KR102724366B1 - Manufacturing method of separator for storage battery - Google Patents
Manufacturing method of separator for storage battery Download PDFInfo
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- KR102724366B1 KR102724366B1 KR1020240058882A KR20240058882A KR102724366B1 KR 102724366 B1 KR102724366 B1 KR 102724366B1 KR 1020240058882 A KR1020240058882 A KR 1020240058882A KR 20240058882 A KR20240058882 A KR 20240058882A KR 102724366 B1 KR102724366 B1 KR 102724366B1
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- fiber yarn
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- wetland
- separator
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- 238000004519 manufacturing process Methods 0.000 title claims description 24
- 238000003860 storage Methods 0.000 title description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 22
- 239000003365 glass fiber Substances 0.000 claims abstract description 20
- 239000012209 synthetic fiber Substances 0.000 claims abstract description 18
- 229920002994 synthetic fiber Polymers 0.000 claims abstract description 18
- 239000008213 purified water Substances 0.000 claims abstract description 16
- 238000001035 drying Methods 0.000 claims abstract description 9
- 239000004848 polyfunctional curative Substances 0.000 claims abstract description 9
- 239000000835 fiber Substances 0.000 claims description 38
- 238000000034 method Methods 0.000 claims description 16
- 239000003795 chemical substances by application Substances 0.000 claims description 12
- -1 polyethylene Polymers 0.000 claims description 9
- 229920006186 water-soluble synthetic resin Polymers 0.000 claims description 9
- 239000000725 suspension Substances 0.000 claims description 8
- 239000012866 water-soluble synthetic resin Substances 0.000 claims description 8
- VGGLHLAESQEWCR-UHFFFAOYSA-N N-(hydroxymethyl)urea Chemical compound NC(=O)NCO VGGLHLAESQEWCR-UHFFFAOYSA-N 0.000 claims description 7
- 238000003825 pressing Methods 0.000 claims description 6
- 238000010521 absorption reaction Methods 0.000 claims description 5
- 239000002518 antifoaming agent Substances 0.000 claims description 5
- 239000000839 emulsion Substances 0.000 claims description 5
- 239000004698 Polyethylene Substances 0.000 claims description 4
- 239000004743 Polypropylene Substances 0.000 claims description 4
- 229920000573 polyethylene Polymers 0.000 claims description 4
- 229920001155 polypropylene Polymers 0.000 claims description 4
- 229920000728 polyester Polymers 0.000 claims description 3
- 238000005507 spraying Methods 0.000 claims description 3
- 238000005303 weighing Methods 0.000 claims description 3
- 239000002253 acid Substances 0.000 abstract description 13
- 239000000463 material Substances 0.000 description 8
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 6
- 230000002745 absorbent Effects 0.000 description 6
- 239000002250 absorbent Substances 0.000 description 6
- 239000003792 electrolyte Substances 0.000 description 6
- 239000011521 glass Substances 0.000 description 5
- 229920005989 resin Polymers 0.000 description 4
- 239000011347 resin Substances 0.000 description 4
- 229920001807 Urea-formaldehyde Polymers 0.000 description 3
- 238000007599 discharging Methods 0.000 description 3
- 150000002500 ions Chemical class 0.000 description 3
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 description 2
- 239000005062 Polybutadiene Substances 0.000 description 2
- 239000004372 Polyvinyl alcohol Substances 0.000 description 2
- 239000011149 active material Substances 0.000 description 2
- 239000000853 adhesive Substances 0.000 description 2
- 230000001070 adhesive effect Effects 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- YADSGOSSYOOKMP-UHFFFAOYSA-N dioxolead Chemical compound O=[Pb]=O YADSGOSSYOOKMP-UHFFFAOYSA-N 0.000 description 2
- 229910001416 lithium ion Inorganic materials 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 229920002857 polybutadiene Polymers 0.000 description 2
- 229920002689 polyvinyl acetate Polymers 0.000 description 2
- 239000011118 polyvinyl acetate Substances 0.000 description 2
- 229920002451 polyvinyl alcohol Polymers 0.000 description 2
- 239000000376 reactant Substances 0.000 description 2
- 230000003014 reinforcing effect Effects 0.000 description 2
- 229920003002 synthetic resin Polymers 0.000 description 2
- 239000000057 synthetic resin Substances 0.000 description 2
- 238000010998 test method Methods 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 229910002640 NiOOH Inorganic materials 0.000 description 1
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000010425 asbestos Substances 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000004202 carbamide Substances 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000004020 conductor Substances 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000010494 dissociation reaction Methods 0.000 description 1
- 230000005593 dissociations Effects 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- 238000003487 electrochemical reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000004088 foaming agent Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 229910000464 lead oxide Inorganic materials 0.000 description 1
- FUJCRWPEOMXPAD-UHFFFAOYSA-N lithium oxide Chemical compound [Li+].[Li+].[O-2] FUJCRWPEOMXPAD-UHFFFAOYSA-N 0.000 description 1
- 229910001947 lithium oxide Inorganic materials 0.000 description 1
- 239000006210 lotion Substances 0.000 description 1
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- BFDHFSHZJLFAMC-UHFFFAOYSA-L nickel(ii) hydroxide Chemical compound [OH-].[OH-].[Ni+2] BFDHFSHZJLFAMC-UHFFFAOYSA-L 0.000 description 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 1
- YEXPOXQUZXUXJW-UHFFFAOYSA-N oxolead Chemical compound [Pb]=O YEXPOXQUZXUXJW-UHFFFAOYSA-N 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920000139 polyethylene terephthalate Polymers 0.000 description 1
- 239000005020 polyethylene terephthalate Substances 0.000 description 1
- 229910052895 riebeckite Inorganic materials 0.000 description 1
- 239000005060 rubber Substances 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 229920002545 silicone oil Polymers 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
Classifications
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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
- H01M50/403—Manufacturing processes of separators, membranes or diaphragms
-
- 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
-
- 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
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M2220/00—Batteries for particular applications
- H01M2220/20—Batteries in motive systems, e.g. vehicle, ship, plane
-
- 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
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Cell Separators (AREA)
Abstract
본 발명은 유리섬유사와 합성섬유사를 정제수와 함께 해리하여 제작된 습지에 경화제를 도포하고 이를 오븐에서 건조하여 프레스로 압착하여 정해진 두께로 제작됨으로써, 내산성과 인장강도 및 낮은 전기저항을 갖는 효과가 있다.The present invention is produced by dissociating glass fiber yarn and synthetic fiber yarn with purified water, applying a hardener to a wetland, drying it in an oven, and compressing it with a press to produce a wetland of a predetermined thickness, thereby achieving the effects of acid resistance, tensile strength, and low electrical resistance.
Description
본 발명은 축전지용 격리막 제조방법에 관한 것으로서, 보다 상세하게는 유리섬유사와 합성섬유사를 정제수와 함께 해리하여 제작된 습지에 경화제를 도포하고 이를 오븐에서 건조하여 프레스로 압착하여 정해진 두께로 제작됨으로써, 내산성과 인장강도 및 낮은 전기저항을 갖는 축전지용 격리막 제조방법에 관한 것이다. The present invention relates to a method for manufacturing a separator for a storage battery, and more specifically, to a method for manufacturing a separator for a storage battery having acid resistance, tensile strength, and low electrical resistance, by dissociating glass fiber yarn and synthetic fiber yarn with purified water, applying a hardener to a wet material, drying the wet material in an oven, and compressing the wet material with a press to produce a predetermined thickness.
일반적으로 축전지는 양극과 음극에 사용되는 물질에 따라 납축전지, 알칼리 축전지 및 리튬이온전지 등으로 구분된다. 납축전지는 가장 오래된 축전지 중 하나로 양극에 산화납을 사용하고 음극에 납이 사용되며, 알칼리 축전지는 음극에 수산화니켈(NiOOH)을 사용한다. 그리고, 리튬이온전지는 양극에 리튬산화물이 사용되고, 음극은 구리와 활물질, 도전재 및 바인더로 구성된다. In general, batteries are classified into lead-acid batteries, alkaline batteries, and lithium-ion batteries, depending on the materials used in the positive and negative electrodes. Lead-acid batteries are one of the oldest batteries and use lead oxide for the positive electrode and lead for the negative electrode, while alkaline batteries use nickel hydroxide (NiOOH) for the negative electrode. In addition, lithium-ion batteries use lithium oxide for the positive electrode, and the negative electrode is composed of copper, active materials, conductive materials, and binders.
이러한 축전지는 이온만 이동시키는 매개인 전해액과, 양극과 음극을 전기적으로 절연시키고 자가방전을 방지하는 분리막이 더 구비되게 된다. 즉, 축전지의 4대 구성요소는 양극, 음극, 전해질 및 분리막으로 이루어진다.These batteries are further equipped with an electrolyte, which is a medium that only moves ions, and a separator that electrically insulates the positive and negative electrodes and prevents self-discharge. In other words, the four major components of a battery are a positive electrode, a negative electrode, an electrolyte, and a separator.
한편, 한국산업표준(KS C 2202)에는 납축전지용 격리판에 대한 규정이 개시되었다. KS C 2202는 자동차, 설치, 전기차용 등의 납축전지 극판 사이의 단락 방지와 간격을 유지할 목적으로 삽입하는 다공 또는 미공성 박판에 대한 규정이다. Meanwhile, the Korean Industrial Standard (KS C 2202) has disclosed regulations on separators for lead-acid batteries. KS C 2202 is a regulation on porous or microporous thin plates inserted to prevent short circuits and maintain gaps between lead-acid battery plates for automobiles, installations, electric vehicles, etc.
여기서, 활물질(active material)은 전극의 전기화학 반응물질로서, 양극은 이산화납, 음극은 스펀지모양 납을 의미하며, 전해질(electrolyte)은 납축전지 내의 전기화학반응시에 이온을 전도시키는 매체로서 납축전지용으로는 묽은 황산을 의미하고, 전기 저항은 묽은 황산 중에서 이온 전도가 격리판에 의해 저해되는 정도를 표시하는 값으로 격리팍 100cm2 ㆍ1 매당의 값이며, 유리염소(free chlorine)는 묽은 황산 중에서 격리판으로부터 용출되는 염화물 이온으로 정의된다.Here, the active material is the electrochemical reactant of the electrode, the anode means lead dioxide, and the cathode means sponge-shaped lead. The electrolyte is a medium that conducts ions during the electrochemical reaction within a lead-acid battery, and for lead-acid batteries it means diluted sulfuric acid. The electrical resistance is a value that indicates the degree to which ion conduction is hindered by the separator in diluted sulfuric acid, and is the value per 100 cm2 of separator, and free chlorine is defined as chloride ion eluted from the separator in diluted sulfuric acid.
그리고, 격리판의 종류로는 미공성 고무격리판, 강화섬유격리판, 합성섬유 격리판, 합성수지 격리판, 흡습성 글라스 매트(AGM, Absorbent Glass Mat Tech) 격리판으로 구분되며, 격리판은 충전과 방전에 따라 전극판과 전해액 사이에 화학 반응과정에서 전극판이 변형되어 상호 접촉되거나 또는 전극판 사이에 내부 방전이 일어나는 것을 방지하기 위해 사용된다. And, the types of separators are classified into microporous rubber separators, reinforced fiber separators, synthetic fiber separators, synthetic resin separators, and absorbent glass mat (AGM, Absorbent Glass Mat Tech) separators, and the separator is used to prevent the electrode plates from being deformed and coming into contact with each other during the chemical reaction between the electrode plates and the electrolyte during charging and discharging, or to prevent internal discharge between the electrode plates.
이와 관련된 종래기술로 등록특허공보 제10-0858720호(2008.09.09.)에는 '축전지용 격리판의 제조방법'이 개시되었다.As a related prior art, Patent Publication No. 10-0858720 (September 9, 2008) discloses a ‘method for manufacturing a separator for a battery.’
상기 종래기술은 축전지용 격리판을 제조방법으로서, 메틸올요소 20~30중량%, 수용성 합성수지 20~30중량% 및 물 40~60중량%로 조성된 수성에멀젼이 투입된 고해기에 린터펄프 40~45중량%, 합성섬유사 20~25중량% 및 유리섬유사 30~40중량%를 혼합하여서 된 혼합물을 섬유농도가 5~8중량%가 되도록 투입하고 섬유를 해리하여 얻은 지료를 압착 건조시켜 제조하는 것을 특징으로 한다. The above-mentioned prior art is a method for manufacturing a separator for a storage battery, characterized in that the method comprises: introducing an aqueous emulsion composed of 20 to 30 wt% of methylol urea, 20 to 30 wt% of a water-soluble synthetic resin, and 40 to 60 wt% of water into a beater, mixing 40 to 45 wt% of linter pulp, 20 to 25 wt% of synthetic fiber yarn, and 30 to 40 wt% of glass fiber yarn, so that the mixture has a fiber concentration of 5 to 8 wt%, and dissociating the fibers to produce a stock obtained by pressing and drying the stock.
상기한 종래기술은 석면을 사용하지 않고도 전기저항이 거의 없으며 내충격성과 내산성이 우수하며, 별도의 경화제 처리공정이 없이 생산하는 제조방법으로 생산공정이 단축되고 합성수지 수용액을 사용하므로서 건조시간을 단축시켜줄 수 있는 특징이 있다. The above-mentioned conventional technology has the characteristics of having almost no electrical resistance and excellent impact resistance and acid resistance without using asbestos, a manufacturing method that shortens the production process by producing without a separate hardening agent treatment process, and shortening the drying time by using a synthetic resin aqueous solution.
다만, 상기한 종래기술은 합성섬유사 재질의 격리판이며, AGM 격리판인 유리섬유사의 격리판은 제공하지 못하는 문제점이 있었다. However, the above-mentioned prior art has a problem in that it is a separator made of synthetic fiber material and cannot provide a separator made of glass fiber, which is an AGM separator.
본 발명은 상기와 같은 종래 기술의 문제점을 해결하기 위해 창작된 것으로 본 발명의 목적은 흡습성 글라스 매트(AGM, Absorbent Glass Mat Tech) 격리판의 주재료인 유리섬유사와 유리섬유사의 인장강도를 강화시키기 위한 합성섬유사를 정제수에 해리하여 습지를 만들고, 습지에서 수분을 제거하고 건조시켜 이를 정해진 두께로 압착하여 제조됨으로써, 유리섬유의 특성상 온도 변화에 덜 민감하고 메쉬구조로 형성되어 전해액이 함습되어 일반 배터리보다 빠른 충전이 가능한 배터리에 적용되는 축전지용 격리판 제조방법을 제공함에 있다.The present invention has been created to solve the problems of the prior art as described above, and an object of the present invention is to provide a method for manufacturing a separator for a storage battery, which is applied to a battery which is less sensitive to temperature changes due to the characteristics of glass fibers and which is formed into a mesh structure so that an electrolyte is impregnated therein and can be charged faster than a general battery, by dissociating glass fibers, which are the main materials of an absorbent glass mat (AGM) separator, and synthetic fibers for reinforcing the tensile strength of the glass fibers, in purified water to create a wetland, removing moisture from the wetland, drying it, and pressing it to a predetermined thickness.
상기한 목적을 달성하기 위한 본 발명에 의한 축전지용 격리판 제조방법은 축전지용 격리판 제조방법으로서, (A)유리섬유사 95중량%와, 합성섬유사 5중량%가 혼합된 6.028g의 제1섬유사와 상기 제1섬유사에 대한 0.05중량부를 추가로 계근한 제2섬유사로 이루어진 섬유사와, 정제수 2000ml를 준비하는 단계와; (B)상기 섬유사와 정제수를 섬유해리기에 투입하여 3분간 해리시키는 단계와; (C)상기 섬유해리기에서 해리된 현탁액을 80 WIRE MESH가 깔린 시트제작기에 투입하는 단계와; (D)상기 시트제작기에 투입된 현탁액에서 발생된 거품을 제거하기 위해 소포제를 투입하는 단계와; (E)상기 거품이 제거된 80MESH 습지를 수분흡수장치에 올려 60%수분을 제거하는 단계와; (F)상기 수분흡수장치에서 60%수분이 제거된 습지의 배면에 정제수에 정제수 대비 0.005중량부로 희석된 경화제를 스프레이 방식으로 분사시키는 단계와; (G)상기 경화제가 분사된 습지를 110℃ 온도의 오븐에 30분간 건조시키는 단계; 및 (H)상기 30분간 건조된 습지가 0.7t 두께로 성형되도록 프레스로 가압하는 단계;로 이루어지고,In order to achieve the above-mentioned object, the present invention provides a method for manufacturing a battery separator, comprising the steps of: (A) preparing fiber yarns comprising 6.028 g of first fiber yarns in which 95 wt% of glass fiber yarn and 5 wt% of synthetic fiber yarn are mixed, and second fiber yarns additionally weighing 0.05 wt% based on the first fiber yarn, and 2,000 ml of purified water; (B) introducing the fiber yarn and purified water into a fiber dissociator and dissociating them for 3 minutes; (C) introducing the suspension dissociated in the fiber dissociator into a sheet manufacturing machine having 80 WIRE MESH; (D) introducing an antifoaming agent to remove bubbles generated in the suspension introduced into the sheet manufacturing machine; (E) placing the 80MESH wetland from which the bubbles have been removed into a moisture absorption device and removing 60% of the moisture; (F) a step of spraying a curing agent diluted in purified water at 0.005 weight part per purified water onto the back surface of a wetland from which 60% of moisture has been removed in the above moisture absorption device; (G) a step of drying the wetland on which the curing agent has been sprayed in an oven at a temperature of 110°C for 30 minutes; and (H) a step of pressing the wetland dried for 30 minutes so that it is molded to a thickness of 0.7 t.
상기 경화제는 상기 섬유사 대비 0.01중량부가 분사되는 것을 특징으로 한다. The above hardener is characterized in that 0.01 weight part is sprayed relative to the fiber.
상기 제2섬유사는 0.200g 내지 0.302g 사이에서 정해지고, 상기 합성섬유사는 폴리에틸렌사, 폴리푸로필렌사, 폴리에스텔사 중 어느 하나로 구비된 것을 특징으로 한다. The above second fiber yarn is determined between 0.200 g and 0.302 g, and the above synthetic fiber yarn is characterized by being provided with any one of polyethylene yarn, polypropylene yarn, and polyester yarn.
상기 경화제는 메틸올요소 20~30중량%, 수용성 합성수지 20~30중량% 및 물 40~60중량%로 조성된 수성에멀젼으로 구비된 것을 특징으로 한다. The above curing agent is characterized in that it is provided as an aqueous emulsion composed of 20 to 30 wt% of methylol urea, 20 to 30 wt% of a water-soluble synthetic resin, and 40 to 60 wt% of water.
상기 (H)단계는 상기 프레스의 가압시 20kgf/cm2 로 가압하는 것을 특징으로 한다. The above step (H) is characterized by applying pressure of 20 kgf/cm2 when pressurizing the press.
상기 (G)단계에서 건조된 상기 습지의 수분율은 0.3% 미만인 것을 특징으로 한다. The moisture content of the wetland dried in the above step (G) is characterized as being less than 0.3%.
이와 같이 본 발명에 의한 축전지용 격리판 제조방법은 유리 섬유사를 합성섬유사와 혼합 해리하여 메쉬구조로 성형함으로써, 전해질의 흡습이 용이할 뿐 아니라 전기저항이 매우 낮고, 고밀도의 유리섬유사로 가공됨으로써 인장강도 및 내산성이 우수하여, 충방전이 잦은 자동차 배터리에 적용될 경우 배터리의 출력이 우수해지며, 시동파워가 향상되어 에너지 효율이 증대되는 효과가 있다. In this way, the method for manufacturing a separator for a storage battery according to the present invention mixes glass fiber yarn with synthetic fiber yarn and forms it into a mesh structure, so that not only is the electrolyte easily absorbed, but the electrical resistance is very low, and since it is processed into high-density glass fiber yarn, the tensile strength and acid resistance are excellent, so when applied to an automobile battery that is frequently charged and discharged, the battery output is excellent, and the starting power is improved, thereby increasing energy efficiency.
이하, 본 발명의 일 실시예를 상세히 설명하면 다음과 같다.Hereinafter, one embodiment of the present invention will be described in detail.
본 발명의 축전지용 격리판 제조방법은 유리섬유사를 주재료로 하여 제조된 흡습성 글라스 매트(AGM, Absorbent Glass Mat Tech) 격리판의 제조방법에 관한 것이다. The method for manufacturing a separator for a battery of the present invention relates to a method for manufacturing an absorbent glass mat (AGM, Absorbent Glass Mat Tech) separator manufactured using glass fiber as a main material.
본 발명의 축전지용 격리판 제조방법은, (A)유리섬유사 95중량%와, 합성섬유사 5중량%가 혼합된 6.028g의 제1섬유사와 상기 제1섬유사에 대한 0.05중량부를 추가로 계근한 제2섬유사로 이루어진 섬유사와, 정제수 2000ml를 준비하는 단계;에서 습지 지료를 준비하게 된다. 여기서, 상기 제2섬유사는 0.302g으로 계근되어, 상기 섬유사는 6.330g으로 계근된다. The method for manufacturing a separator for a battery of the present invention comprises the steps of (A) preparing a fiber yarn comprising 6.028 g of a first fiber yarn mixed with 95 wt% of glass fiber yarn and 5 wt% of synthetic fiber yarn and a second fiber yarn additionally weighing 0.05 wt% of the first fiber yarn, and 2000 ml of purified water; thereby preparing wetland material. Here, the second fiber yarn is weighed at 0.302 g, and the fiber yarn is weighed at 6.330 g.
그리고, (B)단계에서 상기 섬유사와 정제수를 섬유해리기에 투입하여 3분간 해리시키게 된다. 이때, 상기 섬유해리기는 3000rpm 파일롯머신으로 섬유사의 해리상태를 외부에서 육안으로 확인할 수 있도록 구비되는 것이 바람직하다. And, in step (B), the fiber and purified water are put into a fiber dissociator and dissociated for 3 minutes. At this time, it is preferable that the fiber dissociator be equipped with a 3000 rpm pilot machine so that the dissociation state of the fiber can be visually confirmed from the outside.
또한, (C)단계에서는 상기 섬유해리기에서 해리된 현탁액을 80 WIRE MESH가 깔린 시트제작기에 투입하게 된다. In addition, in step (C), the suspension dissociated from the fiber dissociator is fed into a sheet manufacturing machine with 80 WIRE MESH laid out.
이때, 상기 시트제작기의 현탁액에서는 거품이 발생되게 되는 데 이를 제거하기 위해서 (D)단계를 수행하게 된다. 즉, (D)단계는 상기 시트제작기에 투입된 현탁액에서 발생된 거품을 제거하기 위해 소포제를 투입하게 된다. At this time, bubbles are generated in the suspension of the sheet making machine, and step (D) is performed to remove them. That is, step (D) involves adding an antifoaming agent to remove the bubbles generated in the suspension fed into the sheet making machine.
여기서, 상기 소포제(Defoamer)는 내알칼리성 및 고온 내성이 강한 올레핀 용매와 친유성 계면 활성제로 구성되거나, 실리콘 오일과 칼슘으로 구성된 로션 소포제로 구성될 수 있다. Here, the defoaming agent may be composed of an olefin solvent with strong alkaline and high temperature resistance and a lipophilic surfactant, or may be composed of a lotion defoaming agent composed of silicone oil and calcium.
한편, 상기 시트제작기에서 소포제를 투입하면 현탁액에서 거품이 제거된 상태를 습지라 칭한다. 그리고, 상기 거품이 제거된 80MESH 습지를 수분흡수장치에 올려 60%수분을 제거하는 (E)단계를 수행한다. Meanwhile, when the foaming agent is injected into the sheet-making machine, the state in which the bubbles are removed from the suspension is called wetland. Then, the 80MESH wetland from which the bubbles are removed is placed on a moisture absorption device to perform step (E) of removing 60% of the moisture.
그리고, (F)단계는 60% 수분이 제거된 습지의 배면에 정제수에 0.005중량부로 희석된 경화제를 스프레이 방식으로 분사시키게 된다. And, in step (F), a hardener diluted in purified water at 0.005 weight part is sprayed onto the back surface of the wetland from which 60% of the moisture has been removed.
또한, (F)단계에서 경화제가 도포된 습지를 110℃ 온도의 오븐에 30분간 건조시키는 (G)단계를 수행하게 된다. 그리고, 프레스로 가압하는 (H)단계를 수행하게 된다. 상기 (H)단계는 상기 건조된 습지가 0.7t(0.7mm) 두께로 성형되도록 프레스로 가압하게 되며, 이때 오차범위는 ±0.05t(0.05mm)를 허용한다. 여기서 상기 건조된 습지는 가압되지 않은 상태로 두께가 0.7t 이상으로 형성된 가압 전의 격리판이다.In addition, in step (F), step (G) is performed to dry the wetland to which the hardener has been applied in an oven at a temperature of 110℃ for 30 minutes. Then, step (H) of pressurizing is performed. In step (H), pressurizing is performed so that the dried wetland is formed to a thickness of 0.7 t (0.7 mm), and the error range at this time is allowed to be ±0.05 t (0.05 mm). Here, the dried wetland is a pre-pressurized separator formed to a thickness of 0.7 t or more in an unpressurized state.
한편, 상기 경화제(curing agent)는 상기 섬유사 대비 0.01중량부가 분사되는 것은, 40%수분이 포함된 습지에 경화제가 도포되고, 오븐에서 건조된 습지의 외면을 형성하여 인장강도를 강화시키게 된다. Meanwhile, the curing agent is sprayed in an amount of 0.01 weight part relative to the fiber, so that the curing agent is applied to the wetland containing 40% moisture and the outer surface of the wetland is dried in an oven, thereby reinforcing the tensile strength.
그리고, (H)단계 이후에 완성된 격리판의 외형, 내산성, 인장강도, 두께 , 전기저항 등을 한국산업표준의 시험방법에 따른 검사가 수행될 수 있다. And, after step (H), the appearance, acid resistance, tensile strength, thickness, electrical resistance, etc. of the completed separator can be inspected according to the test method of the Korean Industrial Standards.
한편, 상기 제2섬유사는 0.200g 내지 0.302g 사이에서 정해짐으로써, 80 WIRE MESH에서 유실되는 섬유사를 보충할 수 있게 된다. 그리고, 상기 합성섬유사는 폴리에틸렌사, 폴리푸로필렌사, 폴리에스텔사 중 어느 하나로 구비되며, 한편, 린터펄프는 고객의 요구에 따라 사용될 수 있으나 건조시간이 더 많이 걸린다는 단점이 있다. 이와 같은 합성섬유사는 유리섬유사를 고정시키는 접착제 역할을 수행한다. Meanwhile, the second fiber yarn is determined between 0.200 g and 0.302 g, thereby making it possible to supplement the fiber yarn lost in 80 WIRE MESH. In addition, the synthetic fiber yarn is provided as one of polyethylene yarn, polypropylene yarn, and polyester yarn, and while linter pulp can be used according to customer requirements, it has the disadvantage of taking a longer drying time. Such synthetic fiber yarn acts as an adhesive to fix the glass fiber yarn.
그리고, 상기 경화제는 메틸올요소 20~30중량%, 수용성 합성수지 20~30중량% 및 물 40~60중량%로 조성된 수성에멀젼으로 이루어진다. 상기 메틸올요소와 같은 요소수지는 내충격성이 약한 단점을 상기 수용성 합성수지로 보강하게 된다. 그리고, 상기 경화제는 방전과 충전을 반복시키는 반응과정에서 격리판을 구성하는 유리섬유사가 변형되는 것을 막아주기 위한 것이다.And, the curing agent is composed of an aqueous emulsion composed of 20 to 30 wt% of methylol urea, 20 to 30 wt% of a water-soluble synthetic resin, and 40 to 60 wt% of water. The urea resin such as the methylol urea has a weak impact resistance, but this is reinforced by the water-soluble synthetic resin. And, the curing agent prevents the glass fiber yarn constituting the separator from being deformed during the reaction process of repeating discharge and charge.
아울러, 상기 (H)단계는 상기 프레스의 가압시 20kgf/cm2 로 가압하게 된다. 상기 (G)단계에서 상기 습지의 수분율은 0.3% 미만으로 건조되게 된다. In addition, in the above step (H), the press is pressurized at 20 kgf/cm 2. In the above step (G), the moisture content of the wetland is dried to less than 0.3%.
상기와 같은 구성으로 이루어진 본 발명에 따른 축전지용 격리판 제조방법의 작용을 살펴보면 아래와 같다.The operation of the method for manufacturing a separator for a battery according to the present invention having the above-described configuration is as follows.
본 발명에 따른 축전지용 격리판은, 다음과 같은 한국산업표준(KS C 2202:2019)에 규정된 흡습성 글라스 매트(AGM, Absorbent Glass Mat Tech)격리판을 만족한다. 아래 한국산업표준의 AGM 격리판 규정(표1)에 따르면 The battery separator according to the present invention satisfies the hygroscopic glass mat (AGM, Absorbent Glass Mat Tech) separator specified in the following Korean Industrial Standard (KS C 2202:2019). According to the AGM separator specification (Table 1) of the Korean Industrial Standard below:
인장강도 0.21MPa, 전기저항 0.004, AGM 흡습성글라스매트 90%이며, KS C 2202:2019 에 규정된 시험방법에 의해 실측한 본원발명은 상기 규정을 만족한다. The tensile strength is 0.21 MPa, the electrical resistance is 0.004, and the AGM hygroscopic glass mat is 90%. The present invention, which was measured by the test method specified in KS C 2202:2019, satisfies the above provisions.
본 발명에 따른 격리판은 유리섬유사 95중량%와 합성섬유사 5중량%가 혼합된 섬유사를 정제수 2ℓ에 해리되도록 섬유해리기에 투입하게 된다. 여기서, 유리섬유사는 내산성을 향상시키고, 합성섬유사는 유리섬유사의 인장강도를 높이기 위해 사용되는 접착제 역할을 수행하게 된다. The separator according to the present invention is made by introducing a fiber mixed with 95 wt% of glass fiber and 5 wt% of synthetic fiber into a fiber dissociator so that the fiber is dissociated in 2 liters of purified water. Here, the glass fiber improves acid resistance, and the synthetic fiber acts as an adhesive to increase the tensile strength of the glass fiber.
이때, 상기 합성섬유사로서 폴리푸로필렌(polypropylene)사, 폴리에틸렌(polyethylene)사, 폴리에스텔(polyethylene terephthalate)사 중 어느 하나로 구성된다. At this time, the synthetic fiber is composed of one of polypropylene yarn, polyethylene yarn, and polyethylene terephthalate yarn.
그리고, 본 발명에서 사용된 경화제는 축전지를 장시간 사용하거나 잦은 충방전에도 격리판 공극의 변형을 방지하여 낮은 전기저항와 유리섬유사의 물성을 유지시킬 수 있게 된다. 상기 경화제는 수성에멀젼으로서, 메틸올요소 20∼30중량%, 수용성 합성수지 20∼30중량%, 물 40∼60중량%를 균일하게 혼합하여 얻게 된다. In addition, the curing agent used in the present invention prevents deformation of the separator gap even when the battery is used for a long time or when frequent charging and discharging are performed, thereby maintaining low electrical resistance and the properties of the glass fiber. The curing agent is an aqueous emulsion obtained by uniformly mixing 20 to 30 wt% of methylol urea, 20 to 30 wt% of a water-soluble synthetic resin, and 40 to 60 wt% of water.
상기 메틸올요소는 요소수지와 유사한 물리적 성질을 나타내지만 수용성이며, 요소(urea)와 포름알데히드(formaldehyde)의 초기 반응물이며, 요소수지와 유사한 경화제로서의 역할을 하게 된다.The above methylol urea exhibits physical properties similar to those of urea resin, but is water-soluble, is an initial reactant of urea and formaldehyde, and acts as a curing agent similar to urea resin.
상기 수용성 합성수지로서는 폴리비닐알콜, 수용성 초산비닐수지, 수용성 폴리부타디엔수지를 사용할 수도 있다. 폴리비닐알콜은 수용성 합성수지이고 초산비닐수지나 폴리부타디엔수지는 수용성 합성수지가 아니지만 이를 알카리로 검화시켜주면 용이하게 수용성으로 전환 시켜줄 수 있다.As the above water-soluble synthetic resin, polyvinyl alcohol, water-soluble polyvinyl acetate resin, and water-soluble polybutadiene resin can be used. Polyvinyl alcohol is a water-soluble synthetic resin, and polyvinyl acetate resin and polybutadiene resin are not water-soluble synthetic resins, but they can be easily converted to water solubility by saponifying them with alkali.
본 발명의 축전지용 격리판 제조방법은, 유리섬유사와 합성섬유사를 정제수에 해리하여 수분을 제거하고, 수분이 제거된 습지에 경화제를 분사 도포 후 오븐에 건조하고, 정해진 두께로 압착하여 제조함으로써, 높은 인장강도와 저저항 및 내산성이 우수하여 잦은 충방전이 발생되는 전기차에 적용되어 효율이 우수한 배터리를 제작하는 데에 사용될 수 있다. The method for manufacturing a separator for a storage battery of the present invention comprises dissociating glass fiber yarn and synthetic fiber yarn in purified water to remove moisture, spraying a hardener on the wet surface from which moisture has been removed, drying in an oven, and pressing to a predetermined thickness, thereby manufacturing a battery having high tensile strength, low resistance, and excellent acid resistance, and thus can be used to manufacture a battery with excellent efficiency applied to electric vehicles that undergo frequent charging and discharging.
본 발명은 상술한 특정의 바람직한 실시예에 한정되지 아니하며, 청구범위에서 청구하는 본 발명의 요지를 벗어남이 없이 당해 고안이 속하는 기술분야에서 통상의 지식을 가진 자라면 누구든지 다양한 변형실시가 가능한 것은 물론이고, 그와 같은 변경은 청구범위 기재의 범위 내에 있게 된다.The present invention is not limited to the specific preferred embodiments described above, and anyone with ordinary skill in the art to which the present invention pertains may make various modifications without departing from the gist of the present invention claimed in the claims, and such modifications are within the scope of the claims.
Claims (5)
(A)유리섬유사 95중량%와, 합성섬유사 5중량%가 혼합된 6.028g의 제1섬유사와 상기 제1섬유사에 대한 0.05중량부를 추가로 계근한 제2섬유사로 이루어진 섬유사와, 정제수 2000ml를 준비하는 단계와; (B)상기 섬유사와 정제수를 섬유해리기에 투입하여 3분간 해리시키는 단계와; (C)상기 섬유해리기에서 해리된 현탁액을 80 WIRE MESH가 깔린 시트제작기에 투입하는 단계와; (D)상기 시트제작기에 투입된 현탁액에서 발생된 거품을 제거하기 위해 소포제를 투입하는 단계와; (E)상기 거품이 제거된 80MESH 습지를 수분흡수장치에 올려 60%수분을 제거하는 단계와; (F)상기 수분흡수장치에서 60%수분이 제거된 습지의 배면에 정제수에 정제수 대비 0.005중량부로 희석된 경화제를 스프레이 방식으로 분사시키는 단계와; (G)상기 경화제가 분사된 습지를 110℃ 온도의 오븐에 30분간 건조시키는 단계; 및 (H)상기 30분간 건조된 습지가 0.7t 두께로 성형되도록 프레스로 가압하는 단계;로 이루어지고, 상기 경화제는 상기 섬유사 대비 0.01중량부가 분사되며,
상기 제2섬유사는 0.200g 내지 0.302g 사이에서 정해지고, 상기 합성섬유사는 폴리에틸렌사, 폴리푸로필렌사, 폴리에스텔사 중 어느 하나로 구비되고,
상기 경화제는 메틸올요소 20~30중량%, 수용성 합성수지 20~30중량% 및 물 40~60중량%로 조성된 수성에멀젼으로 구비되며,
상기 (H)단계는 상기 프레스의 가압시 20kgf/cm2 로 가압하며,
상기 (G)단계에서 건조된 상기 습지의 수분율은 0.3% 미만인 것을 특징으로 하는 축전지용 격리판 제조방법.In a method for manufacturing a separator for a battery,
(A) A step for preparing a fiber yarn comprising 6.028 g of a first fiber yarn mixed with 95 wt% of glass fiber yarn and 5 wt% of synthetic fiber yarn and a second fiber yarn additionally weighing 0.05 wt% based on the first fiber yarn, and 2,000 ml of purified water; (B) A step for dissociating the fiber yarn and the purified water into a fiber dissociator for 3 minutes; (C) A step for dissociating the suspension dissociated in the fiber dissociator into a sheet manufacturing machine having 80 WIRE MESH; (D) A step for adding an antifoaming agent to remove bubbles generated in the suspension fed into the sheet manufacturing machine; (E) A step for removing 60% of the moisture from the 80MESH wetland from which the bubbles have been removed by placing it on a moisture absorption device; (F) A step for spraying a hardener diluted in purified water at 0.005 wt% based on purified water onto the back surface of the wetland from which 60% of the moisture has been removed in the moisture absorption device; (G) a step of drying the wetland sprayed with the hardener in an oven at a temperature of 110°C for 30 minutes; and (H) a step of pressing the wetland dried for 30 minutes so that it is molded to a thickness of 0.7 t; wherein the hardener is sprayed in an amount of 0.01 weight part relative to the fiber.
The above second fiber yarn is determined between 0.200 g and 0.302 g, and the above synthetic fiber yarn is provided as one of polyethylene yarn, polypropylene yarn, and polyester yarn.
The above curing agent is provided as an aqueous emulsion composed of 20 to 30 wt% of methylol urea, 20 to 30 wt% of water-soluble synthetic resin, and 40 to 60 wt% of water.
The above step (H) applies pressure of 20 kgf/cm 2 when the press is pressed.
A method for manufacturing a battery separator, characterized in that the moisture content of the wetland dried in the above step (G) is less than 0.3%.
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