KR100454270B1 - Low Roughness Electrodeposited Copper Foil Manufacturing Method And Electrodeposited Copper Foil Thereby - Google Patents

Low Roughness Electrodeposited Copper Foil Manufacturing Method And Electrodeposited Copper Foil Thereby Download PDF

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KR100454270B1
KR100454270B1 KR10-2002-0075411A KR20020075411A KR100454270B1 KR 100454270 B1 KR100454270 B1 KR 100454270B1 KR 20020075411 A KR20020075411 A KR 20020075411A KR 100454270 B1 KR100454270 B1 KR 100454270B1
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copper foil
electrolytic copper
ppm
low
roughness
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KR10-2002-0075411A
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KR20040047263A (en
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김상겸
최창희
조차제
김정익
우경녕
기준서
문홍기
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엘지전선 주식회사
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Priority to US10/720,579 priority patent/US20040104118A1/en
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    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25CPROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C1/00Electrolytic production, recovery or refining of metals by electrolysis of solutions
    • C25C1/12Electrolytic production, recovery or refining of metals by electrolysis of solutions of copper
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D3/00Electroplating: Baths therefor
    • C25D3/02Electroplating: Baths therefor from solutions
    • C25D3/38Electroplating: Baths therefor from solutions of copper
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D1/00Electroforming
    • C25D1/04Wires; Strips; Foils
    • HELECTRICITY
    • H05ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
    • H05KPRINTED CIRCUITS; CASINGS OR CONSTRUCTIONAL DETAILS OF ELECTRIC APPARATUS; MANUFACTURE OF ASSEMBLAGES OF ELECTRICAL COMPONENTS
    • H05K1/00Printed circuits
    • H05K1/02Details
    • H05K1/09Use of materials for the conductive, e.g. metallic pattern

Abstract

본 발명은 저조도 전해동박의 제조방법 및 전해동박에 관한 것으로, 황산, 구리이온 및 염소이온을 기본조성으로 하는 전해액을 사용하고, 이에 첨가제를 투입하는데 본 발명에서 사용되는 첨가제는 0.05∼50ppm의 HEC(Hydroxyethyl Cellulose), 0.05 ∼ 20ppm의 SPS(bis(sodiumsulfopropyl)disulfide) 및 0.1∼100ppm의 젤라틴을 인 것을 특징으로 하며, 기존의 제박설비를 활용하여 저조도의 전해동박을 제조하고 제조된 전해동박을 회로기판용 동박적층판의 재료 및 리튬이온전지용 전극재료로 활용할 수 있다.The present invention relates to a method of manufacturing a low-light electrolytic copper foil and an electrolytic copper foil, using an electrolyte solution based on sulfuric acid, copper ions, and chlorine ions, and adding an additive thereto. The additive used in the present invention is 0.05 to 50 ppm of HEC (Hydroxyethyl Cellulose), 0.05-20ppm SPS (bis (sodiumsulfopropyl) disulfide) and 0.1-100ppm gelatin. It can be used as a material and electrode material for lithium ion batteries.

Description

저조도 전해동박의 제조방법 및 전해동박{Low Roughness Electrodeposited Copper Foil Manufacturing Method And Electrodeposited Copper Foil Thereby}Low Roughness Electrodeposited Copper Foil Manufacturing Method And Electrodeposited Copper Foil Thereby}

본 발명은 인쇄회로기판(PCB; printed circuit board)용 절연기판(prepreg)에 접착되는 전해동박(electrodeposited copper foil)의 제조방법에 관한 것으로, 보다 상세하게는 전해동박의 접착면(Matte side)의 조도(roughness)를 낮추어 미세패턴(fine pattern) 형성시에도 잔동이 남지 않게 하도록 하는 제조방법과 그 제조방법으로 제조되는 전해동박에 관한 것이다.BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for manufacturing an electrodeposited copper foil adhered to an insulator substrate for a printed circuit board (PCB), and more particularly, to the roughness of the matte side of the electrolytic copper foil ( The present invention relates to a manufacturing method for lowering roughness so that no residual material remains even when forming a fine pattern, and an electrolytic copper foil manufactured by the manufacturing method.

일반적으로 인쇄회로기판은 라디오, 텔레비전, 세탁기, VTR 등의 민생용 전기/전자제품 및 컴퓨터, 무선통신기기, 각종제어기기 등의 산업용 전가/전자기기의 정밀제어에 광범위하게 사용되고 있다. 산업용 인쇄회로의 절연기판으로는 주로 유리섬유를 에폭시(epoxy) 수지에 함침시킨 난연성(frame retardant)의 프리프레그(prepreg)가 사용되고 있으며, 이러한 절연기판에 인쇄회로용 전해동박을 고온고압 하에서 접착하고 회로설계에 따라 에칭하여 인쇄회로기판을 얻는다.Generally, printed circuit boards are widely used for precision control of consumer electronic / electronic products such as radios, televisions, washing machines, VTRs, and industrial electronic / electronic devices such as computers, wireless communication devices, and various control devices. Flame retardant prepreg in which glass fiber is impregnated with epoxy resin is used as insulation board of industrial printed circuit, and the electrolytic copper foil for printed circuit is bonded to this insulation board under high temperature and high pressure. Etched according to the design to obtain a printed circuit board.

절연기판에 접착되는 전해동박은 일반적으로 황산동 용액에서 연속적인 전해전착법으로 동생박(raw foil)을 만들고 이를 절연기판과의 접착력 향상을 위해 동생박면에 동(copper) 노듈(nodule)을 형성하는 거침도금처리를 하거나, 거침 처리된 표면에 배리어(barrier)층을 형성시킨 후 전해 크로메이트(chromate) 방청처리하여 전해동박을 얻고 있다. 연속적인 전해전착법으로 동생박을 제조하는 경우, 통상적으로 음극인 드럼면에 맞닿은 면은 샤이니면(Shiny side), 전해액쪽의 면은 매트면(Matte side)이라고 부른다.Electrolytic copper foil adhered to an insulating substrate is generally a rough foil in the copper sulfate solution to form a raw foil (copper nodule) on the surface of the sister foil to improve the adhesion with the insulating substrate Electrolytic copper foil is obtained by forming a barrier layer on the surface which has been plated or roughened and then electrolytic chromate rust treatment. In the case of preparing the brother foil by the continuous electrolytic electrodeposition method, the surface of the drum face, which is usually the negative electrode, is called the Shiny side, and the surface of the electrolyte side is called the Matte side.

최근에는 전기/전자기기의 경박 단소화가 가속화됨에 따라서 기판용 인쇄회로가 미세화, 고집적 소형화 되고 있으며, 이에 따라서 기판 및 인쇄회로의 제조방법 강화로 정밀 인쇄회로기판으로 적합한 극저조도 동박이 개발되고 있다.In recent years, as the light and thin shortening of electrical and electronic devices is accelerated, printed circuit boards have been miniaturized and highly integrated and miniaturized. Accordingly, ultra-low roughness copper foils suitable for precision printed circuit boards have been developed by strengthening the manufacturing method of substrates and printed circuits.

종래 전해동박을 제조하는 기술로서, 첫번째 방법이, 전해되는 구간을 양분하여 첫번째 구간보다 두번째 구간의 전류 밀도를 높임으로써, 저조도 동박을 얻는것이다. 그런데 상기한 방법은 제조 설비의 개조에 따른 상당한 비용이 소요되는 문제점이 있다.As a technique for manufacturing a conventional electrolytic copper foil, the first method is to obtain a low light copper foil by dividing the section to be electrolytically and increasing the current density of the second section than the first section. However, the above method has a problem in that it takes a considerable cost according to the modification of the manufacturing equipment.

또한 상기와 같이 제조 설비인 제박기의 구조를 변경시키는 것은 통상 수퍼 아노드(super anode)란 장치를 부착하는 것을 말하는 것이다. 이러한 수퍼 아노드를 적용하면 수퍼 아노드와 본 아노드에 걸어 인가주는 전류량을 조절함으로써 초기 핵 생성시 핵의 크기를 바꿀 수 있다. 초기 핵의 크기를 미세하게 조절함으로써 저조도 동박을 제조할 수 있으나, 이 방법만으로는 현재의 미세회로 패턴에 대응하는 저조도의 동박을 얻을 수 없는 문제점이 있다.In addition, to change the structure of the manufacturing machine which is a manufacturing facility as mentioned above generally means attaching a device as a super anode. By applying such a super anode, the size of the nucleus can be changed during the initial nucleation by adjusting the amount of current applied to the super and bone anodes. By adjusting the size of the initial nucleus finely, it is possible to produce a low-light copper foil, there is a problem that can not obtain a low-light copper foil corresponding to the current microcircuit pattern only by this method.

두번째 방법으로, 전해액(electrolyte) 중 염소 이온(Chloride ion)의 농도를 1 ppm 이하로 낮추어 저조도 동박을 얻는 방법이 알려져 있으나, 전해 동박의 제조의 경우 대부분 원재료로 동 스크랩(scrap)을 사용하고 있는데, 염소 이온의 농도를 1 ppm 이하로 낮추는 것은 사실상 실험실에서나 가능한 수준이며 대량 생산체제에서 동 스크랩을 사용하게 되면 동 스크랩의 대부분을 차지하고 있는 폐전선으로부터의 염소 이온을 막을 수 있는 경제적인 방법이 아직까진 개발되지 못하고 있다. 따라서 실용성이 거의 희박한 한계를 안고 있다.As a second method, a method of obtaining low light copper foil by reducing the concentration of chloride ion in an electrolyte to 1 ppm or less is known. However, in the manufacture of electrolytic copper foil, copper scrap is used as a raw material. For example, lowering the concentration of chlorine ions below 1 ppm is practically possible in the laboratory, and the use of copper scrap in mass production systems still provides an economical way to prevent chlorine ions from the waste wires that make up most of the scrap. It is not being developed until now. Therefore, practicality is rarely limited.

세번째 방법으로, 일반적으로 제조된 전해 동박을 버핑(buffing)을 통하여 기계적으로 연마하여 저조도 동박을 얻는 방법이 알려져 있으나, 이 방법은 별도의 생산 설비를 갖춰야 한다는 점과 버핑 공정시 발생한 동분이 남아 있으면 인쇄회로기판 제조시 잔동으로 남을 우려가 있는 문제점이 있다.As a third method, a method of obtaining a low roughness copper foil by mechanically polishing an electrolytic copper foil manufactured by buffing is generally known. However, this method requires that a separate production facility be provided and that copper content generated during the buffing process remains. There is a problem that may remain as a remnant when manufacturing a printed circuit board.

네번째 방법으로, 전해액에 첨가하는 첨가제를 바꾸어서 동박의 표면 형상(morphology)을 조절하는 방법이 있다. 보다 구체적으로 저분자량 수용성 셀루로우스 에테르(Low molecular weight water-soluble cellulose ether), 저분자량 수용성 폴리알킬렌 글리콜 에테르(Low molecular weight water-soluble polyalkylene glycol ether), 저분자 수용성 폴리에틸렌 이민(Low molecular weight water-soluble polyethyleneimine), 수용성 설포네이티드 유기 황 화합물 (water-soluble sulfonated organic sulfur compound)를 적정량 첨가하여 저조도 동박을 얻는 방법이다. 상기한 방법은 기존 제박기의 변경 및 개조 없이 전해액의 첨가제 만을 변경함으로써 원하는 저조도의 동박을 얻을 수 있고, 버핑 같은 기계적 연마 공정도 필요치 않으며 염소 이온을 극도로 낮게 관리할 필요도 없어 가장 경제적이고 바람직한 방법이라고 할 수 있다.As a fourth method, there is a method of controlling the surface morphology of the copper foil by changing the additives added to the electrolyte solution. More specifically, low molecular weight water-soluble cellulose ethers, low molecular weight water-soluble polyalkylene glycol ethers, and low molecular weight water-soluble polyethylene imines It is a method of obtaining low light copper foil by adding an appropriate amount of -soluble polyethyleneimine) and water-soluble sulfonated organic sulfur compound. The above-described method can obtain the desired low-light copper foil by changing only the additives of the electrolyte without changing or modifying the existing milling machine, eliminating the need for mechanical polishing processes such as buffing, and managing extremely low chlorine ions. It can be called a method.

하지만 이와 같은 방법으로 제조된 동박의 경우 매트면(matte side)의 조도 Rz 값이 3.81㎛ 수준이어서 최근의 저조도 동박의 요구에 부응하지 못한다.However, in the case of the copper foil manufactured by the above method, the roughness Rz value of the matte side is 3.81 µm, which does not meet the demand of the recent low roughness copper foil.

다섯번째 방법으로, 적은 양의 폴리에틸렌 글리콜(Polyethylene glycol), 주석이온(tin ion), 철이온(iron ion) 및 0.1 ppm 이하의 염소 이온을 포함하는 전해액으로 저조도의 동박을 제조하는 방법이 알려져 있으나, 이 방법도 앞서 기술한 바와 같이 사실상 염소이온의 농도를 0.1ppm 이하로 유지하는 것이 대량생산 체계에서는 불가능한 실용성의 한계를 안고 있다.As a fifth method, a method of manufacturing low-light copper foil using an electrolyte solution containing a small amount of polyethylene glycol, tin ions, iron ions, and chlorine ions of 0.1 ppm or less is known. However, this method, as described above, has a practical limit that is practically impossible to maintain in the concentration of chlorine ion below 0.1 ppm in mass production system.

따라서 본 발명은 상기와 같은 종래의 문제점을 감안하여 안출된 것으로, 본 발명의 제 1 목적은, 동박의 제조시 기존에 사용하고 있는 제박기의 설계 변경이나개조가 불필요하며, 기계적 연마와 같은 추가적인 설비와 공정의 추가없이 기존에 사용하던 저가의 폐전선류의 원재료를 그대로 사용하면서 최적의 첨가제 시스템을 구축하여 저조도의 물성을 갖는 전해동박을 제조할 수 있는 저조도 전해동박의 제조방법 및 전해동박을 제공하는 것이다.Accordingly, the present invention has been made in view of the above-mentioned conventional problems, and the first object of the present invention is that it is unnecessary to change or modify the design of the existing mill in the manufacture of copper foil, and it is possible to add additional mechanical such as mechanical polishing. It is to provide a low-light electrolytic copper foil manufacturing method and an electrolytic copper foil that can produce an electrolytic copper foil having low roughness properties by using an optimal additive system while using the raw materials of the existing low-cost waste wire flow without additional equipment and processes.

그리고 본 발명의 제 2 목적은, 리튬이온 전지의 전극, 동박적층판 및 이를 재료로 이용하는 인쇄회로기판, 연성회로기판 등의 전자기기 등으로 활용할 수 있는 저조도 전해동박의 제조방법 및 전해동박을 제공하는 것이다.A second object of the present invention is to provide a method of manufacturing a low-light electrolytic copper foil and an electrolytic copper foil that can be utilized as an electronic device such as an electrode of a lithium ion battery, a copper foil laminated plate, a printed circuit board, and a flexible circuit board using the same.

이러한 본 발명의 목적들은, 회전하는 음극의 드럼(100) 및 상기 드럼(100)의 외주연에 대해 소정간극을 갖고 형상적으로 대응하는 양극판(200)이 전해액(600)에 수장되고,Objects of the present invention, the drum 100 of the rotating negative electrode and the positive electrode plate 200 corresponding to the shape having a predetermined gap with respect to the outer periphery of the drum 100 is stored in the electrolyte 600,

상기 전해액(600)은 황산, 구리이온 및 염소이온을 포함하고,The electrolyte 600 includes sulfuric acid, copper ions and chlorine ions,

상기 드럼(100) 및 양극판(200)에 해당 극성의 전류가 인가되면서 상기 드럼(100)의 표면에 전해동박(400)이 전착되는 전해동박(400)의 제조방법에 있어서,In the manufacturing method of the electrolytic copper foil 400, the electrolytic copper foil 400 is electrodeposited on the surface of the drum 100 while a current of a corresponding polarity is applied to the drum 100 and the positive electrode plate 200,

상기 전해액(600)에는 0.1∼100ppm의 젤라틴, 0.05∼50ppm의 HEC (Hydroxyethyl Cellulose) 및 0.05 ∼ 20ppm의 SPS (bis(sodiumsulfopropyl)disulfide) 을 첨가제로 투입하여 제조되는 것을 특징으로 하는 저조도 전해동박의 제조방법에 의하여 달성된다.The electrolytic solution 600 is prepared by adding 0.1 to 100 ppm gelatin, 0.05 to 50 ppm HEC (Hydroxyethyl Cellulose), and 0.05 to 20 ppm SPS (bis (sodiumsulfopropyl) disulfide) as an additive. Is achieved.

여기서 상기 젤라틴의 첨가량은 2∼5ppm 인 것이 보다 바람직하다.As for the addition amount of the said gelatin, it is more preferable that it is 2-5 ppm.

그리고 상기 HEC 의 첨가량은 1∼3ppm 인 것이 보다 바람직하다.And it is more preferable that the addition amount of the said HEC is 1-3 ppm.

아울러 상기 SPS의 첨가량은 0.5∼3ppm 인 것이 보다 바람직하다.Moreover, it is more preferable that the addition amount of the said SPS is 0.5-3 ppm.

또한 상기 젤라틴의 분자량은 10,000 이상인 것이 바람직하다.In addition, the gelatin molecular weight is preferably 10,000 or more.

아울러 상기 전해동박(400)의 일면 또는 양면에 노듈을 더 형성시키는 후처리 과정이 추가되는 것이 바람직하다.In addition, it is preferable that a post-treatment process of further forming a nodule on one or both surfaces of the electrolytic copper foil 400 is added.

그리고 상기 전해동박(400)의 매트(matte) 면의 조도가 샤이니(shiny) 면의 조도보다 큰 것이 바람직하다.In addition, the roughness of the matte surface of the electrolytic copper foil 400 is preferably larger than that of the shiny surface.

상기와 같은 본 발명의 목적들은, 상기한 방법에 의해 제조되는 것을 특징으로 하는 저조도 전해동박에 의하여 달성된다.The objects of the present invention as described above are achieved by a low light electrolytic copper foil, which is produced by the above method.

이 때 상기 전해동박(400)은 후처리 과정으로 일면 또는 양면에 노듈이 더 형성된 것이 바람직하다.At this time, the electrolytic copper foil 400 is preferably a nodule further formed on one side or both sides as a post-treatment process.

또한 상기 전해동박(400)의 매트(matte) 면의 조도가 샤이니(shiny) 면의 조도보다 큰 것이 바람직하다.In addition, it is preferable that the roughness of the matte surface of the electrolytic copper foil 400 is larger than the roughness of the shiny surface.

본 발명의 그 밖의 목적, 특정한 장점들 및 신규한 특징들은 첨부된 도면들과 연관되어지는 이하의 상세한 설명과 바람직한 실시예들로부터 더욱 분명해질 것이다.Other objects, specific advantages and novel features of the present invention will become more apparent from the following detailed description and the preferred embodiments associated with the accompanying drawings.

도 1은 본 발명에 따른 전해동박의 제조방법의 공정을 도시한 구성도,1 is a block diagram showing a process of the manufacturing method of the electrolytic copper foil according to the present invention,

도 2는 본 발명의 실시예 1에 따라 제조된 전해동박의 전자현미경(SEM) 촬영 사진도,Figure 2 is an electron microscope (SEM) photographic photograph of the electrolytic copper foil prepared according to Example 1 of the present invention,

도 3은 본 발명의 비교예 2에 따라 제조된 전해동박의 전자현미경(SEM) 촬영 사진도이다.3 is an electron micrograph (SEM) photographing picture of the electrolytic copper foil prepared according to Comparative Example 2 of the present invention.

< 도면의 주요부분에 관한 부호의 설명 ><Description of the code | symbol about the principal part of drawing>

100 : 드럼 200 : 양극판100: drum 200: positive plate

300 : 롤러 400 : 전해동박300: roller 400: electrolytic copper foil

500 : 탱크 600 : 전해액500 tank 600 electrolyte solution

다음으로는 본 발명에 따른 저조도 전해동박의 제조방법 및 전해동박에 관하여 첨부되어진 도면과 더불어 설명하기로 한다.Next, a method of manufacturing a low-light electrolytic copper foil and an electrolytic copper foil according to the present invention will be described with reference to the accompanying drawings.

도 1은 본 발명에 따른 전해동박의 제조방법의 공정을 도시한 구성도이다.1 is a block diagram showing a process of the method for producing an electrolytic copper foil according to the present invention.

도 1에 도시된 바와 같이, 전해동박(400)의 제조를 위한 장치로서 제박기는,회전하는 드럼(100)과 둥근 판재 형태인 양극판(200)이 소정간극으로 이격되어 설치되어 있는 구조인데, 상기 드럼(100)과 양극판(200)은 전해액(600)이 담긴 탱크(500)에 수장되어 있다.As shown in FIG. 1, a device for manufacturing an electrolytic copper foil 400 is a structure in which a rotating drum 100 and a positive plate 200 having a round plate shape are spaced apart from each other by a predetermined gap. The drum 100 and the positive electrode plate 200 are stored in a tank 500 containing the electrolyte solution 600.

이 때 상기 드럼(100)은 회전중심을 중심으로 상대적으로 아랫부분이 수장되고, 그 수장된 부위에 형상적으로 대응하여 상기 양극판(200)이 수장되어 있으며, 드럼(100) 및 양극판(200)은 각각 음극 및 양극으로 구분되어 각 극성에 맞는 전류가 인가된다.At this time, the drum 100 has a lower portion relative to the center of rotation, and the positive electrode plate 200 is accommodated in shape corresponding to the stored portion, the drum 100 and the positive electrode plate 200 Are divided into a cathode and an anode, respectively, and a current corresponding to each polarity is applied.

이에 따라 상기 드럼(100) 및 양극판(200) 사이에서 전해가공이 발생하며 이에 따라 드럼(100)의 표면에는 전해동박(400)이 전착된다. 전착되는 전해동박(400)은 우측 상부의 롤러(300)에 의해 이끌려 수득된다.Accordingly, electrolytic processing occurs between the drum 100 and the positive electrode plate 200, and thus the electrolytic copper foil 400 is electrodeposited on the surface of the drum 100. Electrolytic copper foil 400 to be electrodeposited is obtained by the roller 300 of the upper right.

이 때 상기 탱크(500) 내에 담겨진 전해액(600)의 기본조성은 약 50 ∼ 200 g/ℓ정도의 황산(H2SO4)과, 약 30 ∼ 150 g/ℓ정도의 구리이온(Cu2+)과, 약 200㎎/ℓ이하의 염소이온(Cl-)이다. 그리고 상기 전해액(600)의 온도는 약 20 ∼ 80℃이며, 전류밀도는 약 20 ∼ 150 A/d㎡ 정도가 적당하다.At this time, the basic composition of the electrolyte 600 contained in the tank 500 is sulfuric acid (H 2 SO 4 ) of about 50 to 200 g / ℓ, and copper ions (Cu 2+ of about 30 to 150 g / ℓ) ) And about 200 mg / l or less of chloride ion (Cl ). The temperature of the electrolyte 600 is about 20 to 80 ° C., and the current density is about 20 to 150 A / dm 2.

아울러 상기한 방법으로 제조되는 전해동박(400)의 물성을 조절하기 위해서 전해액(600)에는 첨가제가 투입되는 것이 통상적이다. 본 발명에서는 상기 첨가제로서 젤라틴, HEC(Hydroxyethyl Cellulose), SPS(bis(sodiumsulfopropyl)disulfide)를 이용하여 미세 회로 패턴의 형성 및 리튬 이온 전지의 전극재료용으로 사용 가능한 저조도의 전해동박(400)의 제조를 달성하였다.In addition, in order to control the physical properties of the electrolytic copper foil 400 manufactured by the above method, it is common that an additive is added to the electrolyte solution 600. In the present invention, using the gelatin, HEC (Hydroxyethyl Cellulose), SPS (bis sodium sulfopropyl) disulfide (SPS) as the additive to form a fine circuit pattern and the production of a low-light electrolytic copper foil 400 that can be used for the electrode material of a lithium ion battery Achieved.

이 때 상기 첨가제로서 젤라틴은 유도 단백질의 일종으로 본 발명에서는 분자량이 12,000의 젤라틴이 이용되고, 투입량은 최소 약 0.1ppm 내지 최대 약 100ppm 이며, 상기한 투입 범위중에서도 보다 바람직하게는 약 1 ∼ 10 ppm가 투입되는 것이 좋지만, 최적의 실시예로서 약 2 ∼ 5ppm 정도이다.In this case, gelatin is a derivative protein, and in the present invention, gelatin having a molecular weight of 12,000 is used, and the dosage is at least about 0.1 ppm to at most about 100 ppm, more preferably in the range of about 1 to 10 ppm. Is preferably added, but it is about 2 to 5 ppm as an optimal embodiment.

만일 젤라틴이 0.1 ppm 이하로 전해액(600)에 첨가되어 이용될 경우, 보다 미세한 초기조직을 얻을 수 있으나, 전해동박(400)의 성장을 촉진시켜 조대한 조직의 전해동박(400)이 얻어지고 이렇게 조대한 조직은 높은 피크 높이를 가지게 되어 결국 원하는 저조도의 전해동박(400)을 얻을 수 없다.If gelatin is added to the electrolytic solution 600 at 0.1 ppm or less, a finer initial structure can be obtained, but the electrolytic copper foil 400 of coarse tissue is obtained by promoting the growth of the electrolytic copper foil 400. The tissue has a high peak height, and thus, it is impossible to obtain the desired low roughness electrolytic copper foil 400.

그리고 젤라틴이 100ppm 이상으로 전해액(600)에 첨가되어 이용될 경우, 조대 성장을 억제하여 저조도의 전해동박(400)을 얻을 수 있으나, 미세 회로 형성시의 또 다른 주요 특성 중의 하나인 고온 연신율(HTE; High Temperature Elongation, 180℃에서 측정) 특성이 현저하게 떨어지는 단점을 가지게 된다.In addition, when gelatin is added to the electrolyte solution 600 at 100 ppm or more, the coarse growth can be suppressed to obtain an electrolytic copper foil 400 having low roughness, but a high temperature elongation (HTE), which is one of the main characteristics in forming a fine circuit; High Temperature Elongation (measured at 180 ℃) has the disadvantage of remarkably falling.

그리고 첨가제로 이용되는 상기 HEC의 첨가량은 최소 약 0.05 내지 최대 약 50ppm이며 보다 바람직하게는 약 0.5 ∼ 5 ppm이다. 그 중에서도 가장 최적의 실시예는 약 1 ∼ 3ppm이다. 이러한 상기 HEC는 앞서 언급된 SPS 및 젤라틴과 더불어 상기 전해액(600)에 투입되어 전해가공에 이용될 경우 서로 간에 교번하여 일어나는 상호 작용(이하 교호작용)을 함으로써 보다 안정된 저조도의 동박을 제조하는데 기능할 수 있다.And the amount of the HEC added as an additive is at least about 0.05 to at most about 50 ppm and more preferably about 0.5 to 5 ppm. Among them, the most optimal embodiment is about 1 to 3 ppm. The HEC, together with the above-mentioned SPS and gelatin, is put into the electrolyte solution 600 and used to perform electrolytic processing, thereby functioning to produce a more stable low-light copper foil by performing interactions that occur alternately with each other (hereinafter referred to as interaction). Can be.

만일 상기 HEC가 0.05 ppm 이하로 전해액(600)에 첨가되어 이용될 경우, 교호작용 능력이 떨어져 균일하지 않은 전해동박(400)이 제조될 수 있다. 또한 50ppm 이상 첨가되어 이용될 경우 전해동박(400)에서 동분을 석출시키는데 기능함으로써 만일 50ppm 이상의 HEC가 전해액(600)에 첨가되어 전해동박(400)을 제조할 경우 상기 전해동박(400)으로 회로기판용 동박적층판을 제조하고 이를 인쇄회로기판 제조시 이용하게 되면 불량의 원인을 제공하게 된다.If the HEC is added to the electrolyte 600 at 0.05 ppm or less and used, the electrolytic copper foil 400 having a low interaction ability may be manufactured. In addition, if 50ppm or more is used to function to precipitate copper in the electrolytic copper foil 400, if more than 50ppm HEC is added to the electrolyte 600 to produce the electrolytic copper foil 400, the electrolytic copper foil 400, a copper foil laminated board for a circuit board If manufactured and used to manufacture the printed circuit board provides a cause of failure.

아울러 상기 SPS가 전해액(600)에 첨가되는 투입량은 최소 약 0.05ppm 내지 최대 20ppm인 것이 바람직하다. 이러한 투입범위에서도 보다 바람직하게는 약 0.1 ∼ 10 ppm 정도이며, 최적의 실시예로서는 0.5 ∼ 3ppm인 것이 좋다.In addition, the input amount of the SPS is added to the electrolyte 600 is preferably at least about 0.05ppm to 20ppm maximum. More preferably, it is about 0.1-10 ppm, and, as an optimal Example, it is good that it is 0.5-3 ppm.

상기 SPS는 도금시 광택제(brightener)로 이용되는 물질이며, 첨가되어 이용할 경우 HEC와 젤라틴과의 교호작용을 통해 도금되는 조직의 조도를 낮추는데 기능한다. 만일 SPS가 0.05 ppm 이하로 첨가되어 이용될 경우 교호작용 능력이 떨어져 조도가 균일하지 않은 전해동박(400)이 제조될 수 있으며, 또한 20ppm 이상 첨가되어 이용될 경우에는 소정의 특성발현에 전혀 기능하지 못한다.The SPS is a material used as a brightener when plating, and when used, it functions to lower the roughness of the plated tissue through interaction between HEC and gelatin. If the SPS is used in an amount of 0.05 ppm or less, the electrolytic copper foil 400 having a low roughness may be produced due to its low interaction ability, and when used in an amount of 20 ppm or more, it may not function at all. .

이하에서는 첨가제로서 전해액(600)에 투입되는 상기의 젤라틴, HEC, SPS의 투입양을 ppm 단위로 달리하여 전해동박(400)을 제조한 3가지의 실시예에 관하여 설명하기로 한다.Hereinafter, three examples of manufacturing the electrolytic copper foil 400 by varying the amount of the gelatin, HEC, and SPS added to the electrolyte 600 as additives in ppm units will be described.

실시예Example

본 발명에서 제조되는 전해동박(400)의 전해조건 즉 전해액(600)의 기본조성을 약 100 g/ℓ의 황산(H2SO4), 약 100 g/ℓ의 구리이온(Cu2+), 30㎎/ℓ의염소이온(Cl-)으로 하고, 이 때 전해액(600)의 온도는 약 60℃ 이며, 전류밀도는 약 100 A/d㎡로 하여 제조하였다.Electrolytic conditions of the electrolytic copper foil 400 manufactured in the present invention, that is, the basic composition of the electrolyte solution 600 of about 100 g / L sulfuric acid (H 2 SO 4 ), about 100 g / L copper ion (Cu 2 + ), 30mg Chlorine ion (Cl ) of 1 / L, wherein the temperature of the electrolyte solution 600 was about 60 ° C., and the current density was about 100 A / dm 2.

그리고 상기 전해액(600)에 첨가된 첨가제의 첨가량은 표 1과 같다. 이렇게 제조된 전해 동박의 일부를 통상적인 전해동박(400)의 후처리를 거쳐 동박적층판을 제조한 뒤. 인쇄회로 기판 또는 연성회로기판에 적용 가능하도록 제조하였다.And the addition amount of the additive added to the electrolyte 600 is shown in Table 1. After the part of the electrolytic copper foil thus prepared is subjected to the post-treatment of a conventional electrolytic copper foil 400 to produce a copper foil laminated plate. It is manufactured to be applicable to a printed circuit board or a flexible circuit board.

통상적인 전해동박(400)의 후처리란 수지와의 접착력을 증대시키기 위한 노듈처리, 동층이 수지층으로 확산되는 것을 막기 위한 배리어(barrier)처리, 동층의 산화를 막기 위한 방청처리, 수지와의 접착시 그 신뢰도를 높이기 위한 실란 커플링제(Silane coupling agent)처리이다.The post-treatment of a conventional electrolytic copper foil 400 is a nodule treatment for increasing adhesion to the resin, a barrier treatment for preventing the copper layer from diffusing into the resin layer, an antirust treatment for preventing oxidation of the copper layer, and adhesion to the resin. Silane coupling agent treatment to increase the reliability.

젤라틴gelatin HECHEC SPSSPS 실시예 1Example 1 2.5ppm2.5 ppm 3ppm3 ppm 1.5ppm1.5 ppm 실시예 2Example 2 3.5ppm3.5 ppm 1ppm1 ppm 2.5ppm2.5 ppm 실시예 3Example 3 4.5ppm4.5 ppm 2ppm2 ppm 0.5ppm0.5 ppm

상기와 같이 제조된 전해동박(400)은 절연필름층, 접착층과 더불어 동박적층판을 이루며, 상기 동박적층판은 소정의 회로설계에 따라 에칭되어 회로기판으로 제조될 수 있다.The electrolytic copper foil 400 manufactured as described above forms a copper foil laminated plate together with an insulating film layer and an adhesive layer, and the copper foil laminated plate may be etched according to a predetermined circuit design to be manufactured as a circuit board.

이하에서는 상기 각 실시예에 대해 기존 전해조건에 의거한 전해액(600)으로 전해동박(400)을 제조하는 2가지의 비교예를 제시한다.Hereinafter, two comparative examples of manufacturing the electrolytic copper foil 400 using the electrolyte 600 based on the existing electrolytic conditions for each of the above embodiments will be presented.

비교예Comparative example

비교예의 전해조건에서의 전해액(600)의 기본조성은 약 100 g/ℓ정도의황산(H2SO4) , 약 100 g/ℓ정도의 구리이온(Cu2+), 약 30㎎/ℓ정도의 염소이온(Cl-)이다. 그리고 이렇게 조성된 전해액(600)의 온도는 약 60℃정도이며, 전류밀도는 약 100 A/d㎡로 하였다. 이 때 첨가된 첨가제의 첨가량은 하기의 표 2와 같다.Under the electrolytic conditions of Comparative Example, the basic composition of the electrolyte solution 600 was about 100 g / l of sulfuric acid (H 2 SO 4 ), about 100 g / l of copper ions (Cu 2+ ), and about 30 mg / l. a - a chloride ion (Cl). The temperature of the electrolyte solution 600 thus prepared was about 60 ° C., and the current density was about 100 A / dm 2. The amount of the additive added at this time is shown in Table 2 below.

이렇게 제조된 전해동박(400)의 일부를 상기 전해동박(400)의 실시예에서 기술한 통상적인 후처리를 거쳐 동박적층판을 제조하고 인쇄회로기판 및 연성회로기판에 적용가능하도록 제조하였다A portion of the electrolytic copper foil 400 thus prepared was manufactured through a conventional post-treatment described in the embodiment of the electrolytic copper foil 400 to prepare a copper clad laminate and to be applicable to a printed circuit board and a flexible circuit board.

젤라틴gelatin HECHEC SPSSPS ThioureaThiourea 비교예 1Comparative Example 1 2.5ppm2.5 ppm -- 1.5ppm1.5 ppm -- 비교예 2Comparative Example 2 3.5ppm3.5 ppm -- -- 0.4ppm0.4 ppm

도 2는 본 발명의 실시예 1에 따라 제조된 전해동박의 전자현미경(SEM) 촬영 사진도이고, 도 3은 본 발명의 비교예 2에 따라 제조된 전해동박의 전자현미경(SEM) 촬영 사진도이다.2 is an electron micrograph (SEM) photographic view of the electrolytic copper foil prepared according to Example 1 of the present invention, Figure 3 is an electron micrograph (SEM) photographic view of the electrolytic copper foil prepared according to Comparative Example 2 of the present invention.

도 2 및 도 3에 도시된 바와 같이, 앞에서 언급된 본 발명에 따른 실시예와, 비교예에서 제조된 전해동박(400)을 후처리 공정을 거치기 이전에 SEM 사진 촬영을 한 결과가 도시되었다.As shown in FIG. 2 and FIG. 3, the SEM photographs of the embodiments according to the present invention mentioned above and the electrolytic copper foil 400 prepared in the comparative example before the post-treatment process are shown.

본 발명의 실시예에 따라 제조된 전해동박(400) 중 표 1의 실시예1에서 제조된 전해동박(400)의 표면 조도가 표 2의 비교예 2에서 제조된 전해동박(400)에 비해 상대적으로 낮고 매끈한 반면, 비교예 2에서의 전해동박(400)의 표면은 상대적으로 조도가 높음을 알 수 있다.Surface roughness of the electrolytic copper foil 400 prepared in Example 1 of Table 1 of the electrolytic copper foil 400 prepared according to the embodiment of the present invention is relatively low and smooth compared to the electrolytic copper foil 400 prepared in Comparative Example 2 of Table 2 On the other hand, the surface of the electrolytic copper foil 400 in Comparative Example 2 can be seen that the relatively high roughness.

이를 정량화하기 위해 조도 및 인장강도, 연신율, 고온인장강도, 고온 연신율을 측정하여 하기와 같이 표 3에 나타내었다.In order to quantify this, roughness and tensile strength, elongation, high temperature tensile strength and high temperature elongation were measured and shown in Table 3 as follows.

조도 Rz(㎛)Roughness Rz (㎛) 인장강도(kgf/㎟)Tensile strength (kgf / ㎡) 연신율(%)Elongation (%) 고온인장강도(kgf/㎟)High temperature tensile strength (kgf / ㎡) 고온연신율(%)Elongation at high temperature (%) 실시예 1Example 1 1.81.8 33.333.3 15.915.9 18.318.3 16.316.3 실시예 2Example 2 1.61.6 34.634.6 18.118.1 18.218.2 15.115.1 실시예 3Example 3 2.12.1 32.832.8 16.316.3 19.119.1 15.315.3 비교예 1Comparative Example 1 2.52.5 34.134.1 5.85.8 20.120.1 8.58.5 비교예 2Comparative Example 2 3.53.5 33.833.8 8.38.3 20.320.3 2.12.1

이상에서와 같은 본 발명에 따른 저조도 전해동박의 제조방법 및 전해동박에서, 각 실시예별로 언급된 첨가제의 양은 단지 하나의 실시예에 불과하며 본 발명에서 언급되어진 첨가범위에서 다른 다양한 실시예를 구현할 수 있음은 물론이다. 또한 그에 따라 다양한 특성의 전해동박(400), 동박적층판 및 회로기판을 제조하는데 기능할 수 있다.In the manufacturing method and the electrolytic copper foil of the low-light electrolytic copper foil according to the present invention as described above, the amount of the additive mentioned in each embodiment is only one embodiment and can be implemented in various other embodiments in the addition range mentioned in the present invention Of course. In addition, it can function to produce an electrolytic copper foil 400, a copper foil laminated plate and a circuit board of various characteristics.

이상에서와 같은 본 발명에 따른 저조도 전해동박의 제조방법 및 전해동박과 그를 이용한 전자부품에 의하면, 기존 제박시설 및 장치의 구조를 변경하지 않고도 보다 표면 조도가 낮은 전해동박을 제조할 수 있어 부대설비에 소요되는 비용의 추가없이 미세 및 고집적화를 위한 회로기판용 재료 및 리튬이온전지의 전극재료로서 활용할 수 있는 특징이 있다.According to the manufacturing method of the low roughness electrolytic copper foil according to the present invention and the electrolytic copper foil and the electronic component using the same according to the present invention, it is possible to manufacture the electrolytic copper foil having a lower surface roughness without changing the structure of the existing manufacturing facilities and equipment, which is required for the auxiliary equipment. There is a feature that can be utilized as a material for circuit boards for fine and high integration and electrode materials of lithium ion batteries without additional cost.

비록 본 발명이 상기 언급된 바람직한 실시예와 관련하여 설명되어졌지만, 발명의 요지와 범위로부터 벗어남이 없이 다양한 수정이나 변형을 하는 것이 가능하다. 따라서 첨부된 특허청구의 범위는 본 발명의 요지에서 속하는 이러한 수정이나 변형을 포함할 것이다.Although the present invention has been described in connection with the above-mentioned preferred embodiments, it is possible to make various modifications or variations without departing from the spirit and scope of the invention. Accordingly, the appended claims will cover such modifications and variations as fall within the spirit of the invention.

Claims (10)

회전하는 음극의 드럼(100) 및 상기 드럼(100)의 외주연에 대해 소정간극을 갖고 형상적으로 대응하는 양극판(200)이 전해액(600)에 수장되고,A drum 100 of a rotating cathode and a cathode plate 200 corresponding to a shape having a predetermined gap with respect to the outer periphery of the drum 100 are stored in the electrolyte 600, 상기 전해액(600)은 황산, 구리이온 및 염소이온을 포함하고,The electrolyte 600 includes sulfuric acid, copper ions and chlorine ions, 상기 드럼(100) 및 양극판(200)에 해당 극성의 전류가 인가되면서 상기 드럼(100)의 표면에 전해동박(400)이 전착되는 전해동박(400)의 제조방법에 있어서,In the manufacturing method of the electrolytic copper foil 400, the electrolytic copper foil 400 is electrodeposited on the surface of the drum 100 while a current of a corresponding polarity is applied to the drum 100 and the positive electrode plate 200, 상기 전해액(600)에는 0.1∼100ppm의 젤라틴, 0.05∼50ppm의 HEC (Hydroxyethyl Cellulose) 및 0.05 ∼ 20ppm의 SPS (bis(sodiumsulfopropyl)disulfide) 을 첨가제로 투입하여 제조되는 것을 특징으로 하는 저조도 전해동박의 제조방법.The electrolytic solution 600 is prepared by adding 0.1 to 100 ppm gelatin, 0.05 to 50 ppm HEC (Hydroxyethyl Cellulose), and 0.05 to 20 ppm SPS (bis (sodiumsulfopropyl) disulfide) as an additive. . 제1항에 있어서,The method of claim 1, 상기 젤라틴의 첨가량은 2∼5ppm 인 것을 특징으로 하는 저조도 전해동박의 제조방법.The addition amount of the gelatin is 2 to 5ppm method for producing a low roughness electrolytic copper foil. 제1항에 있어서,The method of claim 1, 상기 HEC 의 첨가량은 1∼3ppm 인 것을 특징으로 하는 저조도 전해동박의 제조방법.The addition amount of the said HEC is 1-3 ppm, The manufacturing method of the low roughness electrolytic copper foil characterized by the above-mentioned. 제1항에 있어서,The method of claim 1, 상기 SPS의 첨가량은 0.5∼3ppm 인 것을 특징으로 하는 저조도 전해동박의 제조방법.The addition amount of the said SPS is 0.5-3 ppm, The manufacturing method of the low roughness electrolytic copper foil characterized by the above-mentioned. 제 1항 또는 제 2항에 있어서,The method according to claim 1 or 2, 상기 젤라틴의 분자량이 10,000 이상인 것을 특징으로 하는 저조도 전해동박의 제조방법.A method for producing a low light electrolytic copper foil, characterized in that the molecular weight of the gelatin is 10,000 or more. 제 1항 내지 제 4항 중 어느 한항에 있어서,The method according to any one of claims 1 to 4, 상기 전해동박(400)의 일면 또는 양면에 노듈을 더 형성시키는 후처리 과정을 추가하는 것을 특징으로 하는 저조도 전해동박의 제조방법.Method for producing a low-light electrolytic copper foil, characterized in that for adding a post-treatment process to further form a nodule on one surface or both surfaces of the electrolytic copper foil (400). 제 1항 내지 제 4항 중 어느 한항에 있어서,The method according to any one of claims 1 to 4, 상기 전해동박(400)의 매트(matte) 면의 조도가 샤이니(shiny) 면의 조도보다 큰 것을 특징으로 하는 저조도 전해동박의 제조방법.The roughness of the matte surface of the electrolytic copper foil 400 is larger than the roughness of the shiny surface, the manufacturing method of the low-light electrolytic copper foil. 제 1항 내지 제 4항 중 어느 한항의 방법에 의해 제조되는 것을 특징으로 하는 저조도 전해동박.It is manufactured by the method of any one of Claims 1-4, The low light electrolytic copper foil characterized by the above-mentioned. 제 8항에 있어서,The method of claim 8, 상기 전해동박(400)은 후처리 과정으로 일면 또는 양면에 노듈이 더 형성된 것을 특징으로 하는 저조도 전해동박.The electrolytic copper foil 400 is a low light electrolytic copper foil, characterized in that the nodule is further formed on one side or both sides as a post-treatment process. 제 8항에 있어서,The method of claim 8, 상기 전해동박(400)의 매트(matte) 면의 조도가 샤이니(shiny) 면의 조도보다 큰 것을 특징으로 하는 저조도 전해동박.Low roughness electrolytic copper foil, characterized in that the roughness of the matte (matte) surface of the electrolytic copper foil (400) is larger than the roughness of the shiny (shiny) surface.
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