ¾围 放电电压 持率 实施例 1 LiMn204 1.3-2.05V 2.0 1.8 92% 实施例 2 LiCo02 1,3-1.95V 1.9 1.7 94% 实施例 3 LiFeP04 金属锌片 0:8-1.6V 1.5 1.2 82% 实施例 4 NaVP04F 1.3-2.0V 1.8 1.4 44% 实施例 5 LiMn204禾口 1.3-2.05V 2.0 1.7 91% Table 1 Positive active negative electrode active as voltage open circuit voltage for the first time average 30 weeks of material retention 3⁄4 surrounding discharge voltage holding rate Example 1 LiMn 2 0 4 1.3-2.05V 2.0 1.8 92% Example 2 LiCo0 2 1,3-1.95V 1.9 1.7 94 % Example 3 LiFeP0 4 metal zinc plate 0: 8-1.6 V 1.5 1.2 82% Example 4 NaVP0 4 F 1.3-2.0 V 1.8 1.4 44% Example 5 LiMn 2 0 4 and 1.3-2.05 V 2.0 1.7 91%
LiCo02 LiCo0 2
其中, LiMn2O4作为正极活性物质, 金属锌作为对电极的电池首次充放电曲线如 附图 3所示, 该电池的循环性能如图 4所示。 根据表 1的显示结果, 可以看到, 对于 比较成熟的正极材料(LiMn204、 LiCo02和 LiMn204/LiCo02), 其电化学性能比其他几种 材料 (LiFeP04、 NaVP04F) 要好很多。 Among them, LiMn 2 O 4 is used as the positive electrode active material, and the first charge and discharge curve of the metal zinc as the counter electrode is shown in FIG. 3 , and the cycle performance of the battery is shown in FIG. 4 . According to the results shown in Table 1, it can be seen that for the more mature cathode materials (LiMn 2 0 4 , LiCo0 2 and LiMn 2 0 4 /LiCo0 2 ), the electrochemical performance is better than that of other materials (LiFeP0 4 , NaVP0 4 ). F) It is much better.
实施例 6 Example 6
以 LiMn204为正极活性物质, 按照正极活性物质 88wt %: 导电碳黑 8wt %: 粘接 剂 PTFE 4wt%的比例混合均匀, 裁剪成直径 12mm, 厚度 0.1-0.2mm的圆片, 压制在 石墨集流体上, 做成正极; 负极活性物质为宽 15mm、 厚度 0.5-lmm的镀锰锌片 (其 中锌的还原性不如锰强, 在充放电过程中不参与反应, 只是作为集流体)。 正、 负极之 间间隔 5mm, 无隔膜。 电解液为含 lmd/L锂离子和 5mol/L锰离子的氯化锂和氯化锰 的混合水溶液。 在电压范围 1.3-2.2V之间, 充放电电流为 0.5C进行循环测试。 LiMn 2 0 4 is used as the positive electrode active material, and is uniformly mixed according to the positive electrode active material 88 wt %: conductive carbon black 8 wt %: adhesive PTFE 4 wt%, and cut into discs having a diameter of 12 mm and a thickness of 0.1-0.2 mm, and pressed at On the graphite current collector, the positive electrode is formed; the negative electrode active material is a manganese-coated zinc plate having a width of 15 mm and a thickness of 0.5-lmm (wherein the reduction property of zinc is not as strong as that of manganese, and does not participate in the reaction during charge and discharge, but acts as a current collector). The positive and negative electrodes are separated by 5 mm and have no diaphragm. The electrolytic solution was a mixed aqueous solution of lithium chloride and manganese chloride containing 1 md/L of lithium ion and 5 mol/L of manganese ion. The cycle test was performed with a voltage range of 1.3-2.2 V and a charge-discharge current of 0.5 C.
实施例 7 Example 7
与实施例 6相同的方式制造电池, 所不同的是以泡沬镍代替镀锰锌板作为负极, 相应地以含 5mol/L镍离子的氯化镍代替含 5mol/L锰离子的氯化锰水溶液作为电解液, 在电压范围 0.8-L5V之间, 充放电电流为 0.5C进行循环测试。其电池循环性能测试结 果见表 2和附图 7。 A battery was fabricated in the same manner as in Example 6, except that instead of a manganese-coated zinc plate as a negative electrode, a nickel chloride containing 5 mol/L of nickel ions was replaced by nickel chloride containing 5 mol/L of nickel ions. The aqueous solution was used as an electrolyte for a cycle test between a voltage range of 0.8-L5V and a charge-discharge current of 0.5C. The results of the battery cycle performance test are shown in Table 2 and Figure 7.
实施例 8 Example 8
与实施例 6相同的方式制造电池, 所不同的是以铁片代替镀锰锌板作为负极, 相 应地以含 5mol L铁离子的氯化铁代替含 5mol L锰离子的氯化锰水溶液作为电解液, 在电压范围 1.3-2.0V之间, 充放电电流为 0.5C进行循环测试。 A battery was fabricated in the same manner as in Example 6, except that an iron sheet was used instead of the manganese-coated zinc plate as the negative electrode, and accordingly, an aqueous solution of manganese chloride containing 5 mol of L manganese ions was replaced by ferric chloride containing 5 mol of iron ions. The liquid is subjected to a cycle test in a voltage range of 1.3 to 2.0 V and a charge and discharge current of 0.5 C.
实施例 9 Example 9
与实施例 6相同的方式制造电池, 所不同的是以镉片代替镀锰锌片作为负极, 相 应地以含 5mol/L镉离子的氯化镉代替含 5mol/L锰离子的氯化锰水溶液作为电解液, 在电压范围 1.3-2.0V之间, 充放电电流 0.5C进行循环测试。 与实施例 6相同的方式制造电池, 万不同的是以压制成型的锌粉末代替镀锰锌片 作为负极, 测试方法与实施例 2相同。 A battery was fabricated in the same manner as in Example 6, except that a cadmium sheet was used instead of the manganese-coated zinc sheet as a negative electrode, and a calcium chloride solution containing 5 mol/L of manganese ions was replaced by cadmium chloride containing 5 mol/L of cadmium ions. As the electrolytic solution, a cycle test was performed with a voltage range of 1.3 to 2.0 V and a charge and discharge current of 0.5 C. A battery was fabricated in the same manner as in Example 6, except that the pressed zinc powder was used instead of the manganese-coated zinc sheet as the negative electrode, and the test method was the same as in Example 2.
实施例 11 Example 11
与实施例 6相同的方式制造电池, 所不同的是以泡沫锌代替鍍锰锌片作为负极, 测试方法与实施例 2相同。 A battery was fabricated in the same manner as in Example 6, except that zinc oxide was used instead of the manganese-coated zinc sheet as the negative electrode, and the test method was the same as in Example 2.
容量保持率测试 Capacity retention test
将上述实施例 1和 6-11中的电池经历循环的充电放电操作, 以检测 30周期之后 的容量保持率。首先,在 0.5C倍率的固定电流下对电池进行充电,直到电压达到上限, 接着在 0.5C倍率的固定电流下对电池进行放电,直到电压达到下限值。如此周而复始。 The batteries in the above Examples 1 and 6-11 were subjected to a cyclic charge discharge operation to detect the capacity retention rate after 30 cycles. First, the battery is charged at a fixed current of 0.5 C rate until the voltage reaches the upper limit, and then the battery is discharged at a fixed current of 0.5 C rate until the voltage reaches the lower limit. So repeating this week.
下面的表 2表示了几种不同金属的负极与 LiMn2O4作为正极活性物质对电极所展 示的电池性能。 Table 2 below shows the battery performance exhibited by the negative electrodes of several different metals and LiMn 2 O 4 as the positive electrode active material counter electrode.
表 2 Table 2
可以看出, 以金属锌, 锌粉末, 泡涉锌和金属镍作为负极组成电池的循环性能最 好, 但镍负极电池的电压较低。对于负 来说, 其可逆性直接影响了电池的循环性能。 锌作为一种成熟的, 研究的比较多的负极, 其循环性能明显好于其他几种材料。 It can be seen that the cycle performance of the battery composed of metal zinc, zinc powder, zinc dioxide and nickel metal as the negative electrode is the best, but the voltage of the nickel negative electrode is low. For negative, its reversibility directly affects the cycle performance of the battery. As a mature, more studied anode, zinc has a significantly better cycle performance than several other materials.
实施例 12 Example 12
与实施例 1 相同的方式制造电池, 所不同的是以含 lmol L锂离子的醋酸锂和含 3mol/L锌离子的醋酸锌的水溶液作为电解液, 循环操作电压范围为 1.3-2.05V。 A battery was fabricated in the same manner as in Example 1, except that an aqueous solution of lithium acetate containing 1 mol of lithium ion and zinc acetate containing 3 mol/L of zinc ion was used as an electrolytic solution, and the cycle operating voltage range was 1.3-2.05V.
实施例 13 Example 13
与实施例 1相同的方式制造电池, , 不同的是以含 lmol/L锂离子的醋酸锂和含 3mol/L锌离子的醋酸锌的甲醇溶液作为电解液, 循环操作电压范围为 1.3-2.05V。 A battery was fabricated in the same manner as in Example 1, except that lithium acetate containing 1 mol/L of lithium ion and methanol solution of zinc acetate containing 3 mol/L of zinc ion were used as the electrolyte, and the cycle operating voltage range was 1.3-2.05V. .
实施例 14 与实施例 1 相同的方式制造电池, 所不同的是以含 lmol/L锂离子的醋酸锂和含 3mol/L锌离子的醋酸锌的乙醇溶液作为 ¾解液,循环操作电压范围为 1.3-2.05V。其电 池循环性能测试结果见表 3和附图 8。 ; Example 14 A battery was fabricated in the same manner as in Example 1, except that lithium acetate containing 1 mol/L of lithium ion and ethanol solution of zinc acetate containing 3 mol/L of zinc ion were used as a solution, and the cycle operating voltage range was 1.3-2.05. V. The battery cycle performance test results are shown in Table 3 and Figure 8. ;
实施例 15 Example 15
与实施例 1相同的方式制造电池, 所不同的是以含 lmol/L锂离子的硫酸锂和含 5mol/L锌离子的硫酸锌的水溶液作为电解液, 循环操作电压范围为 1.3-2.05V。 A battery was fabricated in the same manner as in Example 1, except that an aqueous solution of lithium sulfate containing 1 mol/L of lithium ion and zinc sulfate containing 5 mol/L of zinc ion was used as an electrolytic solution, and the cycle operating voltage range was 1.3-2.05V.
容量保持率测试 Capacity retention test
与实施例 1同样的方法进行测试, 电池电性能如表 3所示。 The test was carried out in the same manner as in Example 1. The battery electrical properties are shown in Table 3.
表 3 table 3
可以看出, 不同的电解液中的电池展示了稍有不同的电化学性能。 对于本发明的 电池而言, 水、 甲醇或乙醇作为电解液都是适宜的。 实施例 14 的循环性能如附图 8 所示。 It can be seen that the batteries in different electrolytes exhibit slightly different electrochemical properties. For the battery of the present invention, water, methanol or ethanol is suitable as the electrolyte. The cycle performance of Example 14 is shown in Figure 8.
实施例 16 Example 16
与实施例 1相同的方式制造电池, 戶 jf不同的是以厚度为 lmm的 316L型不锈钢代 替石墨片作为正极活性物质集流体。 A battery was fabricated in the same manner as in Example 1, except that a 316L type stainless steel having a thickness of 1 mm was used instead of the graphite sheet as a positive electrode active material current collector.
实施例 17 Example 17
与实施例 1相同的方式制造电池,^不同的是以厚度为 lmm的 304型不锈钢代替 石墨片作为正极活性物质集流体。 ' A battery was fabricated in the same manner as in Example 1, except that a 304 type stainless steel having a thickness of 1 mm was used instead of the graphite sheet as a positive electrode active material current collector. '
实施例 18 Example 18
与实施例 1相同的方式制造电池, 所不同的是以碳纤维布 (厚度约 0.1mm) 代替 石墨片作为正极活性物质集流体。 A battery was fabricated in the same manner as in Example 1, except that a carbon fiber cloth (thickness of about 0.1 mm) was used instead of the graphite sheet as a positive electrode active material current collector.
容量保持率测试 Capacity retention test
与实施例 1同样的方法进行测试, 电池电性能如表 4所示。 表 4 The test was carried out in the same manner as in Example 1. The battery electrical properties are shown in Table 4. Table 4
由表 4显示的结果, 可以看出, 以完全电化学惰性的碳系材料作为集流体的电池 循环性能要比用不锈钢作为集流体的好的多。 From the results shown in Table 4, it can be seen that the cycle performance of a battery using a completely electrochemically inert carbon-based material as a current collector is much better than that of using a stainless steel as a current collector.
实施例 19 Example 19
发明人还检测了其他很多种锂离子嵌入型化合物与金属作为对电极组成电池的电 性能。 尽管这些组合的循环性能有很大差异, 但他们都能够形成电池且充放电机理都 基本相同, 都符合本发明电池充放电原理。 表 5显示了多种电极组成方式所组成电池 的放电开路电压。 The inventors have also examined the electrical properties of a variety of other lithium ion-embedded compounds and metals as counter electrodes. Although the cycle performance of these combinations is quite different, they all form batteries and the charge and discharge mechanisms are basically the same, which are in accordance with the principle of charge and discharge of the battery of the present invention. Table 5 shows the discharge open circuit voltages of the batteries composed of various electrode compositions.
表 5不同正负极搭配形成电池的开路电压情况 Table 5 shows the open circuit voltage of the battery with different positive and negative poles
表 5中所列的正负极只是本发明电池可能使用的正负极中的一小部分。 因为依据 本发明原理, 该种电池的可能形式有很多种, 尤其是正极材料, 可以包括当今尚未成 熟的钠离子脱嵌化合物, 以及某些官能团脱嵌化合物等。 The positive and negative electrodes listed in Table 5 are only a small portion of the positive and negative electrodes that may be used in the battery of the present invention. Since there are many possible forms of such batteries in accordance with the principles of the present invention, particularly positive electrode materials, it may include sodium ion intercalation compounds which are not yet matured, as well as certain functional group deintercalation compounds and the like.
实施例 20 Example 20
在水溶液中, 电池充电时在电极表面可能伴随着一系列的副反应, 例如水的分解 等。 以与实施例 1相同的方式制造电池, 使电池在不同的充放电电流倍率下工作, 得 到不同的充放电电流效率。 结果如附图 9所示, 在合适的充电倍率下能够获得 91%以 上的充放电效率。 尽管发明人已经对本发明的技术方案做了较为详细的阐述和列举, 应当理解, 对 于本领域一个熟练的技术人员来说,对上述实施例作出修改和 /或变通或者采用等同的 替代方案是显然的, 都不能脱离本发明精神的实质, 本发明中出现的术语用于对本发 明技术方案的阐述和理解, 并不能构成对本发明的限制。 In an aqueous solution, the battery may be accompanied by a series of side reactions such as decomposition of water, etc., while charging the battery. A battery was fabricated in the same manner as in Example 1 to operate the battery at different charge and discharge current rates to obtain different charge and discharge current efficiencies. As a result, as shown in Fig. 9, a charge and discharge efficiency of 91% or more can be obtained at a suitable charge rate. Although the inventors have made a detailed description and enumeration of the technical solutions of the present invention, it should be understood that it is obvious to those skilled in the art that modifications and/or variations of the above-described embodiments or equivalent alternatives are apparent. The terminology used in the present invention is not to be construed as limiting the scope of the invention.
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