CN106981609A - A kind of lead accumulator dividing plate and lead accumulator - Google Patents
A kind of lead accumulator dividing plate and lead accumulator Download PDFInfo
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- CN106981609A CN106981609A CN201710188095.8A CN201710188095A CN106981609A CN 106981609 A CN106981609 A CN 106981609A CN 201710188095 A CN201710188095 A CN 201710188095A CN 106981609 A CN106981609 A CN 106981609A
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- sea
- copet
- dividing plate
- island
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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
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/409—Separators, membranes or diaphragms characterised by the material
- H01M50/411—Organic material
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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
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/409—Separators, membranes or diaphragms characterised by the material
- H01M50/44—Fibrous material
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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
- H01M10/06—Lead-acid accumulators
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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
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
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- General Chemical & Material Sciences (AREA)
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Abstract
The invention discloses a kind of lead accumulator dividing plate and lead accumulator, the composition of the lead accumulator dividing plate includes glass fibre and COPET sea island filaments, wherein, the COPET sea island filaments are obtained by PA/COPET sea-island fibres after molten sea processing.Lead accumulator dividing plate of the present invention with the addition of COPET sea island filaments in the preparation, and the COPET sea island filaments are obtained by PA/COPET sea-island fibres after molten sea processing.After sea-island fibre separation, filament number is thinner, and conventional spinning can not possibly be accomplished, therefore it has the characteristic that general fiber can not possibly have.The more common AGM dividing plates of lead accumulator dividing plate of the present invention have the advantages that suction acid amount is high, durable pressure is big, tensile break strength is big, with good application prospect.
Description
Technical field
The present invention relates to lead accumulator production technical field, more particularly to a kind of lead accumulator dividing plate and lead accumulator.
Background technology
The history in lead accumulator the present in existing more than 150 years, and application field is widely.In recent years, electric car was preferable with its
Performance of riding instead of walk, relatively low storage space requirement and outstanding price advantage in China's fast development, have benefited from this, battery production
Industry has also obtained rapid development.
Lead accumulator is mainly made up of positive and negative pole plate and dividing plate, housing, electrolyte, pole etc..In lead accumulator every
Plate not only plays a part of separated positive/negative plate, and requires that dividing plate has that porosity is high, aperture is small, oxidation resistance is strong, can
Absorb and keep enough electrolyte, there are the characteristics such as good compression rebound.If the clapboard aperture of lead accumulator is too big easy
The penetration of lead dendritic crystal dividing plate of accumulator plate is caused to cause the short circuit of battery, the compression resilience difference of dividing plate can cause lead accumulator
Assembling pressure is too low and fail after the discharge and recharge of a period of time is carried out, and the acid difference of suction of dividing plate can cause lead accumulator circulating
During acid deficient and fail.The dividing plate of current lead accumulator is substantially AGM dividing plates, and its main component is glass fibre.Due to glass
Glass fiber is extracted at random by flame method, and the fineness and length of its fiber are uneven, and current glass fibre is most thin
0.8 μm -1.59 μm can be accomplished, cause that the maximum diameter of hole of the glass fibre separator prepared is larger, pore-size distribution is uneven,
And compression resilience is poor.
In order that the performance of AGM dividing plates is more excellent, some additives can be typically added into AGM dividing plates.Such as:
Authorization Notice No. discloses a kind of AGM baffle of storage battery and its preparation for CN103855346B Chinese invention patent
Method, the AGM baffle of storage battery includes high alkali glass cotton, medium-alkali glass fibre, bicomponent polyester fiber, contains SiO2Particle
Glue, the high alkali glass cotton, medium-alkali glass fibre, bicomponent polyester fiber, contains SiO2The percentage by weight of the glue of particle is
81~87: 2.8~4.6: 1.8~3.7: 8.3~11.4.
Authorization Notice No. discloses a kind of baffle plate of lead acid storage battery and its system for CN 102623659B Chinese invention patent
Preparation Method, the dividing plate is using glass fibre as principal component, also comprising the vistanex that 10%~20% fusing point is 100~200 DEG C
Fiber.
Publication No. CN104852002A Chinese invention patent discloses a kind of baffle plate of lead acid storage battery, including quality hundred
Point than be 85-95% ultra-fine fibre glass, mass percent be 4-10% polyester fiber, mass percent is 1-5% vinegar
Sour fiber.Preparation method is to add polyester fiber and acetate fiber after ultra-fine fibre glass is carried out into mashing 5-10 minutes, then is beaten
Slurry carries out shaping handsheet after 8-12 minutes, at the uniform velocity into drying system, is dried at 160-250 DEG C, winding cutting.
Sea-island fibre is a kind of a kind of material being scattered in polymer in another polymer, is disperseed in fibre section
It is in mutually " island " state, and parent is then equivalent to " sea ", in terms of the cross section of fiber is a kind of composition with fine and scattered state
Surrounded by another composition, there are many island as marine.Its " island " in the axial direction of fiber is continuous, close with " sea " composition
Collection, it is equally distributed.In process of production, it has the fiber number of conventional fibre, but " sea " composition is dissolved away with solvent, then may be used
Obtain collecting the superfine fibre beam of pencil.According to the general classification of fiber, after sea-island fibre separation, filament number only 0.005D, category
Superfine fibre, conventional spinning can not possibly be accomplished, therefore it has the characteristic that general fiber can not possibly have.Sea-island fibre has uniqueness
Performance, with acid resistance is good, crimped resilient is good, the advantages of capillary wick effect is good.
The content of the invention
The present invention is larger for the maximum diameter of hole of AGM dividing plates in the prior art, and pore-size distribution is uneven, and compression rebound
Property difference the problem of there is provided a kind of aperture it is small, inhale the lead accumulator dividing plate that acid amount is high, durable pressure is big, tensile break strength is big.
A kind of lead accumulator dividing plate, the composition of the lead accumulator dividing plate includes glass fibre and COPET sea island filaments, its
In, the COPET sea island filaments are obtained by PA/COPET sea-island fibres after molten sea processing.PA/COPET sea-island fibres refer to marine origin
It is polyamide fibre (PA) to divide, and island component is the sea-island fibre before the molten sea of modified dacron (COPET), and sea component PA therein is dissolved
Afterwards, the superfine fibre beam for obtaining the collection pencil behind molten sea is COPET sea island filaments.
It is preferred that, the specification of the PA/COPET sea-island fibres is:0.6~0.7dtex of line density, 40~80 islands/root.Line
Density is the index for describing fiber thickness degree, the general quality representation with fiber certain length, unit g/km, for fiber
Conventional unit is Tekes (tex), refers to important grams of 1000 meters of long fibers in official regain, tex ten/
One is dtex (dtex);Denier (D) is also the unit of conventional sign fiber linear density, and it represents 9000 meters of long fibre weights
For how many grams, as how many denier.A piece sea-island fibre, sea component is surrounded after the island of tens, molten sea, and sea component is removed,
Internal island one by one spreads out, such as the PA/COPET sea-island fibres of 40 islands/root, then in the sea component of a sea-island fibre
Between have behind the island component of 40, molten sea, this 40 island components scatter, as 40 COPET sea island filaments.
It is preferred that, the mass percentage content of the COPET sea island filaments is 5%~25%.
It is further preferred that the mass percentage content of the COPET sea island filaments is 15%~25%.
It is preferred that, the fineness of the COPET sea island filaments is 0.005-0.01D.
It is further preferred that the fineness of the COPET sea island filaments is 0.008-0.01D.
It is preferred that, the fineness of the glass fibre is 29 °~35 °.The fineness of usual glass fibre is with number of degrees unit come table
Levy, its fibre fineness of 29 ° of glass fibre is 2.083um or so, its fibre fineness of 35 ° of glass fibre is 1.065um or so.
It is preferred that, the preparation method of the COPET sea island filaments is as follows:It is by PA/COPET sea-island fibres immersion mass concentration
In 10%~15% sulfuric acid solution, sea component dissolving is obtained the COPET sea island filaments in 20 minutes by stir process.
It is preferred that, the preparation method of the lead accumulator dividing plate is as follows:By the COPET sea island filaments and glass fibre press than
Example, which is mixed and added water, is configured to slurries, and dividing plate is made in wet moulding, drying.
Present invention also offers the lead accumulator prepared using the lead accumulator dividing plate.
Lead accumulator dividing plate of the present invention with the addition of COPET sea island filaments in the preparation, and the COPET sea island filaments are by PA/COPET
Sea-island fibre is obtained after molten sea processing.After sea-island fibre separation, filament number is thinner, and conventional spinning can not possibly be accomplished, therefore
It has the characteristic that general fiber can not possibly have.The more common AGM dividing plates of lead accumulator dividing plate of the present invention have suction acid amount high, resistance to
The advantages of pressure is big long, tensile break strength is big, with good application prospect.
Brief description of the drawings
Fig. 1 is liquid absorption testing result figure in embodiment 5.
Fig. 2 is durable pressure testing result figure in embodiment 6.
Fig. 3 is tensile break strength testing result figure in embodiment 7.
Embodiment
The PA/COPET sea-island fibres of all size:Purchased from Jiangsu Yizheng Chemical Fibre Co., Ltd.;
Glass fibre:Purchased from Shenyang Dong Xiang glass fibres Co., Ltd.
Embodiment 1
It is the PA/COPET sea-island fibres progress acid treatment that line density is 0.62dtex, 40 islands/root to weigh 15kg specifications, is obtained
To superfine fibre, acid treatment method is that sea-island fibre is put into the H that concentration is 10%2SO4In solution, stir process 20min makes sea
Island fiber fully contacts acid solution, and " sea " (PA) of PA/COPET sea-island fibres is dissolved in acid solution, 8.5kg materials are obtained
For the modified dacron superfine fibre beam (COPET sea island filaments) of COPET collection pencil, its scattered modified dacron sea-island fibre silk
Fineness is 0.01D.
The fineness for weighing above-mentioned preparation is 0.01D COPET sea island filament 4.5kg, glass fibre (wherein 29 ° glass fibres
45% is accounted for, 35 ° of glass fibres account for 55%) 25.5kg, both 30kg (COPET sea island filaments account for 15%) altogether are added in 12 tons of water
Slurries are mixedly configured into, island/fiberglass type non-woven material is manufactured using wet therapy forming process, its drying process temperature is
Dry to dry at 40min, 100 DEG C at 90 DEG C and 40min is dried at 40min, 120 DEG C, total drying time is 2h, finally prepares and goes to sea
Island/fiberglass type lead accumulator dividing plate.The generous of dividing plate is 71.5mm × 0.62mm, and this dividing plate can be used for 20AH battery system
It is standby.
Embodiment 2
It is the PA/COPET sea-island fibres progress acid treatment that line density is 0.69dtex, 50 islands/root to weigh 15kg specifications, is obtained
To superfine fibre, acid treatment method is that sea-island fibre is put into the H that concentration is 15%2SO4In solution, stir process 20min makes sea
Island fiber fully contacts acid solution, and " sea " (PA) of PA/COPET sea-island fibres is dissolved in acid solution, 8.2kg materials are obtained
For the modified dacron superfine fibre beam (COPET sea island filaments) of COPET collection pencil, its scattered modified dacron sea-island fibre silk
Fineness is 0.008D.
The fineness for weighing above-mentioned preparation is 0.008D COPET sea island filament 7.5kg, glass fibre (wherein 29 ° glass fibres
45% is accounted for, 35 ° of glass fibres account for 55%) 22.5kg, both 30kg (COPET sea island filaments account for 25%) altogether are added in 12 tons of water
Slurries are mixedly configured into, island/fiberglass type non-woven material is manufactured using wet therapy forming process, its drying process temperature is
Dry to dry at 40min, 100 DEG C at 90 DEG C and 40min is dried at 40min, 120 DEG C, total drying time is 2h, finally prepares and goes to sea
Island/fiberglass type lead accumulator dividing plate.The generous of dividing plate is 71.5mm × 0.62mm, and this dividing plate can be used for 20AH battery system
It is standby.
Embodiment 3
It is the PA/COPET sea-island fibres progress acid treatment that line density is 0.60dtex, 60 islands/root to weigh 15kg specifications, is obtained
To superfine fibre, acid treatment method is that sea-island fibre is put into the H that concentration is 10%2SO4In solution, stir process 20min makes sea
Island fiber fully contacts acid solution, and " sea " (PA) of PA/COPET sea-island fibres is dissolved in acid solution, 8.7kg materials are obtained
For the modified dacron superfine fibre beam (COPET sea island filaments) of COPET collection pencil, its scattered modified dacron sea-island fibre silk
Fineness is 0.006D.
The fineness for weighing above-mentioned preparation is 0.006D COPET sea island filament 1.5kg, glass fibre (wherein 29 ° glass fibres
45% is accounted for, 35 ° of glass fibres account for 55%) 28.5kg, both 30kg (COPET sea island filaments account for 5%) altogether add in 12 tons of water and mixed
Conjunction is configured to slurries, and island/fiberglass type non-woven material is manufactured using wet therapy forming process, and its drying process temperature is 90
Dry to dry at 40min, 100 DEG C at DEG C and 40min is dried at 40min, 120 DEG C, total drying time is 2h, finally prepares and goes to sea
Island/fiberglass type lead accumulator dividing plate.The generous of dividing plate is 71.5mm × 0.62mm, and this dividing plate can be used for 20AH battery system
It is standby.
Embodiment 4
It is the PA/COPET sea-island fibres progress acid treatment that line density is 0.70dtex, 80 islands/root to weigh 15kg specifications, is obtained
To superfine fibre, acid treatment method is that sea-island fibre is put into the H that concentration is 15%2SO4In solution, stir process 20min makes sea
Island fiber fully contacts acid solution, and " sea " (PA) of PA/COPET sea-island fibres is dissolved in acid solution, 8.6kg materials are obtained
For the modified dacron superfine fibre beam (COPET sea island filaments) of COPET collection pencil, its scattered modified dacron sea-island fibre silk
Fineness is 0.005D.
The fineness for weighing above-mentioned preparation is 0.005D COPET sea island filament 3.0kg, glass fibre (wherein 29 ° glass fibres
45% is accounted for, 35 ° of glass fibres account for 55%) 27.0kg, both 30kg (COPET sea island filaments account for 10%) altogether are added in 12 tons of water
Slurries are mixedly configured into, island/fiberglass type non-woven material is manufactured using wet therapy forming process, its drying process temperature is
Dry to dry at 40min, 100 DEG C at 90 DEG C and 40min is dried at 40min, 120 DEG C, total drying time is 2h, finally prepares and goes to sea
Island/fiberglass type lead accumulator dividing plate.The generous of dividing plate is 71.5mm × 0.62mm, and this dividing plate can be used for 20AH battery system
It is standby.
Comparative example 1
By 30kg100% glass fibre, (wherein 29 ° account for 45%, and 35 ° account for 55%) to add in 12 tons of water is made one
Fixed slurry, manufactures island/fiberglass type non-woven material, its drying process temperature is at 90 DEG C using wet therapy forming process
Dry to dry at 40min, 100 DEG C and 40min is dried at 40min, 120 DEG C, total drying time is 2h, finally prepares glass fibre
Type lead accumulator dividing plate.The generous of dividing plate is 71.5mm × 0.62mm, and this dividing plate can be used for 20AH battery to prepare.
Embodiment 5
The detection that acid amount is inhaled in pressurization is carried out to dividing plate prepared by embodiment 1~4 and comparative example 1.
Dividing plate is cut into 50mm × 50mm 15, square first, more than 1h, Ran Houqu are dried at 80 DEG C ± 2 DEG C
Go out to be placed in drier and be cooled to room temperature.Using 10kPa calibrators measure sample thickness, and be added sample to be tested total thickness
Degree, the gross weight for weighing style to be measured obtains g1;Testing sample is placed in the middle of fixture, fixture is adjusted, its spacing is surveyed in 50kPa
Its thickness (being surveyed with slide measure) is surveyed under thick instrument, and fixture, dividing plate are put into together fill (25 DEG C) density for 1.280g/cm3
In the acid-resistant container of ± 0.005g/cm3 sulfuric acid solution, taken out after 30min, keep pressure drip 5min, take out dividing plate and claim total matter
G2 is measured, then inhales acid amount X=(g2-g1)/g1.Every kind of sample surveys its durable pressure from 5 samples, seeks its average value.
As a result as shown in table 1 and Fig. 1, dividing plate prepared by embodiment 1~4, it is equal compared with dividing plate prepared by comparative example 1 that it inhales acid amount
Tool improves, and increase rate is between 6.9%~10.9%.
Table 1
Embodiment 1 | Embodiment 2 | Embodiment 3 | Embodiment 4 | Comparative example 1 | |
Liquid absorption (unit g/g) | 5.88±0.15 | 6.10±0.18 | 5.95±0.21 | 6.05±0.23 | 5.50±0.19 |
Embodiment 6
The durable pressure test of hygrometric state is carried out to dividing plate prepared by embodiment 1~4 and comparative example 1.
Detection method is as follows:
1) a diameter of 5cm 15 circle AGM dividing plates are cut, neat be put into water is stacked and fully soaks, then take out code
Put neat;
2) actual (real) thickness under original depth and 100kPa pressure of the dividing plate under 0kPa pressure is determined;
3) decrement (decrement=original depth-actual (real) thickness) of dividing plate is calculated;
4) universal testing machine working procedure is set, reaches and 120s is stood after predetermined decrement, then fixture returns to displacement and is
At zero, so moving in circles carries out durability test 200 times;
5) data point when standing 120s is chosen as the durable pressure value in this circulation of dividing plate;
6) every kind of sample surveys its durable pressure from 5 samples, seeks its average value.
As a result as shown in table 2 and Fig. 2, dividing plate prepared by embodiment 1~4, its durable pressure is equal compared with dividing plate prepared by comparative example 1
Tool improves, and increase rate is between 28.1%~59.4%.
Table 2
Embodiment 7
Tensile break strength is carried out to dividing plate prepared by embodiment 1~4 and comparative example 1.
Detection method is as follows:
5 samples (every kind of 5 samples of sample) are cut along splitter plate molding direction first, specimen length is 100mm, a width of
15mm, makes the mark that fixture is 50mm, by specimen holder on the upper and lower fixture of puller system, in test process on sample
Sample should be clamped, it is impossible to slide and damage sample, clamp central line should be coaxial with the center line of sample, with 100mm/min ±
5mm/min speed tensile, load during record sample destruction, its tensile strength δ=P/b, wherein δ is tensile strength, unit
For kN/m, P is the failing load of sample, and unit is N (ox);B is specimen width, and unit is mm.Embodiment 1~4 and comparative example 1
The dividing plate of preparation, it is every kind of to take 5 samples to survey its tensile break strength, and average.
As a result as shown in table 3 and Fig. 3, dividing plate prepared by embodiment 1~4, its tensile break strength is prepared compared with comparative example 1
Dividing plate is respectively provided with certain raising, and increase rate is between 17.9%~25.6%.
Table 3
Claims (10)
1. a kind of lead accumulator dividing plate, it is characterised in that be made up of glass fibre and COPET sea island filaments, wherein, the COPET
Sea island filament is obtained by PA/COPET sea-island fibres after molten sea processing.
2. lead accumulator dividing plate as claimed in claim 1, it is characterised in that the specification of the PA/COPET sea-island fibres is:
0.6~0.7dtex of line density, 40~80 islands/root.
3. lead accumulator dividing plate as claimed in claim 1, it is characterised in that the mass percent of the COPET sea island filaments contains
Measure as 5%~25%.
4. lead accumulator dividing plate as claimed in claim 3, it is characterised in that the mass percent of the COPET sea island filaments contains
Measure as 15%~25%.
5. lead accumulator dividing plate as claimed in claim 1, it is characterised in that the fineness of the COPET sea island filaments is 0.005-
0.01D。
6. lead accumulator dividing plate as claimed in claim 5, it is characterised in that the fineness of the COPET sea island filaments is 0.008-
0.01D。
7. lead accumulator dividing plate as claimed in claim 1, it is characterised in that the fineness of the glass fibre is 29 °~35 °.
8. lead accumulator dividing plate as claimed in claim 1, it is characterised in that the preparation method of the COPET sea island filaments is as follows:
PA/COPET sea-island fibres are immersed into mass concentration in 10%~15% sulfuric acid solution, stir process 20 minutes is by sea component
Dissolving obtains the COPET sea island filaments.
9. lead accumulator dividing plate as claimed in claim 1, it is characterised in that the preparation method of the lead accumulator dividing plate is such as
Under:The COPET sea island filaments are mixed and added water in proportion with glass fibre and are configured to slurries, wet moulding, dry be made every
Plate.
10. the lead accumulator prepared using the lead accumulator dividing plate as described in claim 1~9 is any.
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107403934A (en) * | 2017-08-27 | 2017-11-28 | 山东金科力电源科技有限公司 | A kind of polar plate of lead acid storage battery chopped fiber |
CN109004154A (en) * | 2018-07-23 | 2018-12-14 | 广东蒙泰高新纤维股份有限公司 | A kind of method of wet process copy paper technique manufacture diaphragm of power lithium ion battery |
CN109841786A (en) * | 2019-04-02 | 2019-06-04 | 南京林业大学 | Chemical fibre composite diaphragm and its production method |
CN113279145A (en) * | 2021-05-27 | 2021-08-20 | 天津齐邦新材料有限公司 | Preparation method of degradable superfine mask base cloth |
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CN102522513A (en) * | 2011-12-19 | 2012-06-27 | 中材科技股份有限公司 | Glass fiber battery membrane and preparation method thereof |
CN103088450A (en) * | 2013-02-05 | 2013-05-08 | 济南欣海特种纤维有限公司 | Sea-island fiber preparation process and distributing plate for spinning |
WO2017031159A1 (en) * | 2015-08-17 | 2017-02-23 | Celgard, Llc | Improved battery separators and related methods |
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Publication number | Priority date | Publication date | Assignee | Title |
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CN1356731A (en) * | 2000-08-10 | 2002-07-03 | 日本维林株式会社 | Partition for battery |
CN102522513A (en) * | 2011-12-19 | 2012-06-27 | 中材科技股份有限公司 | Glass fiber battery membrane and preparation method thereof |
CN103088450A (en) * | 2013-02-05 | 2013-05-08 | 济南欣海特种纤维有限公司 | Sea-island fiber preparation process and distributing plate for spinning |
WO2017031159A1 (en) * | 2015-08-17 | 2017-02-23 | Celgard, Llc | Improved battery separators and related methods |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107403934A (en) * | 2017-08-27 | 2017-11-28 | 山东金科力电源科技有限公司 | A kind of polar plate of lead acid storage battery chopped fiber |
CN109004154A (en) * | 2018-07-23 | 2018-12-14 | 广东蒙泰高新纤维股份有限公司 | A kind of method of wet process copy paper technique manufacture diaphragm of power lithium ion battery |
CN109841786A (en) * | 2019-04-02 | 2019-06-04 | 南京林业大学 | Chemical fibre composite diaphragm and its production method |
CN113279145A (en) * | 2021-05-27 | 2021-08-20 | 天津齐邦新材料有限公司 | Preparation method of degradable superfine mask base cloth |
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