JP4895013B2 - Indium recovery method - Google Patents
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Description
本発明は、塩化インジウム溶液からスポンジ状の金属インジウムを効率よく析出させるインジウムを回収する方法に関する。 The present invention relates to a method for recovering indium that efficiently deposits spongy metallic indium from an indium chloride solution.
インジウム−錫酸化物(ITO)薄膜が半導体材料として広く使用されており、この薄膜は一般にスパッタリング法によって形成されている。このスパッタリングのターゲット材としてITO高密度焼結体が用いられており、使用済みターゲット材として多量のITOスクラップが生じている。ITO焼結には高純度の材料が使用されており、価格も高いので、このようなスクラップ材からインジウムを回収することが行われている。このインジウム回収方法として、ITOスクラップを塩酸に溶解し、該溶解液に水酸化ナトリウムを添加して液中のスズを水酸化スズ沈澱にして分離した後に、インジウムを回収する方法が知られている(特許文献1、2、3)。 An indium-tin oxide (ITO) thin film is widely used as a semiconductor material, and this thin film is generally formed by a sputtering method. An ITO high-density sintered body is used as a sputtering target material, and a large amount of ITO scrap is generated as a used target material. Since high-purity materials are used for ITO sintering and the price is high, indium is recovered from such scrap materials. As this indium recovery method, a method of recovering indium after dissolving ITO scrap in hydrochloric acid, adding sodium hydroxide to the solution to separate and separate tin in the solution by tin hydroxide precipitation is known. (Patent Documents 1, 2, and 3).
従来の上記インジウム回収方法は、電解採取によって金属インジウムを回収する方法と、置換析出によってスポンジインジウムを回収する方法とが知られている。電解採取法は、液中のスズを水酸化スズ沈澱にして分離した塩化インジウム液のpHを調整して水酸化インジウムを沈澱させ、これを濾過回収して硫酸に溶解し、この硫酸インジウム溶液を電解して金属インジウムを採取する方法であり、塩化インジウム溶液のpHを中性(pH5〜6)に調整して水酸化インジウムを沈澱させる方法(特許文献1)、塩化インジウム溶液のpHをアルカリ性(pH7〜9)に調整して水酸化インジウムを凝集させて沈澱させる方法(特許文献2)が知られている。
スポンジインジウムの回収方法は、水酸化スズを除去した塩化インジウム溶液に亜鉛を添加してスポンジ状の金属インジウムを置換析出させる方法である(特許文献3)。
As the conventional indium recovery method, there are known a method of recovering metal indium by electrowinning and a method of recovering sponge indium by displacement deposition. In the electrowinning method, the pH of the indium chloride solution separated from tin in the solution by precipitation with tin hydroxide is adjusted to precipitate indium hydroxide, which is recovered by filtration and dissolved in sulfuric acid. It is a method of collecting metal indium by electrolysis, a method of adjusting the pH of the indium chloride solution to neutral (pH 5-6) to precipitate indium hydroxide (Patent Document 1), and adjusting the pH of the indium chloride solution to alkaline ( A method (Patent Document 2) in which indium hydroxide is aggregated and precipitated by adjusting the pH to 7-9) is known.
A method for recovering sponge indium is a method in which zinc is added to an indium chloride solution from which tin hydroxide has been removed to displace and deposit sponge-like metal indium (Patent Document 3).
従来の上記インジウム回収方法において、水酸化インジウムを沈澱させて濾別する方法はこの沈澱の濾過性が悪く、また回収した水酸化インジウムを硫酸に溶解して電解する工程が続き、処理工程が煩雑である。 In the conventional method for recovering indium, the method of precipitating indium hydroxide and filtering it out is poor in filterability of the precipitate, and the process of dissolving the recovered indium hydroxide in sulfuric acid followed by electrolysis is complicated. It is.
一方、置換析出によってスポンジインジウムを析出させる従来のインジウム回収方法は、液中のインジウム濃度48.6g/L程度とし、溶液のpHを1.5〜2.5に調整することによって水酸化インジウム沈澱が生じないようにしてインジウムを析出させているが、インジウムイオン濃度を高めると、亜鉛板の表面に薄いインジウム膜が生じて亜鉛の溶出が妨げられ、亜鉛とインジウムの置換反応の阻害されるため、セメンテーションが進行しなくなると云う問題がある。
本発明は、スポンジインジウムを回収する方法において、従来の上記問題を解決したものであり、従来の方法とは異なり、液中に遊離のインジウムイオンと共に積極的に水酸化インジウムを共存させることによって、セメンテーションが円滑に進行するようにし、安定にスポンジインジウムを析出させることができるインジウムの回収方法を提供する。 The present invention solves the above-mentioned conventional problems in a method for recovering sponge indium, and unlike conventional methods, by actively allowing indium hydroxide to coexist with free indium ions in the liquid, Provided is a method for recovering indium that allows cementation to proceed smoothly and allows sponge indium to be deposited stably.
本発明によれば、以下の構成によって上記課題を解決したインジウムの回収方法が提供される。
(1)塩化インジウム溶液に亜鉛を添加して金属インジウムを析出させる工程において、液中にインジウムイオンと水酸化インジウムを共存させて金属インジウムを析出させることを特徴とするインジウムの回収方法。
(2)塩化インジウム溶液に亜鉛を添加して金属インジウムを析出させる工程において、液中にインジウムイオンと水酸化インジウムを共存させ、液中のインジウムイオン濃度を60〜85g/Lとして、金属インジウムを析出させる上記(1)に記載するインジウムの回収方法。
(3)上記(1)または上記(2)の方法において、塩化インジウム溶液のpHを2.5〜3.5に調整して水酸化インジウムを生成させ、インジウムイオンと水酸化インジウムを共存させて金属インジウムを析出させるインジウムの回収方法。
(4)塩化インジウム溶液中のインジウムイオン初期濃度60〜85g/L、初期の水酸化インジウム量(In換算)5〜60g/L(合計インジウム濃度90〜120g/L)の濃度範囲で金属インジウムを析出させる上記(1)〜上記(3)の何れかに記載するインジウムの回収方法。
According to the present invention, a method for recovering indium that solves the above-described problems is provided by the following configuration.
(1) A method for recovering indium characterized in that in the step of depositing metal indium by adding zinc to an indium chloride solution, indium ions and indium hydroxide coexist in the solution to deposit metal indium.
(2) In the step of adding zinc to an indium chloride solution to deposit metallic indium, indium ions and indium hydroxide coexist in the liquid, and the concentration of indium ions in the liquid is set to 60 to 85 g / L. The method for recovering indium as described in (1) above.
(3) In the method of (1) or (2) above, the pH of the indium chloride solution is adjusted to 2.5 to 3.5 to produce indium hydroxide, and indium ions and indium hydroxide coexist. A method for recovering indium to deposit metal indium.
(4) Indium metal in an indium chloride solution in an initial concentration of 60 to 85 g / L and an initial indium hydroxide amount (in conversion) of 5 to 60 g / L (total indium concentration of 90 to 120 g / L). The method for recovering indium as described in any one of (1) to (3) above.
本発明の方法は、塩化インジウム溶液に亜鉛を添加して金属インジウムを析出させる工程において、液中にインジウムイオンと水酸化インジウムを共存させた状態で金属インジウムを析出させるので、液中のインジウムイオン濃度をセメンテーションに適した範囲に保持しながら溶液全体のインジウム濃度を高くすることができ、亜鉛板の不溶化を防止して安定にインジウムを析出させることができる。 In the method of the present invention, in the step of adding zinc to an indium chloride solution to deposit metallic indium, metallic indium is deposited in the state where indium ions and indium hydroxide coexist in the liquid. While maintaining the concentration in a range suitable for cementation, the concentration of indium in the entire solution can be increased, and insolubilization of the zinc plate can be prevented and indium can be stably deposited.
本発明の方法によって回収したスポンジ状の金属インジウムには水酸化インジウムおよび水酸化亜鉛は殆ど含まれておらず、不純物の少ない金属インジウムを得ることができる。 Sponge-like metal indium recovered by the method of the present invention contains almost no indium hydroxide or zinc hydroxide, and metal indium with few impurities can be obtained.
以下、本発明を実施例と共に具体的に説明する。
本発明の方法は、塩化インジウム溶液に亜鉛を添加して金属インジウムを析出させる工程において、液中にインジウムイオンと水酸化インジウムを共存させた状態で金属インジウムを析出させることを特徴とするインジウムの回収方法である。
Hereinafter, the present invention will be specifically described together with examples.
In the method of the present invention, in the step of depositing metal indium by adding zinc to an indium chloride solution, metal indium is deposited in a state where indium ions and indium hydroxide coexist in the liquid. It is a collection method.
本発明の塩化インジウム溶液は、例えば、ITOスクラップを塩酸に溶解し、液中のズスを水酸化スズ沈澱などにして濾過分離した溶液である。具体的には、ITOスクラップを60〜90℃の温度下で塩酸に溶解する。この溶解液にアルカリ(水酸化ナトリウム等)を添加してpH1.5〜2.5に調整して水酸化スズ沈澱を生成させ、固液分離して水酸化スズ沈澱を除去する。 The indium chloride solution of the present invention is, for example, a solution in which ITO scrap is dissolved in hydrochloric acid and the residue in the solution is filtered and separated by tin hydroxide precipitation or the like. Specifically, ITO scrap is dissolved in hydrochloric acid at a temperature of 60 to 90 ° C. An alkali (sodium hydroxide or the like) is added to the solution to adjust the pH to 1.5 to 2.5 to produce a tin hydroxide precipitate, and solid-liquid separation is performed to remove the tin hydroxide precipitate.
水酸化スズを除去した塩化インジウム溶液にさらに水酸化ナトリウム等のアルカリを添加して該溶液のpHを2.5〜3.5に調整して水酸化インジウムを生成させる。このpHが2.5より低いと水酸化インジウム沈澱が十分に生成しない。またこのpHが3.5より高いとインジウムイオンの多くが水酸化インジウム沈澱となり、液中のインジウムイオン濃度が低くなり過ぎる。上記pH範囲の液性下でセメンテーション(亜鉛とインジウムの置換反応)を行う。 An alkali such as sodium hydroxide is further added to the indium chloride solution from which tin hydroxide has been removed to adjust the pH of the solution to 2.5 to 3.5 to produce indium hydroxide. If the pH is lower than 2.5, indium hydroxide precipitates are not sufficiently formed. If this pH is higher than 3.5, most of the indium ions are precipitated by indium hydroxide, and the concentration of indium ions in the liquid becomes too low. Cementation (substitution reaction between zinc and indium) is performed under liquidity in the above pH range.
塩化インジウム溶液に亜鉛板を浸漬してセメンテーションを行う場合、インジウムイオンの初期濃度は70g/L前後の範囲が好ましい。インジウムイオンの初期濃度がこれより高いと、例えば150g/L程度で、亜鉛板の表面に薄いインジウム膜が生成して亜鉛の溶出が妨げられ、亜鉛とインジウムの置換反応の阻害されるため、セメンテーションが進行しなくなる。一方、液中のインジウムイオン濃度が上記初期濃度より大幅に低いと金属インジウムの析出に時間がかかり、効率が低下する。 When cementation is performed by immersing a zinc plate in an indium chloride solution, the initial concentration of indium ions is preferably in the range of about 70 g / L. If the initial concentration of indium ions is higher than this, for example, about 150 g / L, a thin indium film is formed on the surface of the zinc plate, hindering zinc elution and inhibiting the substitution reaction between zinc and indium. The stationation will not progress. On the other hand, if the indium ion concentration in the liquid is significantly lower than the initial concentration, it takes time to deposit metal indium, and the efficiency is lowered.
また、金属インジウムの析出が進行すると液中のインジウムイオン濃度が次第に減少するので、インジウムイオンの初期濃度が70g/L前後の範囲でセメンテーションを行う場合、インジウムイオンを補充せずに十分な量の金属インジウムを得るには、初期の液量を多く必要とし、最終工程でのインジウムロスが多くなる。 In addition, since the indium ion concentration in the liquid gradually decreases as the deposition of metal indium proceeds, when cementation is performed in the range where the initial concentration of indium ions is around 70 g / L, a sufficient amount without replenishing indium ions. In order to obtain this metal indium, a large amount of initial liquid is required, and indium loss in the final process increases.
本発明の回収方法は、塩化インジウム溶液のpHを2.5〜3.5調整して水酸化インジウムを生成させ、液中にインジウムイオンと水酸化インジウムを共存させた状態で金属インジウムを析出させるので、水酸化インジウムを含めた溶液全体のインジウム濃度を高くしながら、しかも液中のインジウムイオン濃度をセメンテーションに適した濃度範囲に保持してセメンテーションを行うことができるので、亜鉛板の不溶化を防止して安定にインジウムを析出させることができる。 The recovery method of the present invention adjusts the pH of the indium chloride solution to 2.5 to 3.5 to produce indium hydroxide, and deposits metal indium in the state where indium ions and indium hydroxide coexist in the liquid. Therefore, it is possible to perform cementation while increasing the indium concentration of the entire solution including indium hydroxide while maintaining the concentration of indium ions in the solution within a concentration range suitable for cementation, so that the zinc plate is insolubilized. Indium can be stably deposited.
具体的には、セメンテーションに用いる塩化インジウム溶液のインジウム初期濃度は、インジウムイオン濃度60〜100g/L、好ましくは60〜85g/Lの範囲、液中の水酸化インジウム量(In換算)5〜60g/Lの範囲、従って合計のインジウム濃度90〜120g/Lの範囲であるのが好ましい。この濃度範囲の塩化インジウム溶液に亜鉛板を浸漬してインジウムと亜鉛の置換反応を行わせる。置換反応が進行して液中のインジウムイオン濃度が減少すると、液中の水酸化インジウムが溶解してインジウムイオンを液中に供給し、インジウムイオン濃度の平衡が保たれる。 Specifically, the initial concentration of indium chloride in the indium chloride solution used for cementation is in the range of indium ion concentration of 60 to 100 g / L, preferably 60 to 85 g / L, the amount of indium hydroxide in the liquid (In conversion) 5 A range of 60 g / L and therefore a total indium concentration of 90 to 120 g / L is preferred. A zinc plate is immersed in an indium chloride solution in this concentration range to perform a substitution reaction between indium and zinc. When the substitution reaction proceeds and the indium ion concentration in the liquid decreases, indium hydroxide in the liquid dissolves and indium ions are supplied into the liquid, and the equilibrium of the indium ion concentration is maintained.
なお、セメンテーション行うpH範囲下(pH2.5〜3.5)では、液中に溶出した亜鉛イオンが水酸基と結合して水酸化亜鉛を生じる反応は進行しないので、回収したスポンジ状の金属インジウムには水酸化亜鉛が含まれない。 Note that, in the pH range where the cementation is performed (pH 2.5 to 3.5), the reaction of zinc ions eluted in the liquid to combine with hydroxyl groups to generate zinc hydroxide does not proceed. Does not contain zinc hydroxide.
塩化インジウム溶液に水酸化ナトリウム等を添加してpHを上記範囲に調整することによって水酸化インジウムが生成、液が白濁する。これに亜鉛板を浸漬すると置換反応が進行し、スポンジ状の金属インジウムが析出して容器の底に溜まり、一方、液中の水酸化インジウムは置換反応に消費されて次第に溶液を透明になる。反応後、脱水してスポンジ状の金属インジウムを回収する。水酸化インジウムは全量消費され、亜鉛イオンは水酸化亜鉛を生じないので、回収した金属インジウムには水酸化インジウムおよび水酸化亜鉛が含まれておらず、不純物の少ない金属インジウムを回収することができる。 By adding sodium hydroxide or the like to the indium chloride solution and adjusting the pH to the above range, indium hydroxide is generated and the liquid becomes cloudy. When a zinc plate is immersed in this, the substitution reaction proceeds, and sponge-like metal indium is deposited and collected at the bottom of the container. On the other hand, the indium hydroxide in the liquid is consumed in the substitution reaction, and the solution gradually becomes transparent. After the reaction, dehydration is performed to recover sponge-like metal indium. Indium hydroxide is consumed in its entirety, and zinc ions do not produce zinc hydroxide. The recovered metal indium does not contain indium hydroxide and zinc hydroxide, and metal indium with less impurities can be recovered. .
本発明の実施例を比較例と共に以下に示す。 Examples of the present invention are shown below together with comparative examples.
〔実施例1〕
塩化インジウム溶液6500リットルに水酸化ナトリウムを添加し、pH2.8にして水酸化インジウムを生成させ、液中の水酸化インジウム量(In換算)25g/L、遊離のインジウムイオン量69g/L(合計インジウム濃度94g/L)の白濁溶液とした。この溶液に上記pH下で亜鉛板(面積1200cm2)を複数枚浸漬し、72時間放置したところ透明溶液となり、容器底部に沈殿物が堆積した。濾過して沈澱物を回収し、脱水乾燥してスポンジ状の金属インジウム604.5Kgを得た。この金属インジウムに含まれる水酸化インジウムおよび水酸化亜鉛は検出限界以下であった。この結果を表1に示した。
[Example 1]
Sodium hydroxide is added to 6500 liters of indium chloride solution to adjust the pH to 2.8 to produce indium hydroxide. The amount of indium hydroxide in the solution (In conversion) is 25 g / L, the amount of free indium ions is 69 g / L (total) A cloudy solution having an indium concentration of 94 g / L was obtained. A plurality of zinc plates (area: 1200 cm 2 ) were immersed in this solution under the above pH and left for 72 hours to become a transparent solution, and a precipitate was deposited on the bottom of the container. The precipitate was collected by filtration, dehydrated and dried to obtain 604.5 kg of spongy metallic indium. Indium hydroxide and zinc hydroxide contained in the metal indium were below the detection limit. The results are shown in Table 1.
〔実施例2〜3、比較例1、2〕
塩化インジウム溶液のpHを表1に示す値に調整した以外は実施例1と同様にしてスポンジ状の金属インジウムを得た。この結果を表1に示した。
[Examples 2 to 3, Comparative Examples 1 and 2]
Sponge-like metal indium was obtained in the same manner as in Example 1 except that the pH of the indium chloride solution was adjusted to the value shown in Table 1. The results are shown in Table 1.
表1に示すように、本発明の実施例1〜3は金属インジウムの回収量が多く、回収した金属インジウムに含まれる不純物も少ない。一方、水酸化インジウムを共存させない比較例1は実施例よりも金属インジウムの回収量が大幅に少なく、また、インジウムの大部分が水酸化インジウムである比較例2ではセメンテーションが殆ど進行せず、金属インジウムの回収量が極端に少ない。 As shown in Table 1, Examples 1 to 3 of the present invention have a large amount of recovered metal indium and a small amount of impurities contained in the recovered metal indium. On the other hand, in Comparative Example 1 in which indium hydroxide does not coexist, the amount of recovered metal indium is much smaller than that in Example, and in Comparative Example 2 in which most of indium is indium hydroxide, cementation hardly proceeds. The amount of recovered metal indium is extremely small.
Claims (4)
A method for recovering indium, characterized in that, in a step of depositing metal indium by adding zinc to an indium chloride solution, indium ions and indium hydroxide coexist in the solution to deposit metal indium.
In the step of depositing metal indium by adding zinc to an indium chloride solution, indium ions and indium hydroxide coexist in the liquid, and the concentration of indium ions in the liquid is set to 60 to 85 g / L. Item 2. The method for recovering indium according to Item 1.
3. The method of claim 1, wherein the indium chloride solution is adjusted to a pH of 2.5 to 3.5 to produce indium hydroxide, and indium ions and indium hydroxide coexist to deposit metal indium. Collection method.
Claims for depositing metal indium in an indium chloride solution in an indium ion initial concentration of 60 to 85 g / L and an initial indium hydroxide amount (in conversion) of 5 to 60 g / L (total indium concentration of 90 to 120 g / L). Item 4. The method for recovering indium according to any one of Items 1 to 3.
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| JPS63140047A (en) * | 1986-12-02 | 1988-06-11 | Nippon Mining Co Ltd | Recovering method for indium in acid liquor |
| JP3173404B2 (en) * | 1997-01-22 | 2001-06-04 | 三菱マテリアル株式会社 | How to recover indium |
| JP4598921B2 (en) * | 2000-06-09 | 2010-12-15 | 出光興産株式会社 | Indium recovery method |
| JP4549501B2 (en) * | 2000-08-28 | 2010-09-22 | 日鉱金属株式会社 | Indium recovery method |
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