KR20020000685A - Method of preparing indium tin oxide(ITO) - Google Patents

Method of preparing indium tin oxide(ITO) Download PDF

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KR20020000685A
KR20020000685A KR1020000035949A KR20000035949A KR20020000685A KR 20020000685 A KR20020000685 A KR 20020000685A KR 1020000035949 A KR1020000035949 A KR 1020000035949A KR 20000035949 A KR20000035949 A KR 20000035949A KR 20020000685 A KR20020000685 A KR 20020000685A
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powder
ito
sno
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precipitate
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최훈
남정규
박상철
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박영구
삼성코닝 주식회사
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    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B35/00Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/622Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/64Burning or sintering processes
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    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B2235/00Aspects relating to ceramic starting mixtures or sintered ceramic products
    • C04B2235/02Composition of constituents of the starting material or of secondary phases of the final product
    • C04B2235/30Constituents and secondary phases not being of a fibrous nature
    • C04B2235/32Metal oxides, mixed metal oxides, or oxide-forming salts thereof, e.g. carbonates, nitrates, (oxy)hydroxides, chlorides
    • C04B2235/3293Tin oxides, stannates or oxide forming salts thereof, e.g. indium tin oxide [ITO]
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    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B35/00Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/01Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics
    • C04B35/453Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics based on zinc, tin, or bismuth oxides or solid solutions thereof with other oxides, e.g. zincates, stannates or bismuthates
    • C04B35/457Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics based on zinc, tin, or bismuth oxides or solid solutions thereof with other oxides, e.g. zincates, stannates or bismuthates based on tin oxides or stannates
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    • C04B35/00Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/622Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/626Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B
    • C04B35/63Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B using additives specially adapted for forming the products, e.g.. binder binders
    • C04B35/632Organic additives

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Abstract

PURPOSE: Provided is a preparation method of indium tin oxide(ITO) of high density sintered body by pre-treating alcohol dispersion treatment in the preparation step of In2O3 and SnO2 powder, and making the fine ITO powder with the diameter of not more than 8nm and controlling precipitating conditions such as concentration, pH and temperature for the solutions containing In and Sn salts in making In2O3 and SnO2. ITO is used in the transparent coating layer of flat display device of LCD, plasma display panel, electric field discharge indicator, electric discharge device and electrodes of solar cell and transparent heat ray. CONSTITUTION: The preparation method comprises: (a) a step of making precipitate at 10-90deg.C under pH 4-10 by introducing a precipitating agent to the solutions containing the salts of In and Sn, wherein the concentration of In salt solution is 0.1-2N and that of Sn salt is 1-2N; (b) a step of aging the precipitate obtained in the above step (a), wherein aging is carried out at 20-100deg.C for In and 20-60deg.C for Sn; (c) a dispersion treating step of the resultant obtained in the above step of (b) with alcohol with C1-C4 at 10-50deg.C; (d) a mixing step of In2O3 and SnO2 powders in a ratio of 85:15-95:5 and making ITO after drying the resultants obtained in the above step of (c) and heat treating at 500-900deg.C.

Description

인듐 틴 옥사이드(ITO)의 제조방법{Method of preparing indium tin oxide(ITO)}Method of preparing indium tin oxide (ITO) {Method of preparing indium tin oxide (ITO)}

본 발명은 인듐 틴 옥사이드(ITO)의 제조방법에 관한 것으로서, 보다 상세하기로는 고밀도 ITO 타겟용 ITO 분말의 제조방법에 관한 것이다.The present invention relates to a method for producing indium tin oxide (ITO), and more particularly to a method for producing ITO powder for high density ITO target.

가시광선에서 광투과도가 커서 투명하고 전기전도도가 큰 ITO 투명도전막은 액정표시장치, 플라즈마 디스플레이 패널, 전계방출표시소자, 전계발광소자 등의 평판표시소자, 태양전지, 투명열선 등의 투명전극에 널리 이용된다. 이러한 투명전극 형성용 물질로는 SnO2, ZnO 등이 사용되며, 그중에서도 In2O3에 SnO2를 첨가한 인듐 틴 옥사이드(ITO)가 널리 이용된다.ITO transparent conductive film that is transparent and has high electric conductivity due to its large light transmittance in visible light is widely used in flat electrodes such as liquid crystal display, plasma display panel, field emission display device, electroluminescent device, transparent electrode such as solar cell and transparent heating wire. Is used. As the material for forming the transparent electrode, SnO 2 , ZnO, or the like is used, and indium tin oxide (ITO) in which SnO 2 is added to In 2 O 3 is widely used.

ITO는 화학양론적인 조성이 맞으면 가시파장 영역에서 투명한 전기절연물질이지만 산소 부족으로 인하여 화학양론적인 조성을 벗어나면 결정내에 자유전자가 생성되어 가시파장영역에서 투명하고 전도성을 갖게 된다. ITO막은 증착법, 스퍼터링법 등으로 제조된 결정질 투명막으로 액정표시용 전극으로 고저항영역(200Ω/? 이상)에서 저저항영역(10Ω/□)까지 폭넓게 사용된다. 이 ITO 박막은 여러가지 박막증착방법에 의하여 제조되는데, 평면 디스플레이의 경우, 대면적의 균일한 박막이 요구되기 때문에 스퍼터링법이 가장 널리 사용된다. 이 스퍼터링법을 이용하기 위해서는 고밀도의 ITO 소결체가 필요하고 이를 위한 많은 개발이 이루어지고 있다.ITO is a transparent electrically insulating material in the visible wavelength region if the stoichiometric composition is correct, but free electrons are generated in the crystal when it is out of the stoichiometric composition due to lack of oxygen, thereby making it transparent and conductive in the visible wavelength region. The ITO film is a crystalline transparent film produced by a vapor deposition method, a sputtering method, or the like, and is used as a liquid crystal display electrode in a wide range from a high resistance region (over 200 Ω /?) To a low resistance region (10 Ω / □). This ITO thin film is manufactured by various thin film deposition methods. In the case of flat panel displays, the sputtering method is most widely used because a large area uniform thin film is required. In order to use this sputtering method, a high-density ITO sintered body is required and many developments have been made for this.

최근 평판표시소자의 디스플레이 화면이 커지고 화면도의 선명도를 높이기 위해서는 저저항의 ITO막이 필요하게 되었다. 이를 달성하기 위해서는 98% 이상의 높은 소결밀도를 갖는 ITO 타겟이 요구되었다. 이러한 고밀도 ITO 타겟을 제조하기 위해서는 미세 ITO 분말 제조, 성형 및 소결 기술의 확립이 필요하다.Recently, in order to increase the display screen of a flat panel display device and to increase the clarity of the screen, an ITO film having a low resistance is required. To achieve this, an ITO target with a high sintered density of at least 98% was required. In order to manufacture such a high density ITO target, it is necessary to establish a fine ITO powder production, molding and sintering technology.

ITO 타겟의 발전과정을 살펴보면, 초기에는 HIP(Hot Isostatic Pressing)등 성형, 소결 기술에 의존하였으나 점차 분말제조기술이 발전하면서 CIP(Cold Isostatic Pressing)등을 이용한 상압소결이 가능해졌다. 이와 같이 상압소결이 가능해진 것은 분말제조공정이 개선된 데서 기인된 것이다. 그리고 분말제조공정의 개선으로 분말의 미세화가 가능해져 1차입경이 100nm 이하까지 가능해졌다. 상기 분말 제조공정에는 전기분해법, 침전법, 스프레이법 등이 이용된다.Looking at the development of the ITO target, the initial dependence on the molding and sintering technology such as hot isostatic pressing (HIP), but gradually advances in powder manufacturing technology, the atmospheric pressure sintering using CIP (cold isostatic pressing) is possible. This atmospheric sintering is possible due to the improved powder manufacturing process. In addition, the refinement of the powder manufacturing process enabled the refinement of the powder, enabling the primary particle size to 100 nm or less. In the powder manufacturing process, an electrolysis method, a precipitation method, a spray method, or the like is used.

미국 특허 공보 제5,700,419호, 일본 공개 특허 공보 평 6-1918416, 평 10-1821150호에 따르면, 침전법을 이용하여 입자의 미세화에 초점을 맞추어 ITO 분말을 제조하였고, 미국 특허 공보 제5,866,493호는 결정화된 ITO 분말을 이용하여 상압 및 산소 분위기 소결에서 고밀도의 ITO 분말을 제조하였다. 그리고 미국 특허 공보 제5,417,816호는 전기분해법을 이용하여 ITO 분말을 제조하였고, 이 분말으로부터 고밀도의 ITO 소결체를 제조하였다.According to U.S. Patent No. 5,700,419, Japanese Laid-Open Patent Publication No. Hei 6-1918416, Hei 10-1821150, an ITO powder was prepared by focusing on miniaturization of particles using the precipitation method, and U.S. Patent No. 5,866,493 was crystallized. The high density ITO powder was prepared under normal pressure and oxygen atmosphere sintering using the prepared ITO powder. And U. S. Patent No. 5,417, 816 prepared ITO powder by electrolysis, and produced high density ITO sintered body from this powder.

상기 특허들에 개시된 내용을 종합해볼 때, 현재까지 알려진 ITO 분말 제조방법은 In-Sn 금속을 HNO3, HCl 등과 같은 산에 용해하여 공침법에 의하여 ITO 분말을 제조하는 방법과, In 금속이나 In 함유 염으로부터 In2O3를 제조하고, 여기에 SnO2분말을 혼합하는 방법으로 분류할 수 있다. 상술한 두가지 방법에 따르면, 모두 ITO 1차 분말의 크기가 100nm 이하로 미세화되었고, 소결밀도도 향상되었다. 그러나, 이러한 미세분말은 입자간의 응집력이 크게 높아져 소결시 불균일한 치밀화와 기공의 형성으로 또 다른 저해요인으로 작용된다.In view of the contents disclosed in the above patents, ITO powder production methods known to date are prepared by dissolving an In-Sn metal in an acid such as HNO 3 , HCl, etc. to prepare ITO powder by coprecipitation method, In metal or In In 2 O 3 can be prepared from the containing salt, and it can be classified by the method of mixing SnO 2 powder thereto. According to the above two methods, the size of the ITO primary powder was refined to 100 nm or less, and the sintered density was also improved. However, such fine powder has a high cohesive force between particles, which acts as another inhibitor of non-uniform densification and formation of pores during sintering.

본 발명이 이루고자 하는 기술적 과제는 상기 문제점을 해결하여 ITO 분말을 보다 미세화시키면서 알콜을 이용한 분산처리로 ITO 입자의 분산성을 높여 고밀도화된 ITO 소결체를 얻을 수 있는 ITO의 제조방법을 제공하는 것이다.The technical problem to be solved by the present invention is to provide a method for producing ITO that can obtain a high-density ITO sintered body by improving the dispersibility of the ITO particles by dispersing with alcohol while making the ITO powder finer by solving the above problems.

상기 기술적 과제를 이루기 위하여 본 발명에서는, (a) In 함유 염 용액과 Sn 함유 염 용액에 침전제를 각각 주입하여 침전물을 형성하는 단계;In order to achieve the above technical problem, in the present invention, the step of forming a precipitate by injecting a precipitant into the In-containing salt solution and Sn-containing salt solution, respectively;

(b) 상기 (a) 단계로부터 얻어진 침전물을 각각 시효처리하는 단계;(b) aging the precipitates obtained from step (a), respectively;

(c) 상기 (b) 단계로부터 얻어진 결과물을 각각 여과한 다음, 분산제에 의하여 분산처리하는 단계; 및(c) filtering the resultant obtained from step (b), and then dispersing with a dispersant; And

(d) 상기 (c)단계로부터 얻은 결과물을 각각 건조한 다음, 이를 열처리하여 In2O3분말과 SnO2분말을 각각 얻고, 이들을 혼합하는 단계;를 포함하는 것을 특징으로 하는 인듐 틴 옥사이드(ITO)의 제조방법을 제공한다.(d) drying the resultant obtained from step (c), and then heat treating them to obtain In 2 O 3 powder and SnO 2 powder, respectively, and mixing them; indium tin oxide (ITO), comprising: It provides a method of manufacturing.

본 발명에 따른 ITO 제조방법은, 상기 (d) 단계로부터 얻은 In2O3분말과 SnO2분말의 혼합물을 성형 및 공기분위기에서 소결하여 ITO 소결체를 얻는 단계를 더 포함하기도 한다. 이 단계를 거치면, In2O3분말 입방(cubic) 구조안에 Sn이 치환되는 과정을 거치게 되어, 보다 고밀도의 ITO 소결체를 얻을 수 있다.The method for producing ITO according to the present invention may further include obtaining the ITO sintered body by sintering a mixture of In 2 O 3 powder and SnO 2 powder obtained from the step (d) in an air atmosphere. Through this step, Sn is substituted in the In 2 O 3 powder cubic structure, thereby obtaining a higher density ITO sintered body.

본 발명은 ITO 분말의 1차 입경을 80nm 이하로 미세화하고 ITO 분말의 소결에 있어서 결정적인 영향을 미치는 SnO2의 분산성을 높여 소결시 In2O3에 SnO2가 치환되는 정도를 높이고 치밀화시 기공의 형성을 막아 ITO 소결체를 고밀도화시킨 데 그 특징이 있다. 또한 알콜을 이용한 분산처리로 ITO 형성용 In2O3및 SnO2분말 입자의 분산성을 높여 일반 대기 분위기하에서도 높은 소결밀도를 갖는 ITO 타겟을 제조하고자 한 것이다.In the present invention, the primary particle size of the ITO powder is refined to 80 nm or less, and the dispersibility of SnO 2 , which has a decisive influence on the sintering of the ITO powder, is increased, thereby increasing the degree of SnO 2 substitution in the In 2 O 3 upon sintering and porosity during densification It is characteristic to make the ITO sintered compact high by preventing the formation of. In addition, to improve the dispersibility of In 2 O 3 and SnO 2 powder particles for forming ITO by dispersing with alcohol to prepare an ITO target having a high sintered density even in a normal atmosphere.

상술한 바와 같이, SnO2분말의 입자 형상은 향후 소결에 큰 영향을 주게 되는데, 이는 In2O3분말의 입방(cubic) 구조안에 Sn이 치환되는 과정이 소결체의 치밀화과정시 함께 일어나기 때문이다. 그리고 SnO2분말의 제조시 침전반응 조건 및 시효 처리 조건은 SnO2분말의 입자 형상에 매우 중요한 영향을 미치므로 소정범위내로 조절하는 것이 바람직하다. 즉, Sn의 경우는 시효처리가 20 내지 60℃에서 이루어지는 것이 바람직하며, Sn 함유 염 수용액의 농도는 1 내지 2N이고, Sn의 침전물은 pH 4 내지 10, 온도 10 내지 90℃에서 형성되는 것이 바람직하다. 그리고 In 함유 염 용액으로부터 침전물을 형성하는 조건은 pH 4 내지 10, 온도가 10 내지 90℃이다. 그리고 In 함유 염 용액의 농도는 0.1 내지 2N인 것이 바람직하다. SnO2가 In2O3에 비하여 제조방법에 따라 소결체의 소결밀도에 큰 영향을 미치는 이유는 소결된 최종 소결체의 경우 In2O3의 입방(cubic) 구조를 갖기 때문에 치밀화와 더불어 In2O3로 치환되는 과정을 동시에 거치기 때문이다.As described above, the particle shape of the SnO 2 powder has a great influence on the sintering in the future, because the process of replacing Sn in the cubic structure of the In 2 O 3 powder occurs during the densification of the sintered body. And precipitation conditions, aging conditions and in the manufacture of a SnO 2 powder is therefore exerts an important effect on the particle shape of the SnO 2 powder is preferably adjusted within a predetermined range. That is, in the case of Sn, it is preferable that the aging treatment is performed at 20 to 60 ° C, the concentration of the aqueous solution containing Sn is 1 to 2N, and the precipitate of Sn is preferably formed at a pH of 4 to 10 and a temperature of 10 to 90 ° C. Do. The conditions for forming a precipitate from the In-containing salt solution are pH 4 to 10, the temperature is 10 to 90 ℃. And it is preferable that the density | concentration of an In containing salt solution is 0.1-2N. SnO 2 is In 2 O 3 on the reason a great influence on the sintered density of the sintered body according to the manufacturing method is In 2 O 3, with compaction since it has a cubic (cubic) structure, in the case of the sintered final sintered In 2 O 3 as compared This is because they go through the process of being replaced by.

이와 같이 상기 범위내로 In 및 Sn의 침전반응 및 시효처리 조건이 제어되면 잘 분산된 미세 SnO2분말은 소결시 In2O3에 잘 치환되고 치밀화시 기공의 발생을 유발하지 않기 때문이다. 만약 침전반응 조건 및 시효 처리 조건이 적절하게 제어되지 않은 경우에는 강한 응집이 일어나 추후분산처리에 의해서도 분산성을 높이는데 한계가 분명히 존재하게 된다.In this way, if the precipitation and aging treatment conditions of In and Sn are controlled within the above range, the finely dispersed fine SnO 2 powder is well substituted with In 2 O 3 upon sintering and does not cause pore generation during densification. If precipitation and aging treatment conditions are not properly controlled, strong agglomeration occurs and there is a clear limit to increase dispersibility even by subsequent dispersion treatment.

본 발명에 따른 ITO 분말의 제조방법을 보다 상세히 설명하면 다음과 같다.Hereinafter, the method for preparing ITO powder according to the present invention will be described in detail.

먼저, In 함유 염 용액과 Sn 함유 염 용액에 침전제를 각각 주입하여 침전물을 형성한다. 여기에서 침전제로는 암모니아수, 탄산암모니아수 등을 사용한다. 이 때 In 함유 염 용액으로는 질산인듐(In(NO3)3)을 물에 용해한 것을 사용하며, In 함유 염 용액으로부터 침전물을 형성하는 조건은 pH 4 내지 10, 온도가 10 내지 90℃이다. 그리고 In 함유 염 용액의 농도는 0.1 내지 2N인 것이 바람직하다. 만약 In 함유 염 용액의 농도가 0.1N 미만인 경우에는 침전량이 너무 적고 2N를 초과하면 침전후 점도가 너무 높아져 균일하게 제조하기가 어려운 단점이 있어서 바람직하지 못하다. 그리고 Sn 함유 염 용액으로는 사염화주석(SnCl4)을 물에 용해한 것을 사용하며, Sn 함유 염 용액으로부터 침전물을 형성하는 조건은 In의 경우와 마찬가지로 pH 4 내지 10, 온도가 10 내지 90℃이다. 그리고 Sn 용액의 농도는 1 내지 2N인 것이 바람직하다. 만약 Sn 함유 염 용액의 농도가 1N 미만인 경우에는 입자간의 응집력이 강해 소결밀도가 떨어지고 2N를 초과하면 침전후 점도가 너무 높아져 균일하게 제조하기가 어려운 단점이 있어서 바람직하지 못하다.First, a precipitant is injected into an In-containing salt solution and a Sn-containing salt solution, respectively, to form a precipitate. Here, ammonia water, ammonia carbonate water, or the like is used as the precipitant. In this case, as the In-containing salt solution, one obtained by dissolving indium nitrate (In (NO 3 ) 3 ) in water is used. The conditions for forming a precipitate from the In-containing salt solution are pH 4 to 10 and a temperature of 10 to 90 ° C. And it is preferable that the density | concentration of an In containing salt solution is 0.1-2N. If the concentration of the In-containing salt solution is less than 0.1N, it is not preferable because the amount of precipitation is too small and if it exceeds 2N, the viscosity is too high after precipitation, making it difficult to prepare uniformly. The Sn-containing salt solution is a solution of tin tetrachloride (SnCl 4 ) dissolved in water. The conditions for forming a precipitate from the Sn-containing salt solution are pH 4 to 10 and a temperature of 10 to 90 ° C. as in the case of In. And it is preferable that the density | concentration of Sn solution is 1-2N. If the concentration of the salt solution containing Sn is less than 1N, the cohesive force between the particles is so strong that the sintered density is lowered, if it exceeds 2N, the viscosity is too high after precipitation is not preferable because it is difficult to produce uniformly.

이어서, 상기 단계로부터 얻어진 침전 분말을 각각 시효처리한다. 이 때 In의 경우는 20 내지 100℃에서 이루어지는 것이 바람직하며, Sn의 경우는 20 내지 60℃에서 이루어지는 것이 바람직하다. 만약 In의 시효처리온도가 상기 범위를 벗어나는 경우에는 침전시 추가적인 온도조절장치, 수열반응장치 등을 설치해야 하고, Sn의 시효처리온도가 20℃ 미만인 경우에는 추가적인 저온 제어 온도 조절장치가 필요하고 60℃를 초과하는 경우에는 입자간의 응집을 초래하므로 바람직하지 못하다.Subsequently, the precipitated powders obtained from the above steps are respectively aged. In this case, In is preferably made at 20 to 100 ° C, and Sn is preferably made at 20 to 60 ° C. If the aging treatment temperature of In is out of the above range, additional temperature control device and hydrothermal reaction device should be installed during precipitation, and if the aging treatment temperature of Sn is less than 20 ℃, an additional low temperature control temperature control device is required. When it exceeds C, since it causes aggregation between particles, it is not preferable.

시효처리가 완결되면, 얻어진 결과물을 각각 여과한 다음, 분산제에 의하여 분산처리하는 단계를 거친다. 이 때 분산제로는 탄소수 1 내지 4의 알콜로서 구체적인 예로는 메탄올, 에탄올 등이 있다. 분산처리시 온도는 10 내지 50℃인 것이 바람직하며, 처리시간은 5 내지 50시간동안 이루어진다. 만약 분산처리온도가 10℃ 미만인 경우에는 온도 조절에 어려움이 있고, 분산처리온도가 50℃를 초과하는 경우에는 알콜이 휘발되므로 바람직하지 못하다.After the aging treatment is completed, the resultant is filtered, and then subjected to a dispersion process with a dispersant. In this case, the dispersant may be an alcohol having 1 to 4 carbon atoms, and specific examples thereof include methanol and ethanol. In the dispersion treatment, the temperature is preferably 10 to 50 ° C., and the processing time is performed for 5 to 50 hours. If the dispersion treatment temperature is less than 10 ℃ difficult to control the temperature, if the dispersion treatment temperature exceeds 50 ℃ alcohol is not preferred because it is volatilized.

그 후, 상기 분산된 결과물을 각각 건조한다. 이 때 건조온도는 70 내지 120℃이다. 이어서, 건조된 결과물을 공기분위기에서 열처리하면 대응하는 산화물인In2O3분말과 SnO2분말을 각각 얻을 수 있다. 이 때 In2O3분말의 1차 입경은 10 내지 80nm이고, SnO2분말의 1차 입경은 10 내지 80nm이다. 이와 같이 ITO 분말의 1차입경은 80nm 이하로서, 종래의 경우에 비하여 보다 미세화된다.Thereafter, the dispersed product is dried. At this time, the drying temperature is 70 to 120 ℃. Subsequently, when the dried product is heat-treated in an air atmosphere, corresponding oxides In 2 O 3 powder and SnO 2 powder may be obtained, respectively. In this case, the primary particle diameter of the In 2 O 3 powder is 10 to 80 nm, the primary particle diameter of the SnO 2 powder is 10 to 80 nm. Thus, the primary particle diameter of ITO powder is 80 nm or less, and it becomes finer compared with the conventional case.

상기 열처리온도는 500 내지 900℃인 것이 바람직하다. 열처리온도가 500℃미만인 경우에는 잔류한 NO3나 Cl이 남아 있게 되고 900℃를 초과하는 경우에는 불균일하고 큰 입자의 생성으로 소결밀도를 저하시키는 문제점이 있다.The heat treatment temperature is preferably 500 to 900 ℃. If the heat treatment temperature is less than 500 ℃ remaining residual NO 3 or Cl and if it exceeds 900 ℃ there is a problem of lowering the sintered density due to the generation of non-uniform and large particles.

상기 In2O3분말과 SnO2분말을 소정혼합비로 혼합하면 본 발명의 ITO 분말이 얻어진다. 이 때 상기 In2O3분말과 SnO2분말의 혼합비는 85:15 내지 95:5 중량비인 것이 바람직하다. 만약 In2O3분말의 함량이 상기 범위를 초과하는 경우에는 전기전도도가 낮아지고, 상기 범위 미만인 경우에는 치환되지 않은 SnO2가 남게 된다.When the In 2 O 3 powder and the SnO 2 powder are mixed at a predetermined mixing ratio, the ITO powder of the present invention is obtained. At this time, the mixing ratio of the In 2 O 3 powder and SnO 2 powder is preferably 85:15 to 95: 5 weight ratio. If the content of In 2 O 3 powder exceeds the above range the electrical conductivity is lowered, if less than the above range is left unsubstituted SnO 2 .

또한, 본 발명의 제조방법에 따르면, 상기 In2O3분말과 SnO2분말의 혼합물을 성형 및 공기분위기에서 소결처리하면 고밀도의 ITO 소결체 즉, ITO 타겟을 얻을 수 있다. 여기에서 소결은 1400 내지 1600℃에서 이루어지며, 이 소결단계에서 In의 입방구조에 Sn이 치환되는 과정이 일어나서 치밀화된다.In addition, according to the manufacturing method of the present invention, when the mixture of the In 2 O 3 powder and SnO 2 powder is molded and sintered in an air atmosphere, a high density ITO sintered body, that is, an ITO target can be obtained. Here, sintering is performed at 1400 to 1600 ° C. In this sintering step, a process of replacing Sn in the cubic structure of In occurs and densifies.

이하, 본 발명을 하기 실시예를 들어 상세하게 설명하기로 하되, 본 발명이 하기 실시예로만 한정되는 것은 아니다.Hereinafter, the present invention will be described in detail with reference to the following examples, but the present invention is not limited only to the following examples.

실시예 1Example 1

1N In(NO3)3용액 150㎖에 침전제 5N NH4OH 70㎖를 주입하여 25℃에서 pH를 5로 조절하여 침전물을 형성한 다음, 80℃에서 400rpm으로 1시간동안 교반하여 시효처리를 실시하였다.70 ml of precipitant 5N NH 4 OH was added to 150 ml of 1N In (NO 3 ) 3 solution to adjust the pH to 5 at 25 ° C. to form a precipitate, followed by aging treatment at 80 ° C. at 400 rpm for 1 hour. It was.

그 후, 상기 반응 혼합물을 여과한 다음, 이를 증류수로 세척하고 얻어진 결과물에 에탄올 100㎖를 부가하여 이를 300rpm으로 교반하면서 30℃, 15시간동안 분산처리하였다. 분산처리과정이 끝나면, 80℃에서, 24시간동안 건조한 다음, 600℃에서 하소하여 In2O3분말을 얻었다. 이 때 In2O3분말의 1차 입경은 20 내지 40nm이었다.Thereafter, the reaction mixture was filtered, washed with distilled water, and 100 ml of ethanol was added to the resultant, which was dispersed at 30 ° C. for 15 hours with stirring at 300 rpm. After the dispersion treatment was completed, dried at 80 ℃ for 24 hours, and then calcined at 600 ℃ to obtain an In 2 O 3 powder. In this case, the primary particle diameter of the In 2 O 3 powder was 20 to 40 nm.

이와 별도로, 1N SnCl4용액 150㎖에 침전제 5N NH4OH 200㎖를 주입하여 25℃에서 pH를 9로 조절하여 침전물을 형성하고 25℃에서 400rpm으로 24시간동안 교반하여 시효처리를 실시하였다.Separately, 200 ml of precipitant 5N NH 4 OH was added to 150 ml of 1N SnCl 4 solution to adjust the pH to 9 at 25 ° C. to form a precipitate, followed by aging treatment at 25 ° C. at 400 rpm for 24 hours.

그 후, 상기 반응 혼합물을 여과한 다음, 이를 증류수로 세척하고 에탄올 100㎖를 부가하고 이를 300rpm으로 교반하면서 30℃에서 15시간동안 분산처리하였다. 분산처리과정이 끝나면, 80℃에서 24시간동안 건조한 다음, 600℃에서 하소하여 SnO2분말을 얻었다. 이 때 SnO2분말의 1차 입경은 20 내지 40nm이었다.Thereafter, the reaction mixture was filtered and then washed with distilled water, and 100 ml of ethanol was added thereto, and the mixture was dispersed for 15 hours at 30 ° C. while stirring at 300 rpm. After the dispersion treatment was completed, dried at 80 ℃ for 24 hours, and then calcined at 600 ℃ to obtain a SnO 2 powder. At this time, the primary particle diameter of the SnO 2 powder was 20 to 40 nm.

상기 과정에 따라 제조된 In2O3분말과 SnO2분말을 9:1 무게비로 혼합하고 CIP를 이용하여 3ton/㎠의 압력으로 성형하고 이를 5℃/min의 승온속도로 1500℃까지 가열한 다음, 이 온도에서 2시간동안 공기분위기에서 소결하여 ITO 소결체를 얻었다.The In 2 O 3 powder and SnO 2 powder prepared according to the above process were mixed at a weight ratio of 9: 1, and molded at a pressure of 3 ton / cm 2 using CIP, and heated to 1500 ° C. at a temperature rising rate of 5 ° C./min. At this temperature, the mixture was sintered in an air atmosphere for 2 hours to obtain an ITO sintered body.

실시예 2Example 2

후술하는 사항을 제외하고는, 실시예 1과 동일한 방법에 따라 실시하여 ITO 소결체를 얻었다.Except the matter mentioned later, it carried out according to the same method as Example 1, and obtained the ITO sintered compact.

In 공급원으로서 1N In(NO3)3대신 0.5N In(NO3)3를 사용하고, In 용액 및 Sn 용액으로부터 침전물 형성시 온도는 25℃로 최종 pH는 9로 조절하였다. 그리고 시효처리에 있어서, In 용액의 경우는 80℃에서 400rpm으로 교반하면서 24시간동안 유지하였고, Sn 용액의 경우는 25℃에서 실시하는 것을 제외한 나머지 과정은, In 용액의 경우와 동일하게 시효처리하였다. 단, In2O3의 하소온도는 700℃이었다. 이 때 In2O3분말의 1차 입경은 30 내지 50nm이었고, SnO2분말의 1차 입경은 20 내지 40nm이었다.0.5N In (NO 3 ) 3 was used instead of 1N In (NO 3 ) 3 as the In source, and the temperature was adjusted to 25 ° C. and the final pH was 9 when forming precipitates from the In and Sn solutions. In the aging treatment, the In solution was maintained for 24 hours with stirring at 400 rpm at 80 ° C., and the Sn process was aged in the same manner as in the In solution except for 25 ° C. . However, the calcining temperature of In 2 O 3 was 700 ° C. At this time, the primary particle diameter of the In 2 O 3 powder was 30 to 50 nm, the primary particle diameter of the SnO 2 powder was 20 to 40 nm.

실시예 3Example 3

후술하는 사항을 제외하고는, 실시예 1과 동일한 방법에 따라 실시하여 ITO 소결체를 얻었다.Except the matter mentioned later, it carried out according to the same method as Example 1, and obtained the ITO sintered compact.

In 용액 및 Sn 용액으로부터 침전물 형성시, 온도는 25℃에서 최종 pH는 9로 조절하였다. 그리고 In, Sn 용액의 경우 모두 시효처리는 25℃에서 400rpm으로 24시간동안 교반함으로써 실시하였다. 그리고 In 용액과 Sn 용액의 시효처리를 상기한 바와 같이 실시한 다음, 각각의 반응 혼합물을 여과한 다음, 이를 증류수로 세척하고 에탄올 100㎖를 부가하고, 그 결과물을 300rpm으로 혼합하면서 30℃에서 15시간동안 분산처리하였다. 분산처리과정이 끝나면, 80℃에서, 24시간동안 건조한 다음, 600℃에서 하소하여 In2O3분말과 SnO2분말을 각각 얻었다. 이 때 In2O3분말의 1차 입경은 20 내지 40nm이었고, SnO2분말의 1차 입경은 20 내지 40nm이었다.Upon precipitate formation from In and Sn solutions, the temperature was adjusted to 25 at < RTI ID = 0.0 > 25 C. < / RTI > In the case of both In and Sn solutions, the aging treatment was performed by stirring at 25 ° C. at 400 rpm for 24 hours. After the aging treatment of the In solution and the Sn solution was carried out as described above, each reaction mixture was filtered, washed with distilled water, and 100 ml of ethanol was added, and the resultant was mixed at 300 rpm for 15 hours at 30 ° C. During the dispersion. After the dispersion treatment was completed, dried at 80 ℃ for 24 hours, and then calcined at 600 ℃ to obtain In 2 O 3 powder and SnO 2 powder, respectively. At this time, the primary particle diameter of the In 2 O 3 powder was 20 to 40 nm, the primary particle diameter of the SnO 2 powder was 20 to 40 nm.

비교예 1Comparative Example 1

1N In(NO3)3용액 150㎖에 5N NH4OH 70㎖를 주입하여 25℃에서 pH를 9로 조절하여 침전물을 형성하였다.70 ml of 5N NH 4 OH was injected into 150 ml of 1N In (NO 3 ) 3 solution to adjust the pH to 9 at 25 ° C. to form a precipitate.

그 후, 상기 반응 혼합물을 여과한 다음, 이를 증류수로 세척하고 최종 여과시 세척액으로 에탄올을 사용하였다. 여과과정이 끝나면, 상기 결과물을 80℃에서 24시간동안 건조한 다음, 600℃에서 하소하여 In2O3분말을 얻었다. 이 때 In2O3분말의 1차 입경은 20 내지 40nm이었다.Thereafter, the reaction mixture was filtered and then washed with distilled water and ethanol was used as a washing solution in the final filtration. After the filtration process, the resultant was dried for 24 hours at 80 ℃ and calcined at 600 ℃ to obtain an In 2 O 3 powder. In this case, the primary particle diameter of the In 2 O 3 powder was 20 to 40 nm.

이와 별도로, 1N SnCl4용액 150㎖에 녹인 다음, 여기에 침전제 5N NH4OH 140㎖를 주입하여 25℃에서 pH를 5로 조절하여 침전물을 형성하였다.Separately, it was dissolved in 150 ml of 1N SnCl 4 solution, and then, 140 ml of precipitant 5N NH 4 OH was added thereto to adjust the pH to 5 at 25 ° C. to form a precipitate.

그 후, 상기 반응 혼합물을 여과한 다음, 이를 증류수로 세척하고 최종 여과시 세척액으로서 에탄올을 사용하였다. 여과과정이 끝나면, 얻어진 결과물을 80℃에서 24시간동안 건조한 다음, 600℃에서 하소하여 SnO2분말을 얻었다. 이 때 SnO2분말의 1차 입경은 20 내지 40nm이었다.Thereafter, the reaction mixture was filtered and then washed with distilled water and ethanol was used as a washing solution in the final filtration. After the filtration process, the resultant was dried for 24 hours at 80 ℃ and calcined at 600 ℃ to obtain a SnO 2 powder. At this time, the primary particle diameter of the SnO 2 powder was 20 to 40 nm.

상기 과정에 따라 제조된 In2O3분말과 SnO2분말을 9:1 무게비로 혼합하고 CIP를 이용하여 3ton/㎠의 압력으로 성형하고 이를 5℃/min의 승온속도로 1500℃까지 가열한 다음, 이 온도에서 2시간동안 공기분위기에서 소결하여 ITO 소결체를 얻었다.The In 2 O 3 powder and SnO 2 powder prepared according to the above process were mixed at a weight ratio of 9: 1, and molded at a pressure of 3 ton / cm 2 using CIP, and heated to 1500 ° C. at a temperature rising rate of 5 ° C./min. At this temperature, the mixture was sintered in an air atmosphere for 2 hours to obtain an ITO sintered body.

비교예 2Comparative Example 2

1N In(NO3)3용액 150㎖에 침전제 5N NH4OH 70㎖를 주입하고 25℃에서 pH를 5로 조절하여 침전물을 형성하고, 이 결과물을 25℃에서 400rpm으로 24시간동안 교반하여 시효(aging) 처리를 실시하였다.70 ml of precipitant 5N NH 4 OH was added to 150 ml of 1N In (NO 3 ) 3 solution, and the pH was adjusted to 5 at 25 ° C. to form a precipitate, and the resultant was stirred for 24 hours at 400 rpm at 25 ° C. aging) treatment.

그 후, 상기 반응 혼합물을 여과한 다음, 이를 증류수로 세척하고 최종 여과시 세척액으로서 에탄올을 이용하였다. 여과가 끝나면, 얻어진 결과물을 80℃에서 24시간동안 건조하였고, 600℃에서 하소하여 In2O3분말을 얻었다. 이 때 In2O3분말의 1차 입경은 20 내지 40nm이었다.Thereafter, the reaction mixture was filtered and then washed with distilled water and ethanol was used as a washing solution in the final filtration. After filtration, the resultant was dried at 80 ° C. for 24 hours and calcined at 600 ° C. to obtain an In 2 O 3 powder. In this case, the primary particle diameter of the In 2 O 3 powder was 20 to 40 nm.

이와 별도로, 1N SnCl4용액 150㎖에 침전제 5N NH4OH 200㎖를 주입하여 25℃에서 pH를 9로 조절하여 침전물을 형성하였고, 이 결과물을 25℃에서 400rpm으로 24시간동안 교반하여 시효처리를 실시하였다.Separately, 200 ml of precipitant 5N NH 4 OH was added to 150 ml of 1N SnCl 4 solution to adjust the pH to 9 at 25 ° C. to form a precipitate, and the resultant was stirred for 24 hours at 400 ° C. at 25 ° C. for aging treatment. Was carried out.

그 후, 상기 반응 혼합물을 여과한 다음, 이를 증류수로 세척하고 최종 여과시 세척액으로서 에탄올을 이용00하여 세척하였다. 여과가 끝나면, 얻어진 결과물을 80℃에서, 24시간동안 건조한 다음, 600℃에서 하소하여 SnO2분말을 얻었다. 이 때 SnO2분말의 1차 입경은 20 내지 40nm이었다.Thereafter, the reaction mixture was filtered and then washed with distilled water and washed with ethanol as a washing solution in the final filtration. After filtration, the resultant was dried at 80 ° C. for 24 hours and then calcined at 600 ° C. to obtain a SnO 2 powder. At this time, the primary particle diameter of the SnO 2 powder was 20 to 40 nm.

상기 과정에 따라 제조된 In2O3분말과 SnO2분말을 9:1 무게비로 혼합하고 CIP를 이용하여 3ton/㎠의 압력으로 성형하고 이를 5℃/min의 승온속도로 1500℃까지 가열한 다음, 이 온도에서 2시간동안 공기분위기에서 소결하여 ITO 소결체를 얻었다.The In 2 O 3 powder and SnO 2 powder prepared according to the above process were mixed at a weight ratio of 9: 1, and molded at a pressure of 3 ton / cm 2 using CIP, and heated to 1500 ° C. at a temperature rising rate of 5 ° C./min. At this temperature, the mixture was sintered in an air atmosphere for 2 hours to obtain an ITO sintered body.

비교예 3Comparative Example 3

1N In(NO3)3용액 150㎖에 침전제 5N NH4OH 145㎖를 주입하여 25℃에서 pH를 9로 조절하여 침전물을 형성하였고, 이 결과물을 25℃에서 400rpm으로 24시간동안 교반함으로써 시효(aging) 처리를 실시하였다.145 ml of precipitant 5N NH 4 OH was added to 150 ml of 1N In (NO 3 ) 3 solution to adjust the pH to 9 at 25 ° C. to form a precipitate, and the resultant was aged by stirring at 400 ° C. at 25 ° C. for 24 hours. aging) treatment.

그 후, 상기 반응 혼합물을 여과한 다음, 이를 증류수로 세척하고 에탄올 100㎖를 부가하고 이 결과물을 300rpm으로 혼합하면서 30℃에서 15시간동안 분산처리하였다. 분산처리가 끝난 후, 얻어진 결과물을 80℃에서 24시간동안 건조하였고, 600℃에서 하소하여 In2O3분말을 얻었다. 이 때 In2O3분말의 1차 입경은 20 내지 40nm이었다.Thereafter, the reaction mixture was filtered, washed with distilled water, and 100 ml of ethanol was added, and the resultant was dispersed for 15 hours at 30 DEG C while mixing at 300 rpm. After the dispersion treatment was completed, the resultant was dried at 80 ° C. for 24 hours and calcined at 600 ° C. to obtain an In 2 O 3 powder. In this case, the primary particle diameter of the In 2 O 3 powder was 20 to 40 nm.

이와 별도로, 1N SnCl4용액 150㎖에 침전제 5N NH4OH 200㎖를 주입하여 25℃에서 pH를 9로 조절하여 침전물을 형성하였고, 이 결과물을 80℃에서 400rpm으로 24시간동안 교반함으로써 시효처리를 실시하였다.Separately, 200 ml of precipitant 5N NH 4 OH was added to 150 ml of 1N SnCl 4 solution to adjust the pH to 9 at 25 ° C. to form a precipitate, and the resultant was stirred for 24 hours at 80 ° C. at 400 rpm for 24 hours. Was carried out.

그 후, 상기 반응 혼합물을 여과한 다음, 이를 증류수로 세척하고 에탄올 100㎖를 부가하고, 이 결과물을 300rpm으로 혼합하면서 30℃에서 15시간동안 분산처리하였다. 분산처리가 끝난 후, 얻어진 결과물을 80℃에서 24시간동안 건조하였고, 800℃에서 하소하여 SnO2분말을 얻었다. 이 때 SnO2분말의 1차 입경은 60 내지 80nm이었다.Thereafter, the reaction mixture was filtered, washed with distilled water, and 100 ml of ethanol was added, and the resultant was dispersed for 15 hours at 30 DEG C while mixing at 300 rpm. After the dispersion treatment was completed, the resultant was dried at 80 ° C. for 24 hours and calcined at 800 ° C. to obtain a SnO 2 powder. At this time, the primary particle diameter of the SnO 2 powder was 60 to 80 nm.

상기 과정에 따라 제조된 In2O3분말과 SnO2분말을 9:1 무게비로 혼합하고CIP를 이용하여 3ton/㎠의 압력으로 성형하고 이를 5℃/min의 승온속도로 1500℃까지 가열한 다음, 이 온도에서 2시간동안 공기분위기에서 소결하여 ITO 소결체를 얻었다.The In 2 O 3 powder and SnO 2 powder prepared according to the above process are mixed at a weight ratio of 9: 1, and molded using a CIP at a pressure of 3 ton / cm 2 and heated to 1500 ° C. at a temperature rising rate of 5 ° C./min. At this temperature, the mixture was sintered in an air atmosphere for 2 hours to obtain an ITO sintered body.

비교예 4Comparative Example 4

1N In(NO3)3용액 150㎖에 침전제 5N NH4OH 145㎖를 주입하여 25℃에서, pH를 9로 조절하여 침전물을 형성하였고, 이 결과물을 400rpm으로 1시간동안 교반하면서 25℃에서 24시간을 유지하여 시효(aging) 처리를 실시하였다.145 ml of precipitant 5N NH 4 OH was injected into 150 ml of 1N In (NO 3 ) 3 solution, and the precipitate was formed at 25 ° C. by adjusting the pH to 9, and the resultant was stirred at 400 rpm for 1 hour at 24 ° C. at 24 ° C. The aging treatment was performed while keeping the time.

그 후, 상기 반응 혼합물을 여과한 다음, 이를 증류수로 세척하고 에탄올을 부가하고, 이를 300rpm으로 혼합하면서 30℃에서 15시간동안 분산처리하였다. 분산처리가 끝난 후, 얻어진 결과물을 80℃에서 24시간동안 건조하였고, 600℃에서 하소하여 In2O3분말을 얻었다. 이 때 In2O3분말의 1차 입경은 20 내지 40nm이었다.Thereafter, the reaction mixture was filtered, washed with distilled water and ethanol was added, and the mixture was dispersed for 15 hours at 30 ° C. while mixing at 300 rpm. After the dispersion treatment was completed, the resultant was dried at 80 ° C. for 24 hours and calcined at 600 ° C. to obtain an In 2 O 3 powder. In this case, the primary particle diameter of the In 2 O 3 powder was 20 to 40 nm.

이와 별도로, 0.5N SnCl4용액 150㎖에 침전제 5N NH4OH 100㎖를 주입하여 25℃에서 pH를 9로 조절하여 침전물을 형성하였고 80℃에서 400rpm으로 24시간동안 교반하여 시효처리를 실시하였다.Separately, 150 ml of 0.5 N SnCl 4 solution was injected with 100 ml of precipitant 5N NH 4 OH to adjust pH to 9 at 25 ° C. to form a precipitate. Aging was performed by stirring at 400 rpm at 80 ° C. for 24 hours.

그 후, 상기 반응 혼합물을 여과한 다음, 이를 증류수로 세척하고 에탄올을 부가하고, 이 결과물을 300rpm으로 혼합하면서 30℃에서 15시간동안 분산처리하였다. 분산처리가 끝난 후, 얻어진 결과물을 80℃에서 24시간동안 건조하였고, 600℃에서 하소하여 SnO2분말을 얻었다. 이 때 SnO2분말의 1차 입경은 30 내지 50nm이었다.Thereafter, the reaction mixture was filtered, washed with distilled water and ethanol was added, and the resultant was dispersed for 15 hours at 30 DEG C while mixing at 300 rpm. After the dispersion treatment was completed, the resultant was dried at 80 ° C. for 24 hours and calcined at 600 ° C. to obtain a SnO 2 powder. At this time, the primary particle diameter of the SnO 2 powder was 30 to 50 nm.

상기 과정에 따라 제조된 In2O3분말과 SnO2분말을 9:1 무게비로 혼합하고 CIP를 이용하여 3ton/㎠의 압력으로 성형하고 이를 5℃/min의 승온속도로 1500℃까지 가열한 다음, 이 온도에서 2시간동안 공기분위기에서 소결하여 ITO 소결체를 얻었다.The In 2 O 3 powder and SnO 2 powder prepared according to the above process were mixed at a weight ratio of 9: 1, and molded at a pressure of 3 ton / cm 2 using CIP, and heated to 1500 ° C. at a temperature rising rate of 5 ° C./min. At this temperature, the mixture was sintered in an air atmosphere for 2 hours to obtain an ITO sintered body.

상기 실시예 1 내지 3에 따르면, 25℃ 또는 80℃에서 400rpm으로 교반을 하면서 1시간 또는 24시간동안 유지함으로써 시효처리를 실시하였다. 그리고 여과후, 에탄올을 이용하여 30℃, 15시간동안 분산처리로 분말사이의 분산성을 높였다.According to Examples 1 to 3, the aging treatment was performed by maintaining for 1 hour or 24 hours while stirring at 400 rpm at 25 ° C or 80 ° C. After filtration, dispersibility between powders was increased by dispersing for 15 hours at 30 ° C. using ethanol.

이에 반하여, 비교예 1의 경우는 시효처리와 알콜 분산처리를 모두 실시하지 않았고, 비교예 2의 경우는 반응 혼합물을 400rpm으로 교반을 하면서 24시간동안 유지함으로써 시효처리를 실시하면서 알콜 분산처리는 실시하지 않았다. 그리고 비교예 3 및 4의 경우는 시효처리와 알콜 분산처리를 모두 실시하였으나, 비교예 3의 경우는 Sn의 경우 시효처리시 온도가 80℃로 높았고, Sn 함유 염 용액의 초기농도가 0.5N로 낮았다.On the contrary, in Comparative Example 1, neither the aging treatment nor the alcohol dispersion treatment was performed. In the case of Comparative Example 2, the alcohol dispersion treatment was performed while the aging treatment was carried out by maintaining the reaction mixture for 24 hours with stirring at 400 rpm. Did not do it. In Comparative Examples 3 and 4, both the aging treatment and the alcohol dispersion treatment were performed. In Comparative Example 3, the temperature of Sn was high at 80 ° C., and the initial concentration of the Sn-containing salt solution was 0.5N. Low.

상기 실시예 1 내지 3 및 비교예 1 내지 4에 따라 제조된 ITO 소결체의 밀도를 측정하였다.The densities of the ITO sintered bodies prepared according to Examples 1 to 3 and Comparative Examples 1 to 4 were measured.

측정 결과, 실시예 1의 ITO 소결체의 밀도는 이론밀도 대비 98.36%이고, 실시예 2의 ITO 소결체의 밀도는 이론밀도 대비 98.12%이고, 실시예 3의 ITO 소결체의 밀도는 이론밀도 대비 97.4%이고, 비교예 1의 ITO 소결체의 밀도는 이론 밀도 대비 84%이고, 비교예 2의 ITO 소결체의 밀도는 이론밀도 대비 92%이고, 비교예 3의 ITO 소결체의 밀도는 이론밀도 대비 93%이고, 비교예 4의 ITO 소결체의 밀도는이론밀도 대비 86%이다.As a result of the measurement, the density of the ITO sintered compact of Example 1 was 98.36% compared with the theoretical density, the density of the ITO sintered compact of Example 2 was 98.12% compared with the theoretical density, and the density of the ITO sintered compact of Example 3 was 97.4% compared with the theoretical density , The density of the ITO sintered compact of Comparative Example 1 is 84% of the theoretical density, the density of the ITO sintered compact of Comparative Example 2 is 92% of the theoretical density, the density of the ITO sintered compact of Comparative Example 3 is 93% of the theoretical density, The density | concentration of the ITO sintered compact of Example 4 is 86% with respect to theoretical density.

이상의 결과로부터, 특히 실시예들과 비교예 1 및 2의 결과를 비교해보면 시효처리와 알콜분산처리가 ITO 소결체의 밀도를 높이는 데 효과가 확실하다는 것을 알 수 있었다. 그러나, 비교예 3 및 4의 경우, 시효처리와 알콜분산처리를 모두 실시한다고 하더라도 SnO2의 제조조건에 따라서 특히 SnO2의 제조과정중 시효온도가 80℃로 높은 경우 초기농도가 0.5로 낮아진 경우 ITO 소결체의 소결밀도가 급격하게 낮아진다는 것을 확인할 수 있었다. 이는 SnO2의 경우, 초기에 응집되면 분산처리에 의해서도 입자의 분산성을 높일 수 없음을 알 수 있었다. 따라서 SnO2의 경우 실시예 1-3의 경우처럼 침전시 Sn의 농도를 1 내지 2N로 조절하고 시효처리의 경우도 20 내지 60℃ 범위로 제어해야 저온에서 초기 입자들의 응집을 막고 최종 분산처리로 하소 과정에서의 고분산 ITO 분말을 제조할 수 있었다.From the above results, in particular, when comparing the results of Examples and Comparative Examples 1 and 2, it was found that the aging treatment and the alcohol dispersion treatment were effective in increasing the density of the ITO sintered compact. However, in Comparative Examples 3 and 4 In the case of, for aging treatment and even if carried out all the alcohol dispersion treatment according to the manufacturing conditions of the SnO 2 is particularly the case for manufacturing the aging temperature of the SnO 2 as high as 80 ℃ when the initial concentration lowered to 0.5 It was confirmed that the sintered density of the ITO sintered compact was sharply lowered. It was found that, in the case of SnO 2 , the dispersibility of the particles could not be increased even by dispersing when initially aggregated. Therefore, in the case of SnO 2 , the concentration of Sn should be controlled to 1 to 2N during precipitation as in the case of Example 1-3, and the aging treatment should also be controlled to be in the range of 20 to 60 ° C. Highly dispersed ITO powder in the calcination process could be prepared.

본 발명에 따르면, ITO 분말의 1차 입경을 80nm 이하로 미세화시키고 In2O3와 SnO2의 제조시 In 함유 염 용액과 Sn 함유 염 용액의 농도, pH, 온도 등과 같은 침전물 형성 조건과 시효처리 조건을 적정 범위내로 제어함으로써 소결시 In2O3의 입방구조안에 Sn이 치환되는 정도를 높여서 치밀화시 기공의 형성을 막고, In2O3분말과 SnO2분말의 제조시 여과후 건조전 알콜 분산처리를 거침으로써 고밀도화된 ITO 소결체를 얻을 수 있다.According to the present invention, the primary particle size of the ITO powder is refined to 80 nm or less, and precipitation conditions and aging treatments such as concentration, pH, and temperature of the In-containing salt solution and the Sn-containing salt solution are prepared in the preparation of In 2 O 3 and SnO 2 . By controlling the conditions within an appropriate range, the degree of Sn substitution in the cubic structure of In 2 O 3 during sintering is increased to prevent the formation of pores during densification, and the alcohol dispersion before drying after filtration during preparation of In 2 O 3 powder and SnO 2 powder By the treatment, a densified ITO sintered body can be obtained.

Claims (9)

(a) In 함유 염 용액과 Sn 함유 염 용액에 침전제를 각각 주입하여 침전물을 형성하는 단계;(a) injecting a precipitant into the In-containing salt solution and the Sn-containing salt solution, respectively, to form a precipitate; (b) 상기 (a) 단계로부터 얻어진 침전물을 각각 시효처리(aging)하는 단계;(b) aging the precipitates obtained from step (a), respectively; (c) 상기 (b) 단계로부터 얻어진 결과물을 각각 여과한 다음, 분산제에 의하여 분산처리하는 단계; 및(c) filtering the resultant obtained from step (b), and then dispersing with a dispersant; And (d) 상기 (c)단계로부터 얻은 결과물을 각각 건조한 다음, 이를 열처리하여 In2O3분말과 SnO2분말을 각각 얻고, 이들을 혼합하는 단계;를 포함하는 것을 특징으로 하는 인듐 틴 옥사이드(ITO)의 제조방법.(d) drying the resultant obtained from step (c), and then heat treating them to obtain In 2 O 3 powder and SnO 2 powder, respectively, and mixing them; indium tin oxide (ITO), comprising: Manufacturing method. 제1항에 있어서, 상기 (d) 단계로부터 얻은 In2O3분말과 SnO2분말의 혼합물을 성형 및 공기분위기에서 소결하여 ITO 소결체를 얻는 단계를 더 포함하는 것을 특징으로 하는 방법.The method of claim 1, further comprising the step of sintering the mixture of In 2 O 3 powder and SnO 2 powder obtained from the step (d) in a molding and air atmosphere to obtain an ITO sintered body. 제1항에 있어서, 상기 (d) 단계에서 In2O3분말과 SnO2분말의 혼합중량비가 85:15 내지 95:5인 것을 특징으로 하는 방법.The method of claim 1, wherein the mixed weight ratio of In 2 O 3 powder and SnO 2 powder in step (d) is 85:15 to 95: 5. 제1항에 있어서, 상기 (d) 단계에서 소결온도가 1400 내지 1600℃인 것을 특징으로 하는 방법.The method of claim 1, wherein the sintering temperature in the step (d) is 1400 to 1600 ℃. 제1항 또는 제2항에 있어서, 상기 (b) 단계에서, In의 경우는 시효처리가 20 내지 100℃에서 이루어지고, Sn의 경우는 시효처리가 20 내지 60℃에서 이루어지는 것을 특징으로 하는 방법.The method according to claim 1 or 2, wherein in step (b), in the case of In, the aging treatment is performed at 20 to 100 ° C, and in the case of Sn, the aging treatment is performed at 20 to 60 ° C. . 제1항 또는 제2항에 있어서, 상기 (c) 단계의 분산제가 탄소수 1 내지 4의 알콜이고 분산처리가 10 내지 50℃에서 이루어지는 것을 특징으로 하는 방법.The method according to claim 1 or 2, wherein the dispersing agent of step (c) is an alcohol having 1 to 4 carbon atoms and the dispersing treatment is performed at 10 to 50 ° C. 제1항 또는 제2항에 있어서, 상기 (d)의 열처리온도가 500 내지 900℃에서 이루어지는 것을 특징으로 하는 방법.The method according to claim 1 or 2, wherein the heat treatment temperature of (d) is performed at 500 to 900 ° C. 제1항 또는 제2항에 있어서, 상기 (a) 단계의 In 함유 염 용액의 농도가 0.1 내지 2N이고, Sn 함유 염 용액의 농도가 1 내지 2N이고,According to claim 1 or 2, wherein the concentration of the In-containing salt solution of the step (a) is 0.1 to 2N, the concentration of the Sn-containing salt solution is 1 to 2N, In 및 Sn의 침전물이 pH 4 내지 10, 온도 10 내지 90℃에서 형성되는 것을 특징으로 하는 방법.The precipitate of In and Sn is formed at pH 4-10, temperature 10-90 degreeC. 제1항에 있어서, 상기 (d) 단계에서 얻은 In2O3분말과 SnO2분말의 1차 입경이 80nm 이하인 것을 특징으로 하는 방법.The method of claim 1, wherein the primary particle diameter of the In 2 O 3 powder and SnO 2 powder obtained in the step (d) is 80nm or less.
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