CN1485943A - High specific energy lead-acid battery for electric vehicle - Google Patents

High specific energy lead-acid battery for electric vehicle Download PDF

Info

Publication number
CN1485943A
CN1485943A CNA021396434A CN02139643A CN1485943A CN 1485943 A CN1485943 A CN 1485943A CN A021396434 A CNA021396434 A CN A021396434A CN 02139643 A CN02139643 A CN 02139643A CN 1485943 A CN1485943 A CN 1485943A
Authority
CN
China
Prior art keywords
lead
grid
negative electrode
copper
tin
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CNA021396434A
Other languages
Chinese (zh)
Other versions
CN100347900C (en
Inventor
戴明德
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Guangzhou Warner Energy Technology Co., Ltd.
Original Assignee
戴明德
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 戴明德 filed Critical 戴明德
Priority to CNB021396434A priority Critical patent/CN100347900C/en
Publication of CN1485943A publication Critical patent/CN1485943A/en
Application granted granted Critical
Publication of CN100347900C publication Critical patent/CN100347900C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • 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
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Abstract

The invention is a high specific energy electric vehicle solid accumulator. The vitriol electrolyte is absorbed by silicon dioxide and added with phosphoric acid, boron sulphate, tin sulphate, and kalium sulphate; the accumulator positive and negative diachylon contains tin dioxide, graphite, calcium sulphate, baihuixiong, muna, carbon fiber, duobenduo, polytetrafluoroethylene, barium sulphate, bismuth trioxide, silicon sol, humic acid, and alpha-xiangjing-beta-benzoic acid; and the surface of polar plate is sprayed with trisodium citrate. Its effective high specific power is 5S, the circulation life can reach 10 years; the specific energy is 80wh/kg, and the quick-charge is 100%2h.

Description

High-energy-density electric vehicles solid accumulator
Technical field
The present invention relates to a kind of high-energy-density electric vehicles solid accumulator, belong to the power type accumulator battery field.
Background technology
The storage battery that is used for motor vehicle at present has fuel cell.Produce main material platinum (Pt), the palladium (PZ) of fuel cell, 30 tons of global annual productions, reserves are few, and high price is expensive, the manufacturing technology complexity, technology is immature, and safety in utilization is poor.Other type storage battery, the grid storage battery of the aluminum titanium alloy of producing as storage battery such as sodium, sulphur, hydrogen nickel, NI-G, lithium and China, cost all is higher than the common lead storage battery more than 5 times, and specific energy also reaches 50wh/kg, and cycle life is 500 times.Specific energy is 200wh/kg in the long-term goal of the lead accumulator that the conjuncted body USABC of United States advanced battery formulates; It is that charging 100% is 30min that the electric vehicle storage battery that the international advanced battery exploitation ALABC of association formulates fills tortoise time target again.The high-energy-density of lead accumulator is 200wh/kg, and the cycle life number of times is 10,000 times, but above-mentioned be to extravagantly hope still to fail to realize.
Lead accumulator is adsorbed in silicon dioxide (SnO with sulfuric acid electrolyte 2.nH 2O) technology, Japan Patent are openly speciallyyed permit the report that 5-151988 rock Tian Hanxing patent has been loaded with China R﹠D institution: its performance all is better than lead acid storage battery and separates liquid and negative electrode absorption type sealing excide battery.But really throw in practical application and can satisfy the use needs electrokinetic cell still in development.
Technology contents
The objective of the invention is, develop high-energy-density electric vehicles solid accumulator, have environmental protection and energy saving, the life-span is long, cost is low characteristics, be high-energy-density, economical product.
Technical scheme of the present invention, described high-energy-density electric vehicles solid accumulator comprise shell, loam cake, have the anode plate grid of lug and negative electrode grid, bus-bar, end pole and polar biased post, electric liquid liquid, and its technical characterictic is:
1, anode plate grid is after plating 4-6 μ m silver layer on the thick copper material of 0.2-0.3mm, again the structure of the thick lead layer of plating 5-15 μ m on silver layer;
Negative electrode grid is after plating 5-10 μ m tin layer on the thick copper material of 0.2-0.3mm, again the structure of the thick lead layer of plating 5-15 μ m on the tin layer;
Anode plate grid is 1.0-1.30 with the ratio of negative electrode grid thickness: 1, and anode plate grid is than the negative electrode grid dress of manying a slice; Be that the perforated plastic dividing plate of 0.1-0.2mm, the thick 0.8-1.2mm of muscle, porosity 80-95% is isolated with thickness between the described positive and negative electrode grid;
The lug of the positive and negative pole plate of bus-bar is that the zinc-plated copper rod of 0.4-6mm is connected in parallel with diameter respectively;
The polar biased post by thickness 0.5-5mm copper coin zinc-plated after again the lead-sheathing alloy constitute, and the copper material volume accounts for the 55%-65% of whole polar biased column volume; The end pole by the copper rod electroplating surfaces with tin after lead-sheathing alloy composition again, and the copper material volume accounts for the 55%-65% of whole end pole volume;
2, the composition of additive (in electrolyte weight) is in the electrolyte: phosphatase 11-2%, sulfuric acid boron 0.05-0.1%, STANNOUS SULPHATE CRYSTALLINE 0.02-0.05%, sodium sulphate 0.01-0.05, potassium sulfate 0.002-0.005%;
3, described anode plate grid is coated with the weight portion prescription of copper cream and is: 100 parts in particle diameter 1-2 μ m lead powder, ionized water 12-15L, concentration is 38-40% sulfuric acid 6-8L, tin ash 1-2%, particle diameter is 125-250 μ m graphite 4-8 part, calcium sulfate 1-2 part, wood are received 0.1-0.15 part, white carbon 0.3-0.5 part, diameter 0.5-1.0 μ m, length 1-2mm carbon fiber 0.5-1.0 part, many many 3-4 of benzene parts, ptfe emulsion 1-2 part, black phosphorus 0.02-0.05 part; The apparent density of making lead plaster according to a conventional method is 38-40 ± 1
Described negative electrode grid is coated with lead plaster weight portion prescription: 100 parts in particle diameter 1-2 μ m lead powder, concentration 48-50% sulfuric acid 4-6L, ionized water 11-13L, tin ash 0.1-0.2 part, 240-260 order barium sulfate 0.001-0.003 part, 70-80 order humic acid 0.3-0.5 part, 70-80 order a-hydroxy-beta benzoic acid 1-2 part, bismuth trioxide 0.5-1 part, ptfe emulsion 1-2 part, Ludox 0.5-1 part, diameter 1-2 μ m, long 1-2mm carbon fiber 0.5-1.5 part, making the lead plaster apparent density according to a conventional method is 38-40 ± 1
4, at positive and negative electrode grid surface spraying trisodium citrate (NaC 6H 5O 7) layer, coating thickness 0.05-0.1 μ m.
The present invention is on prior art accumulator structure basis (original structure is constant substantially), realizes with material, electrolysis additive and lead paste formula that the positive and negative electrode grid is coated with etc. through improvement positive and negative electrode grid.
Development principle of the present invention is, with conductance height, big, the heatproof perfect heat-dissipating of overcurrent, the copper that density is little is used for positive and negative pole plate grid of the present invention, and storage battery bus-bar, polar biased post, end pole use copper material), anode plate grid silver-plated (Ag), lead plating (Pb); Negative electrode grid zinc-plated (Sn), lead plating (Pb), bus-bar, polar biased post, zinc-plated, casting lead can reduce accumulator internal resistance and parts weight, the multiplication activity material in a large number.The present invention adopts the lead plaster of special development, can increase active material hole, increase operation rate, can improve capacity, strengthen the adhesive force of lead plaster, slow down the loose of lead plaster, early fallout reaches the purpose in the life-span that prolongs storage battery.The present invention develops the additive in the sulfuric acid electrolyte that is adsorbed in silicon dioxide, makes that the ion migration velocity obtains accelerating, conductance is brought up to 84-86%, and extending battery life, raising battery capacity.
According to the mechanism of accumulator cell charging and discharging, accumulator anode board all is in corrosion area when discharging and recharging.Though copper is not dissolved in dilute sulfuric acid in theory, because the polarized state of difference is inconsistent on the pole plate, the most advanced and sophisticated polarity effect in battery lead plate inferior horn or all burrs position, copper is easily to be dissolved in dilute sulfuric acid.Enter the Cu in the electrolyte + 2Storage battery is harmful to.So grid of the positive and negative pole plate of high-energy-density electric vehicles solid accumulator, adopt the above copper coin of thickness 0.1mm, utilize the surplus limit punch forming of the rectangle grid of preparation copper coin grid, purpose is the adhesive force that supports the amount of the active material that doubles and strengthen active material.
The characteristics of the high-energy-density electric vehicles solid accumulator of the present invention's preparation have: 1, specific energy 〉=80wh/kg (C/3 discharge); 2, specific power 250w/kg (80%DOD); 3, cycle-index is 1000 times; 4, rated voltage 2-48V; 5,100% time of quick charge 〉=2n; 6, self discharge is atomic, and full charge is deposited 2 years power losses 20%; 7, high specific power 〉=5s; 8, the old storage battery rate of recovery 〉=98%; 9, suitable environment temperature-40 is ℃ to 80 ℃; 10, accumulator without maintenance; 11, production cost is low, price 400-500 yuan/kwh; 12, do not have corrosion, the band lotus is dispatched from the factory.
High-energy-density electric vehicles solid accumulator of the present invention is applied to motor vehicle and anti-dark power-cycled field, belongs to environment-friendly and energy-efficient, and the life-span is long, price is low, Eco-power storage battery.
As known from the above, the present invention is a high-energy-density electric vehicles solid accumulator, has the specific energy height, specific power is big, cycle-index is many, self discharge is small, full charge is deposited characteristics such as power loss is little, production cost is low.
Embodiment
An embodiment of the present invention product structure and manufacturing process are described as follows.
The preparation of a, positive and negative pole plate copper coin grid, bus-bar, polar biased post, end pole:
1, the ratio of the extremely positive and negative grid thickness of battery is 1.10-1.3: 1.0, and utmost point grid depth-width ratio is 0.7: 1.0; The perpendicular muscle of grid is 1.0: 0.8 with the ratio of the width of horizontal bar, and perpendicular muscle number is 1.0: 0.7 with the ratio of horizontal bar number; The thickness 0.1mm of grid, the grid grid strikes out rectangle, borrows to be pressed into the corresponding rectangle of quantity towards the surplus limit of grid and periphery makes progress into II shape, and peripheral II height is the thickness of grid.The plate ear of positive/negative plate places 2/5ths places of pole plate partial center distance, the wide 10-30mm of lug, high 10-30mm, in the high 8-20mm of lug position, to wide horizontal direction towards the hole of diameter 1mm more than 1.Plate railings of anode and cathode is pressed the electroplating technology plating then.Anodal copper coin grid silver-plated (Ag), thickness 0.5um, lead plating thickness 10 μ m again.The negative thick 0.6um of grid zinc-plated (Sn), lead plating again (Pb), thick 10 μ m.Grid periphery plastic-blasting material, the wide 1-3mm of plastic-blasting material, thick 0.5 μ m.
The preparation of b, conflux grate part:
The bus-bar effect be storage battery when discharge process, transfer chemical energy to electric energy.The electric energy of multi-disc pole plate compiles through bus-bar, powers to electrical appliance.During charging, be with external electric energy through bus-bar, be transferred to battery pole plates, electric energy is converted into chemical energy.The length and width of bus-bar, thickness are by the size of storage battery power, and how many polar plate numbers decides, through bus-bar one in parallel.Through positive and negative extreme pole, with electric current output or input.The voltage of whole storage battery is high and low be many by the cell batteries series connection, form less.Advanced storage battery is used through-wall welding for reducing resistance, and spot welding connects the polar biased post, with cell batteries series connection (but external latticing connecting mode is arranged).What of polar biased post are by how many decisions of Series Sheet accumulator body; The quantity of end pole is: monomer or whole storage battery have only positive and negative electrode (being the positive and negative utmost point), and the end pole is two.
The current density of copper is 8A/mm 2, overcurrent density is 10 times of above-mentioned current densities 25 ℃ of temperature and at 30min.Main physical performance because of copper: conductance is good, and thermal diffusivity is strong, the fusing point height, and resistivity is 1.7*10 -6Ω/cm, density is 8.99g/cm 3Because of copper has the drawback that produces kelvin effect, the diameter of copper conductor is during greater than 5mm, and current density reduces, and is not more than 5mm with copper coin grid thickness, need during greater than 5mm with many copper rods (or multiply copper stranded conductor).
The structure of bus-bar is a sheath copper, and because of the welding difficulty is big, so sheath copper, the volume of copper accounts for the volume about 3/5ths of bus-bar.All the other are lead alloy, the minimum 3mm of the thickness of bus-bar.
The fastening copper rod diameter of the company of wearing is not more than 4.8mm, and length is determined by the storage battery watt level; The thickness of polar biased post copper coin is not more than 5mm, widens the polar biased post in case of necessity; The copper rod diameter of end pole is not more than 5mm, adopts many copper stranded conductors in case of necessity.
The copper rod of the fastening pole plate of the company of wearing is zinc-plated, zinc-plated thick 0.6 μ m.Polar biased post copper coin is zinc-plated, and zinc-plated thickness 0.6 μ m is plumbous with the punching block casting then; The inclined to one side post in the two poles of the earth is worn the face of weld of wall contact, the thickness 0.5mm that casting is plumbous.
The copper core height of end pole and diameter are by the watt level decision of storage battery.Diameter is not less than 3mm, and the available copper post that is molded into, diameter are used the multiply copper stranded conductor during greater than 5mm.The copper core of end pole, zinc-plated thickness 0.6 μ m.Use die casting lead.The casting lead thickness of end pole top, bottom is not more than 2mm, and all the other positions are not more than 10um.
The general assembly of C, storage battery:
The general assembly of a, storage battery is with accumulator positive, negative plate, places the comb pattern of mould respectively, and the copper rod of the fastening pole plate of the company of wearing of preparation is worn along the lug hole, and lug is fastening.Polar biased post or end pole place comb pattern appropriate location, casting or welding alloy lead, and quality requirement does not have rosin joint, crackle, burr, want firmly, then at the side face and the high 10mm of the lug place of bus-bar, and the polar biased post is when the storage battery general assembly, and coating thickness 2 μ m plastics are anticorrosion.
Dividing plate between b, accumulator positive, negative plate is bored a hole with plastics, and porosity is not less than 90%, the thick 0.2mm of dividing plate base plate, the thickness 1.0mm of rib, total thickness 1.2mm.
C, storage battery total coating process flow process are once covered heat-sealing-air tight test-sealing end pole-perfusion electrolyte sulfuric acid-storage battery secondary lid heat-sealing-charging-accumulator property check for can-dress foam plate washer-storage battery that utmost point group welding-slotting dividing plate-high voltage detects insulation-through-wall welding between the storage battery positive and negative electrode-big current detecting quality of welding spot-silicon dioxide.
The technical conditions of d, silicon dioxide:
The high-load (in weight %) of impurity: 1, water-soluble substance 0.2; 2, hydrofluoric acid nonvolatile matter≤1.0; 3, dry vector≤3.0; 4, chloride (Cl)≤0.005; 5, sulfate (SO 4)≤0.005; 6, calcium (ca)≤0.005; 7, iron (Fe)≤0.005; 8, heavy metal (in Pb)≤0.005; 9, particle diameter 1-10 μ m white foam; 10,1670 ℃ of fusing points.
E, ionized water (H 2O) technical conditions:
The high-load (in weight %) 1 of impurity, outward appearance, water white transparency; 2, total residue content 0.00005; 3, manganese (Mn)≤0.000005:4, iron (Fe)≤0.000001; 5, chlorine (Cl)≤0.000001:6, ammonium (NH 4)≤0.00008:7, nitrate (HNO 4) (N meter), contain (NO 3) 0.00001; 8, reduction permanganic acid acid potassium (KMnO) content of material≤0.000005; 9, metal oxide is with (C in the alkali 2The O meter)≤and 0.00008:10, calcium magnesium oxide (C 2O and MgO)≤0.00001; 11, nitrite (HNO 2)≤0.0001; 12, resistance value is not less than 10 megaohms.
F, the electrolytical preparation of high-energy-density electric vehicles solid accumulator.
Electrolytical preparation: tie up to mix automatically in the machine of stirring and carry out.
The sulfuric acid that will meet enterprise's target ionized water and meet the GB625-89 standard places with 2.49: 1 ratio and mixes the machine of stirring and mix that to stir 1-3min even, with diluted acid sulphur (H 2SO 4) weight meter (%), additive: meet the country and the element of company standard: 1, phosphoric acid 2.0; 2, sulfuric acid boron 0.10; 3, sour tin 0.05; 4, sodium sulphate 0.05; 5, potassium sulfate 0.005; Mix then that to stir 1-3min even.Electrolyte pours into high-energy-density electric vehicles solid accumulator at normal temperatures, and liquid level is to foam phenolic aldehyde plate washer.
The technical conditions and the preparation thereof of g, high specific energy electric vehicles solid accumulator pole plate
The technical conditions of i, anode plate lead plaster:
A, lead powder 100kg, b, sulfuric acid quality 40% quantity 7L; C, ionized water quantity 13L.
All the other weight (%): d, tin ash 1.5 in lead powder; E, graphite (particle diameter Φ 125-250 order) 5.0; F, calcium sulfate 1.5; H, white carbon 0.8; I, charcoal fiber (the long 1-2mm of Φ 0.1-1.0 μ m) 1.0%; Many benzene many 3.0; K, ptfe emulsion 1.5L, black phosphorus 0.04; M, the lead plaster apparent density is 40 ± 1
2, the preparation of anode diachylon and be coated with cream:
Advanced lead plaster preparation method makes cream fast with vacuum.Be example now, lead powder placed anodal paste mixing machine, add tin ash, graphite, calcium sulfate, Mu Na, white carbon, charcoal fiber with paste mixing machine and cream method, fully mix mix stir well even; Add ionized water, many, the ptfe emulsion of many benzene, fully mix to mix stirring well evenly, add sulfuric acid then, mix and stir time 45min, temperature is controlled to be 63-67 ℃., go out pilling up time 20min behind the cream, with the mechanical or manual cream that is coated with.The positive grid coating paste of copper, excessive 〉=10%.Pole plate is through pickling-drying-solidify-change into drying, and in the two surface spraying of pole plate lemon trisodiums, thickness is not more than 1 μ m then.
3, the technical conditions of accumulator negative plate lead plaster;
A, lead powder 100kg; B, sulfuric acid; (quality 50%) 5L; C, ionized water 12L; D, barium sulfate 3g; E, humic acid 0.4kg; All the other are in lead powder weight (%): f, bismuth trioxide, 1.0; 8, ptfe emulsion 2.0; H, Ludox 1.0; J, fiber 1.0; K, apparent density 40 ± 1.
4, the preparation of cathode lead plaster and be coated with cream:
Lead powder is placed the negative pole paste mixing machine, add barium sulfate, humic acid, tin ash, a-Xiang stem-β-benzoic acid, bismuth trioxide, charcoal fiber are fully mixed and are stirred, and the continuous ionized water, Ludox of adding mixed and stirred well evenly, adds sulfuric acid again and mixes and stir time 45min.63-67 ℃ of temperature control.After going out cream, stack 20min, adopt plaster coating machine or be coated with cream to the topped copper coin grid of lead plaster by hand.Pole plate is through pickling, and------solidify---changing into---drying, at polar board surface spraying trisodium citrate, thickness is not more than 1 μ m to drying then.
High-energy-density electric vehicles solid accumulator primary charging process conditions:
One, charge condition:
1, the storage battery primary charging is to carry out in water bath with thermostatic control.
2, the constant temperature of water is 25 ℃ ± 2 ℃.
Two, charging method
1, storage battery connecting mode: serial or parallel connection.
2, charging modes: constant current pressure limiting method, step charge.
3, the first sections, charging current is 0.07C 20, constant current is specified when pressing 12V to whole storage battery, and pressure limiting is 14V, charging 6h.
4, second section, charging current is 0.03-0.05C 20, pressure limiting is 16V, charging 24n.
5, charging finishes preceding with 0.05C 20, charging voltage is placed restrictions on and is 18V.Make charge in batteries voltage and charging current keep 3h., stablize the constant abundance of looking.
6, during charge in batteries, the temperature of intermediate is not more than 45 ℃.
7, storage battery primary charging, the capacity of charging into are 1.2--2.4 times of rated capacity.

Claims (1)

1, a kind of high-energy-density electric vehicles solid accumulator comprises shell, loam cake, has the anode plate grid of lug and negative electrode grid, bus-bar, end pole and polar biased post, electric liquid liquid, it is characterized in that,
(1), anode plate grid is on the thick copper coin of 0.2-0.3mm behind the plating 5-10 μ m tin layer, the structure of the thick lead layer of plating 5-15 μ m on the tin layer again;
Negative electrode grid is after plating 4-6 μ m tin layer on the thick copper material of 0.2-0.3mm, again the structure of the thick lead layer of plating 5-15 μ m on the tin layer;
Anode plate grid is 1.10-1.30 with the ratio of negative electrode grid big and heavy stone degree: 1, and anode plate grid is than the negative electrode grid dress of manying a slice; Be that the perforated plastic dividing plate of 0.1-0.2mm, muscle thickness 0.8-1.2mm, porosity 80-95% is isolated with thickness between the described positive and negative electrode grid;
The lug of the positive and negative pole plate of bus-bar is that the zinc-plated copper rod of 0.4-6mm is connected in parallel with diameter respectively;
The polar biased post by thickness 0.5-5mm copper coin zinc-plated after again the lead-sheathing alloy constitute, and the copper material volume accounts for the 55%-65% of whole polar biased column volume; The end pole by the copper rod electroplating surfaces with tin after lead-sheathing alloy composition again, and the copper material volume accounts for the long-pending 55%-65% of whole end polar body;
(2), the composition of additive (in electrolyte weight) is in the electrolyte: phosphatase 11-2%, sulfuric acid boron 0.05-0.1%, STANNOUS SULPHATE CRYSTALLINE 0.02-0.05%, sodium sulphate 0.01-0.05, potassium sulfate 0.002-0.005%;
(3), described anode plate grid is coated with the weight portion prescription of copper cream and is: 100 parts in particle diameter 1-2 μ m lead powder, ionized water 12-15L, concentration is 38-40% sulfuric acid 6-8L, tin ash 1-2%, particle diameter is 125-250 μ m graphite 4-8 part, calcium sulfate 1-2 part, wood are received 0.1-0.15 part, white carbon 0.3-0.5 part, diameter 0.5-1.0 μ m, length 1-2mm carbon fiber 0.5-1.0 part, many many 3-4 of benzene parts, ptfe emulsion 1-2 part, black phosphorus 0.02-0.05 part; The apparent density of making lead plaster according to a conventional method is 38-40 ± 1
Described negative electrode grid is coated with lead plaster weight portion prescription: 100 parts in diameter of phi 1-2 μ m lead powder, concentration 48-50% sulfuric acid 4-6L, ionized water 11-13L, tin ash 0.1-0.2 part, 240-260 order barium sulfate 0.001-0.003 part, 70-80 order humic acid 0.3-0.5 part, 70-80 order a-hydroxy-beta benzoic acid 1-2 part, bismuth trioxide 0.5-1 part, ptfe emulsion 1-2 part, Ludox 0.5-1 part, diameter 1-2 μ m, long 1-2mm carbon fiber 0.5-1.5 part, making the lead plaster apparent density according to a conventional method is 38-40 ± 1
(4), be coated with the thick lemon trisodium layer of 0.05-1 μ m on positive and negative electrode grid surface.
CNB021396434A 2002-09-26 2002-09-26 High specific energy lead-acid battery for electric vehicle Expired - Fee Related CN100347900C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNB021396434A CN100347900C (en) 2002-09-26 2002-09-26 High specific energy lead-acid battery for electric vehicle

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNB021396434A CN100347900C (en) 2002-09-26 2002-09-26 High specific energy lead-acid battery for electric vehicle

Publications (2)

Publication Number Publication Date
CN1485943A true CN1485943A (en) 2004-03-31
CN100347900C CN100347900C (en) 2007-11-07

Family

ID=34147481

Family Applications (1)

Application Number Title Priority Date Filing Date
CNB021396434A Expired - Fee Related CN100347900C (en) 2002-09-26 2002-09-26 High specific energy lead-acid battery for electric vehicle

Country Status (1)

Country Link
CN (1) CN100347900C (en)

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1317789C (en) * 2005-06-24 2007-05-23 沈涛 Valve controlling type sealed lead acid battery with Nano carbon in electrolyte
CN101034739B (en) * 2006-10-26 2010-10-27 首天恩管理有限公司 Conduction connector for the accumulator and accumulator
CN101924251A (en) * 2010-09-08 2010-12-22 江苏理士电池有限公司 Method for fabricating maintenance-free motorcycle battery with novel terminal structure
CN101964421A (en) * 2010-09-16 2011-02-02 南京双登科技发展研究院有限公司 Super lead storage battery anode active substance for electric automobile
CN101685884B (en) * 2008-09-26 2012-07-11 深圳市夺标环保技术有限公司 Electrolyte of lead-acid battery and preparation method thereof
CN101877402B (en) * 2009-09-18 2012-07-25 华南师范大学 Negative plate of storage battery and manufacturing method thereof
CN103022430A (en) * 2012-11-28 2013-04-03 上海锦众信息科技有限公司 Method for preparing negative-pole lead plaster for lead-carbon storage battery
CN103904331A (en) * 2012-12-31 2014-07-02 陈荣 Formula of additive for improving low-temperature charge property of lead-acid storage battery
CN105932266A (en) * 2016-05-12 2016-09-07 福建紫雄能源发展有限公司 Automobile accumulator
CN106058246A (en) * 2016-08-03 2016-10-26 湖北润阳新能源有限公司 Lead paste formula for positive electrode of lead acid storage battery
US9985281B2 (en) 2015-06-24 2018-05-29 Cabot Corporation Carbonaceous materials for lead acid batteries
CN110071267A (en) * 2019-02-28 2019-07-30 天能电池集团有限公司 A kind of positive plate of lead storage battery lead paste formula
CN111969257A (en) * 2020-08-24 2020-11-20 海志电源技术(赣州)有限公司 Manufacturing method of high-specific-energy power lead-acid battery
CN113394400A (en) * 2021-05-26 2021-09-14 天能电池集团股份有限公司 Negative pole diachylon and negative plate of lead storage battery and lead storage battery

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2239020A2 (en) * 1973-07-24 1975-02-21 Fulmen Electric lead-acid accumulator - has negative grid plate of plastic material with metallic coating
DE3922425A1 (en) * 1989-07-07 1991-01-17 Hoechst Ag ELECTRODE FOR GALVANIC PRIMARY AND SECONDARY ELEMENTS
CN1135101A (en) * 1996-01-05 1996-11-06 海南辉业发展有限公司 Solid accumulator
CN1162931C (en) * 1999-06-06 2004-08-18 戴明德 Process for preparing high-conductivity colloidal electrolyte of electric accumulator and pouring it

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1317789C (en) * 2005-06-24 2007-05-23 沈涛 Valve controlling type sealed lead acid battery with Nano carbon in electrolyte
CN101034739B (en) * 2006-10-26 2010-10-27 首天恩管理有限公司 Conduction connector for the accumulator and accumulator
CN101685884B (en) * 2008-09-26 2012-07-11 深圳市夺标环保技术有限公司 Electrolyte of lead-acid battery and preparation method thereof
CN101877402B (en) * 2009-09-18 2012-07-25 华南师范大学 Negative plate of storage battery and manufacturing method thereof
CN101924251A (en) * 2010-09-08 2010-12-22 江苏理士电池有限公司 Method for fabricating maintenance-free motorcycle battery with novel terminal structure
CN101964421A (en) * 2010-09-16 2011-02-02 南京双登科技发展研究院有限公司 Super lead storage battery anode active substance for electric automobile
CN103022430A (en) * 2012-11-28 2013-04-03 上海锦众信息科技有限公司 Method for preparing negative-pole lead plaster for lead-carbon storage battery
CN103904331A (en) * 2012-12-31 2014-07-02 陈荣 Formula of additive for improving low-temperature charge property of lead-acid storage battery
US9985281B2 (en) 2015-06-24 2018-05-29 Cabot Corporation Carbonaceous materials for lead acid batteries
US10862109B2 (en) 2015-06-24 2020-12-08 Cabot Corporation Carbonaceous materials for lead acid batteries
CN105932266A (en) * 2016-05-12 2016-09-07 福建紫雄能源发展有限公司 Automobile accumulator
CN106058246A (en) * 2016-08-03 2016-10-26 湖北润阳新能源有限公司 Lead paste formula for positive electrode of lead acid storage battery
CN110071267A (en) * 2019-02-28 2019-07-30 天能电池集团有限公司 A kind of positive plate of lead storage battery lead paste formula
CN111969257A (en) * 2020-08-24 2020-11-20 海志电源技术(赣州)有限公司 Manufacturing method of high-specific-energy power lead-acid battery
CN111969257B (en) * 2020-08-24 2022-02-01 海志电源技术(赣州)有限公司 Manufacturing method of high-specific-energy power lead-acid battery
CN113394400A (en) * 2021-05-26 2021-09-14 天能电池集团股份有限公司 Negative pole diachylon and negative plate of lead storage battery and lead storage battery

Also Published As

Publication number Publication date
CN100347900C (en) 2007-11-07

Similar Documents

Publication Publication Date Title
CN100347900C (en) High specific energy lead-acid battery for electric vehicle
CN104835965B (en) A kind of motorcycle lead carbon battery and preparation method thereof
CN104577119B (en) Preparation method of cathode material LiMn1-xFexPO4 for lithium ion cell
US5045170A (en) Electrodies containing a conductive metal oxide
CN101291002B (en) Colloidal electrolyte of lead acid batteries
CN102664256A (en) Anode lead plaster of power lead-acid storage battery polar plate
CN107452947B (en) Lead paste for positive plate of lead storage battery, preparation method of lead paste and lead storage battery
CN109585804A (en) A kind of FeSxThe preparation method and application of/C/CNT composite negative pole material
CN104993154A (en) Graphene-containing lead alloy for lead storage battery grids, and preparation method thereof
CN105375034A (en) Lithium-ion battery current collector and preparation method thereof and lithium-ion battery
CN109585798A (en) Graphene lead composite material and its preparation method and application and anode diachylon, cathode lead plaster
CN104562094A (en) Preparation method of gradient composite anode for nonferrous metals electrodeposition
CN111934028B (en) Lead-acid battery manufacturing method based on conductive adhesive and lead sulfate
CN109411706A (en) A kind of modified working electrode and preparation method thereof
CN104332594A (en) Silicon-based negative electrode material and preparation method and application thereof
CN108461831A (en) A kind of novel storage battery manufacturing method
CN1294418A (en) Alloy material for lattice plate of deeply cyclic battery
CN106229463A (en) A kind of aquo-lithium ion hybrid battery
CN108808010A (en) A kind of Moped Scooter positive electrode grid of lead storage battery alloy and preparation method thereof
CN108682865A (en) Highly corrosion resistant grid and the lead carbon battery and pole plate for having the highly corrosion resistant grid
CN114678490A (en) Lithium ion battery negative plate and preparation method thereof
CN107760922A (en) A kind of high-energy power slab lattice alloy of lead-acid battery and preparation method thereof
CN108400374A (en) A kind of high specific energy lithium ion battery
CN108550854B (en) Positive lead plaster of lead storage battery and preparation method thereof
CN1264238C (en) Valve controlled lead acid cell with composite oxides additive contained in positive electrode

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
ASS Succession or assignment of patent right

Owner name: LAN GUOXIAN; APPLICANT

Free format text: FORMER OWNER: DAI MINGDE

Effective date: 20060421

C41 Transfer of patent application or patent right or utility model
TA01 Transfer of patent application right

Effective date of registration: 20060421

Address after: Room 11, building H, No. 34-36 Hongkong A big industrial center Fo Tan Au Pui Wan Street

Applicant after: Lan Guoxian

Co-applicant after: Dai Mingde

Address before: 419500 No. 240, Longjing street, Chen Yang Town, Chenxi County, Hunan

Applicant before: Dai Mingde

C14 Grant of patent or utility model
GR01 Patent grant
ASS Succession or assignment of patent right

Owner name: GUANGZHOU WANAENER SCIENCE + TECHNOLOGY CO., LTD.

Free format text: FORMER OWNER: LAN GUOXIAN

Effective date: 20111027

Free format text: FORMER OWNER: DAI MINGDE

C41 Transfer of patent application or patent right or utility model
COR Change of bibliographic data

Free format text: CORRECT: ADDRESS; FROM: HONG KONG, CHINA TO: 510530 GUANGZHOU, GUANGDONG PROVINCE

TR01 Transfer of patent right

Effective date of registration: 20111027

Address after: Luogang District Tiantai road Guangzhou City, Guangdong province 510530 No. 1 room 315

Patentee after: Guangzhou Warner Energy Technology Co., Ltd.

Address before: Room 11, building H, A 34-36, China Hongkong Fengsheng industrial center Fo Tan Au Pui Wan Street

Co-patentee before: Dai Mingde

Patentee before: Lan Guoxian

C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20071107

Termination date: 20130926