KR20030035414A - The Preparation Of Mioropouros Separator - Google Patents
The Preparation Of Mioropouros Separator Download PDFInfo
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- KR20030035414A KR20030035414A KR1020010067493A KR20010067493A KR20030035414A KR 20030035414 A KR20030035414 A KR 20030035414A KR 1020010067493 A KR1020010067493 A KR 1020010067493A KR 20010067493 A KR20010067493 A KR 20010067493A KR 20030035414 A KR20030035414 A KR 20030035414A
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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
- H01M50/449—Separators, membranes or diaphragms characterised by the material having a layered structure
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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
- H01M10/12—Construction or manufacture
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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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- 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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Abstract
Description
본 발명은 미다공성 격리막의 제조방법에 관한 것으로, 보다 상세하게는 납축전지에서 양극, 음극전극판 사이에 삽입하는 열가소성 탄성재료로 이루어진 납축전지용 미다공성 격리막(Separator)의 제조 방법에 관한 것이다.The present invention relates to a method for manufacturing a microporous separator, and more particularly, to a method for producing a lead-acid battery microporous separator (Separator) made of a thermoplastic elastic material inserted between the positive electrode and the negative electrode plate in the lead-acid battery.
격리막의 기본적인 역할은 전극판과 전극판제의 침적물에 의해 전기적인 단락을 방지하는 동시에 전해질에 있는 이온의 흐름을 보장하여 전류가 흐르게 하는데 있다. 납축전지는 여러개의 전극판과 격리막이 교대로 있는 다수의 셀로 구성되어 있다.The basic role of the separator is to prevent electric short circuits by depositing the electrode plate and the electrode plate, and to ensure the flow of ions in the electrolyte to allow current to flow. A lead acid battery is composed of a plurality of cells with alternating electrode plates and separators.
납축전지의 격리막은 물리적 충격에 견딜 수 있는 기계적 강도와 유연성을 지녀야 할뿐만 아니라 기공도가 커서 이온의 흐름이 보장되는 동시에 전극 그리드에서 탈락되는 전극판제의 통과를 막는 균일한 미다공성을 지니고 있어야 한다. 또한 전지 환경에서 일어나는 산화와 열에 대해 내구성을 지니고 있어야 한다. 즉 양극의 이산화납의 산화력과 전해질인 황산의 부식에 견딜 수 있는 내화성을 갖는 동시에 자동차 본네트 내에서 열에 견딜 수 있어야 한다. 또한 낮은 전기적 저항과함께 매우 큰 기공도가 요구되어 진다.The lead-acid battery's membrane must not only have mechanical strength and flexibility to withstand physical shocks, but also have a uniform porosity that prevents the passage of electrode plates that fall out of the electrode grid while ensuring the flow of ions due to its large porosity. . It must also be durable against oxidation and heat that occur in the battery environment. In other words, it should be able to withstand the oxidizing power of the lead dioxide of the anode and the corrosion resistance of sulfuric acid, which is an electrolyte, and at the same time, the heat of the car bonnet. In addition, very high porosity is required with low electrical resistance.
납축전지에 사용되는 격리막은 초기에는 리그린을 추출한 얇은 우드, 미다공성 고무 또는 다양한 다공성의 물질들로 제조되었으나 근래에 들어서는 폴리올레핀과 무기충진제로 이루어진 형태가 많이 사용된다. 이러한 격리막의 제조법은 폴리올레핀과 무기충진제 및 가소제를 균일하게 혼합과 혼련시킨 후 압출공정과 캘린더 공정을 통하여 리브형태의 시이트 형상으로 제조한 다음, 제조된 시이트를 적당한 유기 용제에 넣어 가소제를 추출하고 건조하여 기공을 형성하여 미다공성의 막을 제조한다(미국특허 제3,351,495호, 제 4,024,323호, 제 4,237,08호, 일본국 특허공개 소 51-138755, 소 54-38278 호, 소 54-14371 호 등).The separator used in lead acid batteries was initially made of thin wood extracted from ligrin, microporous rubber, or various porous materials, but in recent years, many forms of polyolefins and inorganic fillers are used. In order to prepare such a separator, polyolefin, inorganic filler and plasticizer are uniformly mixed and kneaded, and then manufactured into a rib-like sheet through an extrusion process and a calender process, and then the prepared sheet is put into a suitable organic solvent to extract a plasticizer and dried. To form pores to produce a microporous membrane (US Pat. Nos. 3,351,495, 4,024,323, 4,237,08, Japanese Patent Publication Nos. 51-138755, 54-38278, 54-14371, etc.). .
상기 발명들에서 나타나는 원료의 함량을 보면 폴리올레핀의 10∼30체적%, 무기충진제가 30∼40체적%, 가소제가 30∼60체적%이다. 첨가제로는 카본블랙, 크래파이트 또는 카본파이버를 각각 또는 혼합하여 첨가하는 것을 특징으로 하고 있다. 이들 첨가물은 500∼1,000 Ω·cm-1정도의 전기전도도를 갖는 것이 적절하며 미량 투입하면 착색제의 역할만 할뿐이고 과량 투입하면 격리막 내부의 기공에 침적되어 전기 도체 역할을 하게 되어 폴리올레핀과 실리카를 합한 양에 대하여 0.5∼10체적%의 범위로 첨가하는 것이 바람직하다.The content of the raw materials shown in the above inventions is 10 to 30% by volume of polyolefin, 30 to 40% by volume of inorganic filler, and 30 to 60% by volume of plasticizer. As an additive, carbon black, graphite, or carbon fiber is added, respectively, or it is characterized by adding. These additives are suitable to have an electrical conductivity of about 500 to 1,000 Ω · cm -1 . If a small amount is added, the additive only serves as a colorant, and when an excessive amount is added, the additives are deposited in pores inside the membrane to serve as an electrical conductor, thus combining polyolefin and silica. It is preferable to add in 0.5-10 volume% with respect to quantity.
격리막의 전기저항이 높을 수록 납축전지의 기전력이 저하되어 효율이 낮아지며 저온에서의 시동력이 감소하게 되어 격리막 제조시 전기저항을 감소시키는 것이 주요한 과제로 되어 왔다. 특히 드라이 형태의 납축전지에서는 전해질이 격리막에 빠른 흡수성을 가져야 한다. 전지저항과 흡수율을 증가시키기 위해서는 무기충진제의 함량을 높여 다공성의 향상을 통해 목적하는 바를 얻을 수 있으나 기계적 강도와 내구성에 악영향을 미치게 된다. 따라서 무기충진함량을 증가시키지 않고 전기저항과 흡수율을 향상시킬 필요성이 있다.The higher the electrical resistance of the separator, the lower the electromotive force of the lead acid battery, the lower the efficiency and the lower the starting force at low temperatures has been a major problem to reduce the electrical resistance in the manufacturing of the separator. Particularly in dry lead acid batteries, the electrolyte should have fast absorption into the separator. In order to increase the battery resistance and absorption rate, the desired content can be obtained by increasing the content of the inorganic filler to improve porosity, but it has an adverse effect on mechanical strength and durability. Therefore, there is a need to improve the electrical resistance and absorption rate without increasing the inorganic filling content.
본 발명은 상기한 바와 같은 문제점을 해결하기 위한 것으로 무기충진제의 함량을 증가시키지 않고 낮은 전기저항과 빠른 흡수성을 갖는 납축전지용 격리막을 제조할 수 있는 방법을 제공하는 것을 목적으로 한다.An object of the present invention is to provide a method for manufacturing a lead-acid battery separator having a low electrical resistance and fast absorption without increasing the content of the inorganic filler to solve the problems as described above.
본 발명은 고밀도 폴리올레핀, 무기충진제 및 가소제로 격리막을 제조함에 있어서 알킬페놀 폴리에틸렌 옥사이드 또는 알킬 폴리에틸렌 옥사이드로부터 선택된 1종이상의 비이온계 계면활성제 및 알킬벤젠 설폰 소다, 소디움 디알킬 설포석시네이트, 알킬나프탈렌설포네이트로부터 선택된 1종 이상의 음이온계 계면활성제가 첨가제로 사용되거나 표면에 코팅되는 것을 특징으로 한다.The present invention provides at least one nonionic surfactant selected from alkylphenol polyethylene oxide or alkyl polyethylene oxide and alkylbenzene sulfone soda, sodium dialkyl sulfosuccinate, alkylnaphthalene in preparing the separator with high density polyolefin, inorganic filler and plasticizer. One or more anionic surfactants selected from sulfonates are used as additives or coated on the surface.
이하, 본 발명을 상세히 설명한다.Hereinafter, the present invention will be described in detail.
본 발명에 사용되는 수지는 분자량이 적어도 60만 이상이며 용융지수가 0.04 이하인 고밀도 폴리에틸렌 또는 폴리에틸렌과 폴리프로필렌과 폴리부틸렌 등으로 구성된 폴리올레핀으로 구성되어 있으며 무기 충진제의 경우에는 카본블랙, 흑연, 미다공성의 유리입자, 실리카와 같이 불활성 물질을 사용 할 수 있으나 그 중 실리카가 가장 효과적이다.The resin used in the present invention is composed of high density polyethylene having a molecular weight of at least 600,000 and a melt index of 0.04 or less, or polyolefin composed of polyethylene, polypropylene, polybutylene, and the like. In the case of inorganic fillers, carbon black, graphite, microporous Inert materials such as glass particles and silica can be used, but silica is the most effective.
무기충진제는 비표면적이 90m2 /g 이상이며 오일 흡수량이 100∼300㎖/100g, 입자크기는 25㎛이하가 좋다. 가소제로는 파라핀계가 30중량%이상 함유되어 있는 석유오일이 효과적이다.Inorganic fillers have a specific surface area of 90 m 2 / g or more, oil absorption of 100 to 300 ml / 100 g, and particle size of 25 μm or less. As a plasticizer, petroleum oil containing 30 wt% or more of paraffinic is effective.
폴리올레핀과 무기충진제 및 가소제를 혼합한 후 압출 및 추출공정을 통해 제조된 시이트를 알킬페놀 폴리에틸렌 옥사이드 또는 알킬 폴리에틸렌 옥사이드로부터 선택된 1종이상의 비이온계 계면활성제 및 알킬벤젠 설폰 소다, 소디움 디알킬 설포석시네이트, 알킬나프탈렌설포네이트로부터 선택된 1종 이상의 음이온계 계면활성제가 0.1∼1.5중량%으로 첨가된 물이나 유기용제에 침적시켜 계면활성제를 표면에 코팅하거나 기공내부에 흡수시킨다.After mixing the polyolefin, inorganic filler and plasticizer, the sheet prepared by extrusion and extraction process may be selected from at least one nonionic surfactant selected from alkylphenol polyethylene oxide or alkyl polyethylene oxide, alkylbenzene sulfone soda and sodium dialkyl sulfoxi One or more anionic surfactants selected from nates and alkylnaphthalenesulfonates are deposited in water or organic solvent added at 0.1 to 1.5% by weight to coat the surfactant on the surface or to absorb it into the pores.
0.1중량% 이하가 되면 계면활성제의 효과를 볼 수가 없으며, 1.5중량% 이상이 되면 흡수시간은 빨라졌으나 거품의 발생으로 인해 전기저항이 증가되므로 계면활성제의 효과가 저하되는 문제점이 있다.If less than 0.1% by weight can not see the effect of the surfactant, 1.5% by weight or more absorption time is faster, but the electrical resistance is increased due to the generation of bubbles there is a problem that the effect of the surfactant is lowered.
또 다른 방법으로는 실리카를 고속교반기에 넣은 후 1,000rpm이상으로 회전시키면서 실리카 중량의 0.5∼10중량%의 계면활성제을 포함한 용액과 혼합시킨 후 폴리올레핀과 가소제를 혼합한 후 압출공정, 추출공정, 건조공정을 통해 격리막을 제조한다.Alternatively, the silica is placed in a high speed stirrer and mixed with a solution containing 0.5 to 10% by weight of a surfactant with silica weight while rotating at 1,000 rpm or more, followed by mixing polyolefin and plasticizer, followed by extrusion, extraction, and drying. The separator is prepared through.
이하 실시의 예에 의하여 상세히 설명하고자 하나 하기 실시예에 의해 본 발명이 한정되는 것은 아니다.To be described in detail by the following examples, the present invention is not limited by the following examples.
하기 실시예에서 제조된 격리막의 전기저항, 흡수율, 흡수속도는 다음과 같은 방법으로 측정하였다.The electrical resistance, water absorption rate, and absorption rate of the separator prepared in the following Examples were measured by the following method.
① 전기저항① electrical resistance
한국공업규격(KS C 2202)에 따라 비중 1.260의 황산수용액 속에서 전류를 1A 흘릴 때 전기저항 차이를 측정하여 하기식과 같이 계산한다.According to the Korean Industrial Standard (KS C 2202), when the current flows 1A in sulfuric acid solution with a specific gravity of 1.260, the electric resistance difference is measured and calculated as follows.
(mΩ·cm2/매) (m / cm 2 / piece)
n : 시편수n: number of specimens
R' : 시편 삽입 후의 전기저항R ': electrical resistance after specimen insertion
R : 시편없이 용액만의 저항R: resistance only solution without specimen
② 흡수율② Absorption rate
증류수를 준비하고(25℃로 유지) 시이트를 10cm×10cm의 크기로 잘라서 무게를 잰 후 증류수 속에 시이트를 담구어 두었다가 1시간후 꺼내어 표면수를 제거한 후 무게를 재어 계산한다.Distilled water was prepared (maintained at 25 ° C.), the sheet was cut to 10 cm × 10 cm in size, weighed, and the sheet was immersed in distilled water. After 1 hour, the surface water was removed, and then weighed.
흡수 후의 무게 - 흡수 전의 무게Weight After Absorption-Weight Before Absorption
--------------------------------- × 100--------------------------------- × 100
흡수전의 무게Weight before absorption
③ 흡수속도③ Absorption rate
비중 1.260의 황산수용액을 0.5㎖를 격리막 표면에 적하시킨 후 표면에 물기가 보이지 않는 순간까지의 시간(분)을 측정한다.After 0.5 ml of sulfuric acid aqueous solution having a specific gravity of 1.260 was added dropwise to the surface of the separator, the time (minutes) until the moisture was not seen on the surface was measured.
<실시예 1-4><Example 1-4>
실리카(Hi-sil SBG 비표면적 170m2/g, 오일흡수량 200㎖/100g)와 카본블랙을 고속 교반기에 넣은 후 2000rpm으로 3분 동안 혼합하였다. 이어서, 실리카의 양을 35체적%로 하고 고밀도폴리에틸렌(XL-1800, 용융지수 0.01이하)은 20체적%, 가소제(Shell412, 끓는점 234℃)는 45체적%로 하여 고속교반기하에서 1,000rpm으로 5분 동안 혼합하여 균일한 조성을 갖게 하였다.Silica (Hi-sil SBG specific surface area 170m 2 / g, oil absorption 200ml / 100g) and carbon black was put into a high speed stirrer and mixed for 3 minutes at 2000rpm. Subsequently, the amount of silica was 35% by volume, 20% by volume of high density polyethylene (XL-1800, melting index of 0.01 or less), and 45% by volume of plasticizer (Shell412, boiling point 234 ° C) at 1,000 rpm under high speed stirring. Mixing for a uniform composition.
혼합된 원료를 압출기에 넣고 압출하여 시이트 형상을 얻었으며(온도 190∼220℃), 이를 다시 60℃온도 하에서 트리클로로에틸렌을 이용하여 가소제를 추출하였다. 가소제를 추출한 시이트를 다시 알킬 폴리에틸렌 옥사이드를 0.1∼1.5중량% 함유한 75℃∼95℃의 증류수에 5분동안 침적시키거나 통과시켜 트리클로로에틸렌을 제거 한 후 건조하여 격리막을 제조하였다.The mixed raw materials were placed in an extruder and extruded to obtain a sheet shape (temperature 190-220 ° C.), which was then extracted with a plasticizer using trichloroethylene under a temperature of 60 ° C. The sheet from which the plasticizer was extracted was again immersed or passed through distilled water at 75 ° C to 95 ° C containing 0.1 to 1.5% by weight of alkyl polyethylene oxide for 5 minutes to remove trichloroethylene and dried to prepare a separator.
얻어진 격리막의 물성은 아래의 표1과 같았다.Physical properties of the obtained separator was shown in Table 1 below.
<비교예 1 ∼ 3><Comparative Examples 1-3>
상기 실시예와 다르게 고밀도 폴리에틸렌의 함량을 변화시키고, 계면활성제를 처리하지 않고 제조한 물성을 측정한 결과를 [표 2]에 수록하였다.Unlike the above example, the content of the high density polyethylene was changed and the physical properties of the prepared polymer without surfactant were measured. [Table 2].
<실시예 5 ∼ 7><Examples 5-7>
상기 실시예3과 동일한 조성과 방법으로 만들면서 계면활성제를 달리 처리하여 제조한 물성을 측정한 결과를 [표 3]에 수록하였다.Table 3 shows the results of measuring physical properties prepared by treating the surfactant differently while making the same composition and method as in Example 3.
A : 알킬벤젠 설폰 소다A: alkylbenzene sulfone soda
B : 소디움 디알킬 설포석시네이트B: sodium dialkyl sulfosuccinate
C : 2.4,7,-테트라 메틸-5-데켄-4,7-디올C: 2.4,7, -tetramethyl-5-deken-4,7-diol
본 발명에 의해 제조된 격리막은 낮은 83 ∼122 mΩ·cm2의 전기저항과 82 ∼115 분의 흡수속도 및 83 ∼ 102중량%의 흡수율을 지닌 우수한 전기적 성질을 가지고 있다. 따라서 격리막의 전기적 물성을 향상시키기 위해 무기물의 함량을 증가시킬 필요가 없기 때문에 우수한 전기적 물성과 더불어 기계적 강도와 내구성을 갖는 격리막을 제조할 수 있다.The separator produced by the present invention has excellent electrical properties with low electrical resistance of 83-122 mPa · cm 2 , absorption rate of 82-115 minutes, and absorption rate of 83-102% by weight. Therefore, since it is not necessary to increase the content of the inorganic material to improve the electrical properties of the separator, it is possible to produce a separator having excellent mechanical properties and durability with excellent electrical properties.
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
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WO2018117515A1 (en) * | 2016-12-21 | 2018-06-28 | 에스케이이노베이션 주식회사 | Composition for preparing secondary battery separator and secondary battery using same |
CN110431688A (en) * | 2017-03-31 | 2019-11-08 | 日本瑞翁株式会社 | Non-aqueous secondary battery perforated membrane adhesive composition, non-aqueous secondary battery perforated membrane paste compound, non-aqueous secondary battery perforated membrane and non-aqueous secondary battery |
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2001
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
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WO2018117515A1 (en) * | 2016-12-21 | 2018-06-28 | 에스케이이노베이션 주식회사 | Composition for preparing secondary battery separator and secondary battery using same |
US11462802B2 (en) | 2016-12-21 | 2022-10-04 | Sk Innovation Co., Ltd. | Composition for manufacturing secondary battery separator and secondary battery including the same |
CN110431688A (en) * | 2017-03-31 | 2019-11-08 | 日本瑞翁株式会社 | Non-aqueous secondary battery perforated membrane adhesive composition, non-aqueous secondary battery perforated membrane paste compound, non-aqueous secondary battery perforated membrane and non-aqueous secondary battery |
CN110431688B (en) * | 2017-03-31 | 2022-04-19 | 日本瑞翁株式会社 | Binder composition, slurry composition, porous film, and nonaqueous secondary battery |
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