WO2017124892A1 - Method for recycling copper indium gallium selenium materials - Google Patents

Method for recycling copper indium gallium selenium materials Download PDF

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WO2017124892A1
WO2017124892A1 PCT/CN2016/112147 CN2016112147W WO2017124892A1 WO 2017124892 A1 WO2017124892 A1 WO 2017124892A1 CN 2016112147 W CN2016112147 W CN 2016112147W WO 2017124892 A1 WO2017124892 A1 WO 2017124892A1
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copper
indium gallium
gallium selenide
copper indium
indium
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PCT/CN2016/112147
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French (fr)
Chinese (zh)
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高永涛
刘军飞
王冠
吴国发
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汉能新材料科技有限公司
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    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B7/00Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
    • C22B7/006Wet processes
    • C22B7/007Wet processes by acid leaching
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B19/00Selenium; Tellurium; Compounds thereof
    • C01B19/02Elemental selenium or tellurium
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B15/00Obtaining copper
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B15/00Obtaining copper
    • C22B15/0063Hydrometallurgy
    • C22B15/0065Leaching or slurrying
    • C22B15/0067Leaching or slurrying with acids or salts thereof
    • C22B15/0071Leaching or slurrying with acids or salts thereof containing sulfur
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B15/00Obtaining copper
    • C22B15/0063Hydrometallurgy
    • C22B15/0084Treating solutions
    • C22B15/0089Treating solutions by chemical methods
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B58/00Obtaining gallium or indium
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B7/00Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Definitions

  • the invention relates to a method for recovering a copper indium gallium selenide photovoltaic module, in particular to a method for recovering copper indium gallium selenide material.
  • the copper indium gallium selenide thin film solar cell has many advantages and is favored by the market. It is the biggest hot spot in the research and development, scale production and application of thin film solar cells in recent years.
  • the absorption layer of copper indium gallium selenide solar cell consists of copper, indium, gallium and selenium in the optimal proportion of chalcopyrite structure, which can absorb a wide range of wavelengths, except for the visible spectrum of light absorbed by amorphous silicon solar cells. It can also cover the near-infrared region with a wavelength between 700 and 2000 nm, that is, the longest power generation in one day.
  • the copper indium gallium selenide thin film solar cell can exceed 20% per day compared with the same wattage level crystalline silicon solar cell.
  • Crystalline silicon cells are inherently photo-attenuating, and their power generation efficiency will gradually decrease after prolonged exposure to sunlight.
  • the copper indium gallium selenide solar cell has no photo-induced attenuation characteristics and high power generation stability. Crystal silicon solar cells have hot spots after power generation for a long period of time, resulting in small power generation and increased maintenance costs.
  • the copper indium gallium selenide solar cell can adopt an internal connection structure to avoid this phenomenon, and the maintenance cost is lower than that of the crystalline silicon solar cell.
  • Copper indium gallium selenide thin film solar cells are produced by vacuum sputtering, distillation and non-vacuum coating. No matter which manufacturing method is used, some materials of copper indium gallium selenide are produced during the production process. In addition to heavy metal copper, it also contains rare metals such as indium, gallium and selenium. In order to facilitate the continuous utilization of rare metals such as indium, gallium and selenium and heavy metal copper, it needs to be separated and separately recovered to facilitate further recycling to ensure the sustainable development of copper indium gallium selenide thin film solar cell materials. In the prior art, the method for recovering copper indium gallium selenide material mainly includes acid dissolution method, extraction method and oxidation distillation method. A combination of wet or fire refining methods.
  • a method for recovering copper indium gallium selenide is disclosed in Chinese Patent Application Publication No. CN102296178A, and specifically discloses a method of dissolving a metal powder containing copper indium gallium selenide using a mixed solution of hydrochloric acid and hydrogen peroxide.
  • the method uses helium to reduce selenium, replaces copper with indium metal, and separates indium from gallium by a supported liquid membrane in combination with a dispersed stripping solution.
  • a method for recovering copper indium gallium selenide is disclosed in Chinese Patent Application Publication No. CN103184388A, which first breaks the copper indium gallium selenide thin film solar panel into pieces, and then uses the soaking process to use the sulphuric acid at a predetermined temperature by a soaking process.
  • the soaking solution is obtained by immersing in a mixed system with hydrogen peroxide for a predetermined period of time, and then indium, gallium, and selenium are recovered by processes such as extraction, back extraction, and electrolysis.
  • U.S. Patent No. 5,779,877 discloses a method of recovering copper indium selenide solar cell materials.
  • the method mainly comprises crushing, nitric acid leaching, electrolysis of copper, selenium and indium by two electrodes, followed by evaporation to obtain a mixture of indium and zinc oxides, and oxidative distillation to separate copper and selenium.
  • an object of the present invention is to provide a method for recovering copper indium gallium selenide materials capable of reducing environmental pollution, high indium recovery rate, and low production cost.
  • the method for recovering copper indium gallium selenide material of the invention adopts sulfuric acid + hydrogen peroxide leaching to reduce the volatilization of acid gas during the leaching process, and is relatively environmentally friendly; separating copper by the principle of copper ammonia complexing greatly reduces the cost, the operation is simple, the equipment requirement is low, and at the same time Obtaining a high purity of the copper product; using the two sexes of gallium, that is, by adding excessive The lye directly obtains the sodium gallate solution, thereby achieving the purpose of separating indium and gallium, and the separation effect is good, and the obtained indium and gallium products have high purity.
  • the method for recovering copper indium gallium selenide material of the invention comprises the following steps:
  • step A the copper indium gallium selenide material is placed in a ball mill for ball milling, and then dried by ball milling.
  • step B the concentrated sulfuric acid is diluted, and the alloy powder obtained in the step A is mixed with the diluted concentrated sulfuric acid.
  • the hydrogen peroxide is introduced to carry out leaching, and after the leaching is completed, the residue is filtered to obtain a pure leachate.
  • the process contains the following reactions:
  • step C after the temperature of the leachate is raised, sulfur dioxide gas is introduced to carry out selenium reduction.
  • the process contains the following reactions:
  • Step D after removing the selenium, directly add concentrated ammonia water to adjust the pH value to neutral 7.0, and then stand at room temperature after stirring, then extract the supernatant, directly filter to obtain gallium hydroxide and indium hydroxide precipitate, and copper ammonia supernatant.
  • the process contains the following reactions:
  • step E the copper ammonia supernatant is directly added with sodium sulfide, and the diluted polyacrylamide is added, and the copper sulfide precipitate is obtained by directly filtering after constant temperature stirring.
  • Step F adding a solution of gallium hydroxide and indium hydroxide to the sodium hydroxide solution, stirring at a constant temperature, and then allowing to stand, and then extracting the supernatant, and directly filtering to obtain an indium hydroxide precipitate and a sodium gallate supernatant.
  • the process contains the following reactions:
  • step G the sodium gallate solution is directly electrolyzed under alkaline conditions to obtain a monolithic gallium.
  • the process contains the following reactions:
  • step H the indium hydroxide precipitate is reverse-dissolved with hydrochloric acid, replaced with a zinc plate, and after displacement, washed and filtered to obtain sponge indium.
  • the process contains the following reactions:
  • the method further comprises: ball milling the copper indium gallium selenide material to 40 mesh or less in step A, and drying at 100 ° C for 4 hours after ball milling.
  • the method further comprises: diluting the concentrated sulfuric acid to 25% in step B, mixing the drying material with 25% concentrated sulfuric acid according to a solid-liquid ratio of 1:5, and raising the temperature to At 90 ° C, hydrogen peroxide was introduced at a rate of 8 ml / min, the stirring rate was 600 r / min, and the temperature was leached for 3 h.
  • the method further comprises: after the temperature of the leachate is raised to 65 ° C in step C, the sulfur dioxide gas is introduced at a rate of 10 L/min, and the temperature is maintained for 10 hours.
  • the method further comprises: in step D, the ammonia water concentration is 20%, stirring at normal temperature for 20 minutes, stirring rate is 200r/min, and after standing for 2 hours, the supernatant is extracted, and the washing is performed three times repeatedly.
  • the water consumption per wash water does not exceed 800ml.
  • step E further comprising adding 10% of the diluted polyacrylamide 20 ml in step E, the temperature is 60 ° C, the stirring rate is 200 r/min, and the mixture is stirred at a constant temperature for 20 min.
  • the method further comprises: adding the gallium hydroxide and the indium hydroxide precipitate in the step F to the 8 mol/L sodium hydroxide solution and heating to 80 ° C, stirring at a rate of 200 r/min, and stirring at a constant temperature for 20 min. After the reaction, the supernatant was taken for 2 hours, and washed repeatedly for three times. The water consumption per wash did not exceed 800 ml.
  • the method further comprises: the sodium gallate solution in the step G is directly electrolyzed under alkaline conditions, and the electrolysis condition is a current of 1.5 A, a voltage of 4.0 V, a pole spacing of 25 mm, and a plate area. 50mm ⁇ 50mm, single cathode and double anode configuration, electrolysis for 6h, you can get gallium element.
  • the method further comprises: in step H, pre-dissolving the indium hydroxide precipitate with 600 ml of 10% hydrochloric acid, dissolving and adjusting the pH to 1.5, and heating to 55 ° C, stirring at a constant temperature, stirring The rate was 200 r/min, and the replacement was carried out with a 4N zinc plate, and the replacement time was 6 hours. After the replacement, the sponge was infiltrated and filtered to obtain a sponge indium.
  • Figure 1 is a schematic illustration of a process for recovering a copper indium gallium selenide material of the present invention.
  • the method for recovering copper indium gallium selenide material of the present invention mainly comprises the following steps:
  • step A 200 g of copper indium gallium selenide material was placed in a ball mill, ball-milled to a powder of 40 mesh or less, and dried at 100 ° C for 4 hours.
  • Step B dilute concentrated sulfuric acid to 25%, mix 200g of dried material with 25% concentrated sulfuric acid according to a solid-liquid ratio of 1:5, raise the temperature to 90 ° C, and introduce hydrogen peroxide at a rate of 8 ml / min, stirring rate 600 r / Min, immersed at constant temperature for 3 h, and after the leaching is finished, the residue is filtered off to obtain a pure leachate.
  • step C after the leaching solution is heated to 65 ° C, sulfur dioxide gas is introduced at a rate of 10 L/min and the temperature is kept for 10 h. During the process of reducing selenium, a brick red precipitate is formed in the container, gradually becomes black, and black selenium is obtained after filtration.
  • Step D after removing selenium, directly add 20% concentrated ammonia water to adjust the pH value to neutral 7.0, stir at normal temperature for 20 min, stir at a rate of 200 r/min, and after standing for 2 h, extract the supernatant, and wash it three times with each wash. The amount does not exceed 800 ml, and finally directly filtered to obtain a precipitate of gallium hydroxide and indium hydroxide, and a copper ammonia supernatant.
  • Step E the copper ammonia supernatant is directly added with sodium sulfide, 20 ml of 10% diluted polyacrylamide is added, the temperature is 60 ° C, the stirring rate is 200 r / min, the temperature is stirred for 20 min, and the copper sulfide precipitate is obtained by direct filtration.
  • Step F adding gallium hydroxide and indium hydroxide precipitate to 8 mol/L sodium hydroxide solution and heating to 80 ° C, stirring rate 200 r / min, stirring at a constant temperature for 20 min, after standing for 2 h, extracting the supernatant, repeatedly washing and extracting three times, each The secondary washing water does not exceed 800 ml, and finally directly filtered to obtain an indium hydroxide precipitate and a sodium gallate supernatant.
  • Step G sodium gallate solution is directly electrolyzed under alkaline conditions.
  • the electrolysis conditions are current 1.5A, voltage 4.0V, pole spacing 25mm, plate area 50mm ⁇ 50mm, single cathode double anode configuration, electrolysis 6h, ie A single element of gallium is available.
  • Step H the indium hydroxide precipitate is reversely dissolved with 600 ml of 10% hydrochloric acid, dissolved to adjust the pH to 1.5, and the temperature is raised to 55 ° C with constant temperature stirring, the stirring rate is 200 r / min, and the replacement is performed with 4N zinc plate, the replacement time is 6 h, and the replacement is performed. After washing and filtering, a sponge indium can be obtained.

Abstract

A method for recycling copper indium gallium selenium materials comprises the steps of leaching by using sulfuric acid and hydrogen peroxide, reduction of selenium by using sulfur dioxide, separation of copper by using cuprous ammine complexation, alkali separation of indium and gallium, replacement of indium, hydrolysis of gallium, and the like. In the recycling method, leaching is carried out by using sulfuric acid in cooperation with hydrogen peroxide, so that the leaching rate is greatly improved, and acid gas pollution is reduced; in addition, copper is separated by using cuprous ammine complexation, deposition is not generated, metal ions can be well separated;and in another aspect, in the method, alkali separation of gallium is carried out, separation between indium and gallium can be implemented by merely adjusting the PH of a solution, the separation effect is good, the purities of obtained indium and gallium products are high.

Description

一种铜铟镓硒物料的回收方法Method for recovering copper indium gallium selenide material 技术领域Technical field
本发明涉及一种铜铟镓硒光伏组件的回收方法,尤其涉及一种铜铟镓硒物料的回收方法。The invention relates to a method for recovering a copper indium gallium selenide photovoltaic module, in particular to a method for recovering copper indium gallium selenide material.
背景技术Background technique
铜铟镓硒薄膜太阳能电池具备众多优势而备受市场青睐,其是最近几年薄膜太阳能电池研发、规模生产、应用的最大热点。铜铟镓硒太阳能电池的吸收层由铜、铟、镓、硒四种元素按照最佳比例组成黄铜矿结构,可吸收光谱波长范围广,除了非晶硅太阳能电池可吸收光的可见光谱范围,还可以涵盖波长在700~2000nm之间的近红外区,即一天内发电的时间最长,铜铟镓硒薄膜太阳能电池与同一瓦数级别的晶硅太阳能电池相比,每天可以超出20%比例的总发电量。晶硅电池本质上有光致衰减的特性,经过阳光的长时间暴晒,其发电效能会逐渐减退。而铜铟镓硒太阳能电池则没有光致衰减特性,发电稳定性高。晶硅太阳能电池经过较长一段时间发电后存在热斑现象,导致发电量小,增加维护费用。而铜铟镓硒太阳能电池能采用内部连接结构,可避免此现象的发生,较晶体硅太阳能电池比所需的维护费用低。The copper indium gallium selenide thin film solar cell has many advantages and is favored by the market. It is the biggest hot spot in the research and development, scale production and application of thin film solar cells in recent years. The absorption layer of copper indium gallium selenide solar cell consists of copper, indium, gallium and selenium in the optimal proportion of chalcopyrite structure, which can absorb a wide range of wavelengths, except for the visible spectrum of light absorbed by amorphous silicon solar cells. It can also cover the near-infrared region with a wavelength between 700 and 2000 nm, that is, the longest power generation in one day. The copper indium gallium selenide thin film solar cell can exceed 20% per day compared with the same wattage level crystalline silicon solar cell. The total amount of electricity generated in proportion. Crystalline silicon cells are inherently photo-attenuating, and their power generation efficiency will gradually decrease after prolonged exposure to sunlight. The copper indium gallium selenide solar cell has no photo-induced attenuation characteristics and high power generation stability. Crystal silicon solar cells have hot spots after power generation for a long period of time, resulting in small power generation and increased maintenance costs. The copper indium gallium selenide solar cell can adopt an internal connection structure to avoid this phenomenon, and the maintenance cost is lower than that of the crystalline silicon solar cell.
铜铟镓硒薄膜太阳能电池的制作方式有真空溅镀法、蒸馏法和非真空涂布法,无论采用哪种制作方法,其制作过程中都会产生一些铜铟镓硒的物料,而这些物料中除含重金属铜之外,还含有铟、镓和硒等稀有金属。为有利于铟、镓和硒等稀有金属和重金属铜的持续利用,需要将其进行分离并分别回收,以方便进一步地循环利用,以保证铜铟镓硒薄膜太阳能电池材料的可持续发展。现有技术中,铜铟镓硒物料的回收方法主要有酸溶解法、萃取法、氧化蒸馏法 等湿法或火法精炼组合方法。Copper indium gallium selenide thin film solar cells are produced by vacuum sputtering, distillation and non-vacuum coating. No matter which manufacturing method is used, some materials of copper indium gallium selenide are produced during the production process. In addition to heavy metal copper, it also contains rare metals such as indium, gallium and selenium. In order to facilitate the continuous utilization of rare metals such as indium, gallium and selenium and heavy metal copper, it needs to be separated and separately recovered to facilitate further recycling to ensure the sustainable development of copper indium gallium selenide thin film solar cell materials. In the prior art, the method for recovering copper indium gallium selenide material mainly includes acid dissolution method, extraction method and oxidation distillation method. A combination of wet or fire refining methods.
公开号为CN102296178A的中国专利申请中公开了一种铜铟镓硒的回收方法,具体公开了利用盐酸与过氧化氢的混合液来溶解包含有铜铟镓硒金属粉体的方法。该方法使用肼还原硒,以铟金属置换铜,并通过支撑式液膜结合分散反萃液将铟与镓分离。A method for recovering copper indium gallium selenide is disclosed in Chinese Patent Application Publication No. CN102296178A, and specifically discloses a method of dissolving a metal powder containing copper indium gallium selenide using a mixed solution of hydrochloric acid and hydrogen peroxide. The method uses helium to reduce selenium, replaces copper with indium metal, and separates indium from gallium by a supported liquid membrane in combination with a dispersed stripping solution.
公开号为CN103184388A的中国专利申请中公开了一种铜铟镓硒的回收方法,该方法首先破碎所述铜铟镓硒薄膜太阳能板成碎片,而后利用浸泡工序将所述碎片用规定温度的硫酸与过氧化氢的混合体系浸泡规定时间得到浸泡液,随后利用萃取,反萃取,电解等工艺回收铟、镓、硒元素。A method for recovering copper indium gallium selenide is disclosed in Chinese Patent Application Publication No. CN103184388A, which first breaks the copper indium gallium selenide thin film solar panel into pieces, and then uses the soaking process to use the sulphuric acid at a predetermined temperature by a soaking process. The soaking solution is obtained by immersing in a mixed system with hydrogen peroxide for a predetermined period of time, and then indium, gallium, and selenium are recovered by processes such as extraction, back extraction, and electrolysis.
美国专利号US5779877公开了一种铜铟硒太阳能电池物料的回收方法。所述方法主要包括破碎、硝酸浸出,两电极电解分离铜、硒和铟,然后蒸发分解得到铟和锌的氧化物的混合物,氧化蒸馏分离铜和硒。U.S. Patent No. 5,779,877 discloses a method of recovering copper indium selenide solar cell materials. The method mainly comprises crushing, nitric acid leaching, electrolysis of copper, selenium and indium by two electrodes, followed by evaporation to obtain a mixture of indium and zinc oxides, and oxidative distillation to separate copper and selenium.
在上述现有技术术中,使用盐酸和过氧化氢浸出会消耗大量的氧化剂,且盐酸易挥发,在浸出反应过程中是放热反应,造成盐酸大量挥发,污染较为严重。同时,萃取铟时使用的萃取剂对镓产生共萃现象,造成铟、镓分离困难,从而降低了镓的回收率。另一方面采用铟置换铜处理方法,生产成本过于高昂。In the above prior art technique, the use of hydrochloric acid and hydrogen peroxide leaching consumes a large amount of oxidant, and hydrochloric acid is volatile, and is exothermic during the leaching reaction, causing a large amount of hydrochloric acid to volatilize and the pollution is serious. At the same time, the extractant used in the extraction of indium produces a co-extraction phenomenon of gallium, which makes separation of indium and gallium difficult, thereby reducing the recovery rate of gallium. On the other hand, the indium replacement copper treatment method is too expensive.
发明内容Summary of the invention
为解决现有技术中的上述缺陷,本发明的目的在于提供一种能够减少环境污染,且铟回收率高,生产成本较低的铜铟镓硒物料的回收方法。In order to solve the above-mentioned drawbacks in the prior art, an object of the present invention is to provide a method for recovering copper indium gallium selenide materials capable of reducing environmental pollution, high indium recovery rate, and low production cost.
本发明的铜铟镓硒物料的回收方法采用硫酸+双氧水浸出,减少浸出过程中酸气的挥发,比较环保;通过铜氨络合原理分离铜大幅降低了成本,操作简单,设备要求低,同时得到铜产品纯度较高;利用镓的两性,即通过加入过量 碱液,直接得到镓酸钠溶液,以此达到分离铟、镓的目的,分离效果好,所得到的铟、镓产品纯度较高。The method for recovering copper indium gallium selenide material of the invention adopts sulfuric acid + hydrogen peroxide leaching to reduce the volatilization of acid gas during the leaching process, and is relatively environmentally friendly; separating copper by the principle of copper ammonia complexing greatly reduces the cost, the operation is simple, the equipment requirement is low, and at the same time Obtaining a high purity of the copper product; using the two sexes of gallium, that is, by adding excessive The lye directly obtains the sodium gallate solution, thereby achieving the purpose of separating indium and gallium, and the separation effect is good, and the obtained indium and gallium products have high purity.
本发明的铜铟镓硒物料的回收方法,包括如下步骤:The method for recovering copper indium gallium selenide material of the invention comprises the following steps:
步骤A,将铜铟镓硒物料放置于球磨机中进行球磨,球磨后进行烘干。In step A, the copper indium gallium selenide material is placed in a ball mill for ball milling, and then dried by ball milling.
步骤B,将浓硫酸稀释,将步骤A中所得合金粉末与稀释后浓硫酸混合,升温后,通入双氧水,进行浸出,浸出结束后滤出残渣,即可得到纯净浸出液。该过程包含的反应如下:In step B, the concentrated sulfuric acid is diluted, and the alloy powder obtained in the step A is mixed with the diluted concentrated sulfuric acid. After the temperature is raised, the hydrogen peroxide is introduced to carry out leaching, and after the leaching is completed, the residue is filtered to obtain a pure leachate. The process contains the following reactions:
Figure PCTCN2016112147-appb-000001
Figure PCTCN2016112147-appb-000001
Figure PCTCN2016112147-appb-000002
Figure PCTCN2016112147-appb-000002
Figure PCTCN2016112147-appb-000003
Figure PCTCN2016112147-appb-000003
Figure PCTCN2016112147-appb-000004
Figure PCTCN2016112147-appb-000004
Figure PCTCN2016112147-appb-000005
Figure PCTCN2016112147-appb-000005
步骤C,将浸出液升温后,通入二氧化硫气体,进行硒还原。该过程包含的反应如下:In step C, after the temperature of the leachate is raised, sulfur dioxide gas is introduced to carry out selenium reduction. The process contains the following reactions:
Figure PCTCN2016112147-appb-000006
Figure PCTCN2016112147-appb-000006
还原硒过程中会看到容器内有砖红色沉淀生成,逐渐变成黑色,过滤后得到黑硒。During the process of reducing selenium, a red precipitate of bricks is formed in the container, which gradually turns black, and black selenium is obtained after filtration.
步骤D,除硒后液直接加入浓氨水调节PH值至中性7.0,常温搅拌后静置,随后抽取上清液,直接过滤得到氢氧化镓和氢氧化铟沉淀,以及铜氨上清液。 该过程包含的反应如下:Step D, after removing the selenium, directly add concentrated ammonia water to adjust the pH value to neutral 7.0, and then stand at room temperature after stirring, then extract the supernatant, directly filter to obtain gallium hydroxide and indium hydroxide precipitate, and copper ammonia supernatant. The process contains the following reactions:
6OH-+In2(SO4)3→3Na2SO4+2In(OH)3 6OH - +In 2 (SO 4 ) 3 →3Na 2 SO 4 +2In(OH) 3
6OH-+Ga2(SO4)3→3Na2SO4+2Ga(OH)3 6OH - +Ga 2 (SO 4 ) 3 →3Na 2 SO 4 +2Ga(OH) 3
Cu2++4NH3→Cu(NH3)4 2+ Cu 2+ +4NH 3 →Cu(NH 3 ) 4 2+
步骤E,铜氨上清液直接加入硫化钠,并加入稀释后的聚丙烯酰胺,恒温搅拌后直接过滤即可得到硫化铜沉淀。In step E, the copper ammonia supernatant is directly added with sodium sulfide, and the diluted polyacrylamide is added, and the copper sulfide precipitate is obtained by directly filtering after constant temperature stirring.
步骤F,氢氧化镓和氢氧化铟沉淀加入氢氧化钠溶液,恒温搅拌后静置,随后抽取上清液,直接过滤得到氢氧化铟沉淀和镓酸钠上清液。该过程包含的反应如下:Step F, adding a solution of gallium hydroxide and indium hydroxide to the sodium hydroxide solution, stirring at a constant temperature, and then allowing to stand, and then extracting the supernatant, and directly filtering to obtain an indium hydroxide precipitate and a sodium gallate supernatant. The process contains the following reactions:
Ga(OH)3+OH-→GaO2 -+2H2OGa(OH) 3 +OH - →GaO 2 - +2H 2 O
步骤G,镓酸钠溶液直接在碱性条件下电解,即可得到镓单质。该过程包含的反应如下:In step G, the sodium gallate solution is directly electrolyzed under alkaline conditions to obtain a monolithic gallium. The process contains the following reactions:
GaO2 -+2H2O→Ga+O2+4OH- GaO 2 - +2H 2 O→Ga+O 2 +4OH -
步骤H,将氢氧化铟沉淀用盐酸反溶,用锌板进行置换,置换后洗涤过滤即可得到海绵铟。该过程包含的反应如下:In step H, the indium hydroxide precipitate is reverse-dissolved with hydrochloric acid, replaced with a zinc plate, and after displacement, washed and filtered to obtain sponge indium. The process contains the following reactions:
In(OH)3+3Hcl→InCl3+3H2OIn(OH) 3 +3Hcl→InCl 3 +3H 2 O
3Zn+2InCl3→3ZnCl2+2In3Zn+2InCl 3 →3ZnCl 2 +2In
本发明的铜铟镓硒物料的回收方法中,还进一步包括,在步骤A中将铜铟镓硒物料球磨至40目以下,球磨后100℃下烘干4小时。In the method for recovering the copper indium gallium selenide material of the present invention, the method further comprises: ball milling the copper indium gallium selenide material to 40 mesh or less in step A, and drying at 100 ° C for 4 hours after ball milling.
本发明的铜铟镓硒物料的回收方法中,还进一步包括,在步骤B中将浓硫酸稀释至25%,烘干料与25%浓硫酸按照固液比1:5混合,将温度升至90℃,按8ml/min速率通入双氧水,搅拌速率600r/min,恒温浸出3h。 In the method for recovering the copper indium gallium selenide material of the present invention, the method further comprises: diluting the concentrated sulfuric acid to 25% in step B, mixing the drying material with 25% concentrated sulfuric acid according to a solid-liquid ratio of 1:5, and raising the temperature to At 90 ° C, hydrogen peroxide was introduced at a rate of 8 ml / min, the stirring rate was 600 r / min, and the temperature was leached for 3 h.
本发明的铜铟镓硒物料的回收方法中,还进一步包括,在步骤C中将浸出液升温至65℃后,通入二氧化硫气体,速率10L/min,恒温10h。In the method for recovering the copper indium gallium selenide material of the present invention, the method further comprises: after the temperature of the leachate is raised to 65 ° C in step C, the sulfur dioxide gas is introduced at a rate of 10 L/min, and the temperature is maintained for 10 hours.
本发明的铜铟镓硒物料的回收方法中,还进一步包括,在步骤D中氨水浓度为20%,常温搅拌20min,搅拌速率200r/min,静置2h后抽取上清液,反复洗涤抽取三次,每次洗涤水用水量不超过800ml。In the method for recovering the copper indium gallium selenide material of the present invention, the method further comprises: in step D, the ammonia water concentration is 20%, stirring at normal temperature for 20 minutes, stirring rate is 200r/min, and after standing for 2 hours, the supernatant is extracted, and the washing is performed three times repeatedly. The water consumption per wash water does not exceed 800ml.
本发明的铜铟镓硒物料的回收方法中,还进一步包括,步骤E中加入10%稀释后聚丙烯酰胺20ml,温度60℃,搅拌速率200r/min,恒温搅拌20min。In the method for recovering the copper indium gallium selenide material of the present invention, further comprising adding 10% of the diluted polyacrylamide 20 ml in step E, the temperature is 60 ° C, the stirring rate is 200 r/min, and the mixture is stirred at a constant temperature for 20 min.
本发明的铜铟镓硒物料的回收方法中,还进一步包括,步骤F中氢氧化镓和氢氧化铟沉淀加入8mol/L氢氧化钠溶液加热至80℃,搅拌速率200r/min,恒温搅拌20min后,静置2h后抽取上清液,反复洗涤抽取三次,每次洗涤用水量不超过800ml。In the method for recovering the copper indium gallium selenide material of the present invention, the method further comprises: adding the gallium hydroxide and the indium hydroxide precipitate in the step F to the 8 mol/L sodium hydroxide solution and heating to 80 ° C, stirring at a rate of 200 r/min, and stirring at a constant temperature for 20 min. After the reaction, the supernatant was taken for 2 hours, and washed repeatedly for three times. The water consumption per wash did not exceed 800 ml.
本发明的铜铟镓硒物料的回收方法中,还进一步包括,步骤G中镓酸钠溶液直接在碱性条件下电解,电解条件为电流1.5A,电压4.0V,极间距25mm,极板面积50mm×50mm,单阴极双阳极配置,电解6h,即可得到镓单质。In the method for recovering the copper indium gallium selenide material of the present invention, the method further comprises: the sodium gallate solution in the step G is directly electrolyzed under alkaline conditions, and the electrolysis condition is a current of 1.5 A, a voltage of 4.0 V, a pole spacing of 25 mm, and a plate area. 50mm × 50mm, single cathode and double anode configuration, electrolysis for 6h, you can get gallium element.
本发明的铜铟镓硒物料的回收方法中,还进一步包括,步骤H中将氢氧化铟沉淀用10%盐酸600ml反溶,溶解后调节PH值至1.5,升温至55℃时恒温搅拌,搅拌速率200r/min,用4N锌板进行置换,置换时间6h,置换后洗涤过滤即可得到海绵铟。In the method for recovering the copper indium gallium selenide material of the present invention, the method further comprises: in step H, pre-dissolving the indium hydroxide precipitate with 600 ml of 10% hydrochloric acid, dissolving and adjusting the pH to 1.5, and heating to 55 ° C, stirring at a constant temperature, stirring The rate was 200 r/min, and the replacement was carried out with a 4N zinc plate, and the replacement time was 6 hours. After the replacement, the sponge was infiltrated and filtered to obtain a sponge indium.
附图说明DRAWINGS
图1是本发明的铜铟镓硒物料的回收方法的示意图。BRIEF DESCRIPTION OF THE DRAWINGS Figure 1 is a schematic illustration of a process for recovering a copper indium gallium selenide material of the present invention.
具体实施方式detailed description
以下结合附图对本发明实施方式做进一步阐述。 The embodiments of the present invention are further described below in conjunction with the accompanying drawings.
如图1所示,本发明的铜铟镓硒物料的回收方法主要包括如下步骤:As shown in FIG. 1, the method for recovering copper indium gallium selenide material of the present invention mainly comprises the following steps:
步骤A,将200g铜铟镓硒物料放置于球磨机中,球磨至40目以下的粉末,100℃下烘干4小时。In step A, 200 g of copper indium gallium selenide material was placed in a ball mill, ball-milled to a powder of 40 mesh or less, and dried at 100 ° C for 4 hours.
步骤B,将浓硫酸稀释至25%,将200g烘干料与25%浓硫酸按照固液比1:5混合,将温度升至90℃,按8ml/min速率通入双氧水,搅拌速率600r/min,恒温浸出3h,浸出结束后滤出残渣,即可得到纯净浸出液。Step B, dilute concentrated sulfuric acid to 25%, mix 200g of dried material with 25% concentrated sulfuric acid according to a solid-liquid ratio of 1:5, raise the temperature to 90 ° C, and introduce hydrogen peroxide at a rate of 8 ml / min, stirring rate 600 r / Min, immersed at constant temperature for 3 h, and after the leaching is finished, the residue is filtered off to obtain a pure leachate.
步骤C,将浸出液升温至65℃后,通入二氧化硫气体,速率10L/min,恒温10h,还原硒过程中会看到容器内有砖红色沉淀生成,逐渐变成黑色,过滤后得到黑硒。In step C, after the leaching solution is heated to 65 ° C, sulfur dioxide gas is introduced at a rate of 10 L/min and the temperature is kept for 10 h. During the process of reducing selenium, a brick red precipitate is formed in the container, gradually becomes black, and black selenium is obtained after filtration.
步骤D,除硒后液直接加入20%浓氨水调节PH值至中性7.0,常温搅拌20min,搅拌速率200r/min,静置2h后抽取上清液,反复洗涤抽取三次,每次洗涤水用水量不超过800ml,最后直接过滤得到氢氧化镓和氢氧化铟沉淀,以及铜氨上清液。Step D, after removing selenium, directly add 20% concentrated ammonia water to adjust the pH value to neutral 7.0, stir at normal temperature for 20 min, stir at a rate of 200 r/min, and after standing for 2 h, extract the supernatant, and wash it three times with each wash. The amount does not exceed 800 ml, and finally directly filtered to obtain a precipitate of gallium hydroxide and indium hydroxide, and a copper ammonia supernatant.
步骤E,铜氨上清液直接加入硫化钠,加入10%稀释后聚丙烯酰胺20ml,温度60℃,搅拌速率200r/min,恒温搅拌20min,直接过滤即可得到硫化铜沉淀。Step E, the copper ammonia supernatant is directly added with sodium sulfide, 20 ml of 10% diluted polyacrylamide is added, the temperature is 60 ° C, the stirring rate is 200 r / min, the temperature is stirred for 20 min, and the copper sulfide precipitate is obtained by direct filtration.
步骤F,氢氧化镓和氢氧化铟沉淀加入8mol/L氢氧化钠溶液加热至80℃,搅拌速率200r/min,恒温搅拌20min后,静置2h后抽取上清液,反复洗涤抽取三次,每次洗涤用水量不超过800ml,最后直接过滤得到氢氧化铟沉淀和镓酸钠上清液。Step F, adding gallium hydroxide and indium hydroxide precipitate to 8 mol/L sodium hydroxide solution and heating to 80 ° C, stirring rate 200 r / min, stirring at a constant temperature for 20 min, after standing for 2 h, extracting the supernatant, repeatedly washing and extracting three times, each The secondary washing water does not exceed 800 ml, and finally directly filtered to obtain an indium hydroxide precipitate and a sodium gallate supernatant.
步骤G,镓酸钠溶液直接在碱性条件下电解,电解条件为电流1.5A,电压4.0V,极间距25mm,极板面积50mm×50mm,单阴极双阳极配置,电解6h,即 可得到镓单质。Step G, sodium gallate solution is directly electrolyzed under alkaline conditions. The electrolysis conditions are current 1.5A, voltage 4.0V, pole spacing 25mm, plate area 50mm×50mm, single cathode double anode configuration, electrolysis 6h, ie A single element of gallium is available.
步骤H,将氢氧化铟沉淀用10%盐酸600ml反溶,溶解后调节PH值至1.5,升温至55℃时恒温搅拌,搅拌速率200r/min,用4N锌板进行置换,置换时间6h,置换后洗涤过滤即可得到海绵铟。Step H, the indium hydroxide precipitate is reversely dissolved with 600 ml of 10% hydrochloric acid, dissolved to adjust the pH to 1.5, and the temperature is raised to 55 ° C with constant temperature stirring, the stirring rate is 200 r / min, and the replacement is performed with 4N zinc plate, the replacement time is 6 h, and the replacement is performed. After washing and filtering, a sponge indium can be obtained.
以上实施例仅用于对本发明进行具体说明,其并不对本发明的保护范围起到任何限定作用,本发明的保护范围由权利要求确定。根据本领域的公知技术和本发明所公开的技术方案,可以推导或联想出许多变型方案,所有这些变型方案,也应认为是本发明的保护范围。 The above embodiments are only intended to be illustrative of the invention, and are not intended to limit the scope of the invention, and the scope of the invention is defined by the claims. Many variations can be deduced or derived from the teachings of the present invention and the technical solutions disclosed herein, and all such modifications are also considered to be the scope of the present invention.

Claims (9)

  1. 一种铜铟镓硒物料的回收方法,其特征在于包括如下步骤:A method for recovering copper indium gallium selenide material, comprising the steps of:
    步骤A,将铜铟镓硒物料放置于球磨机中进行球磨,球磨后进行烘干;Step A, placing the copper indium gallium selenide material in a ball mill for ball milling, and drying after ball milling;
    步骤B,将步骤A中所得的烘干料与稀释后的浓硫酸混合,升温后,通入双氧水,进行浸出,浸出结束后滤出残渣,得到浸出液;Step B, the drying material obtained in the step A is mixed with the diluted concentrated sulfuric acid, and after heating, the hydrogen peroxide is introduced to perform leaching, and after the leaching is finished, the residue is filtered to obtain a leachate;
    步骤C,将浸出液升温后,通入二氧化硫气体,进行硒还原;Step C, after the temperature of the leaching solution is raised, sulfur dioxide gas is introduced to perform selenium reduction;
    步骤D,除硒后的余液直接加入浓氨水调节PH值至中性,常温搅拌后静置,随后抽取上清液,直接过滤得到氢氧化镓和氢氧化铟沉淀,以及铜氨上清液;Step D, the residual liquid after removing selenium is directly added with concentrated ammonia water to adjust the pH value to neutrality, and after standing at room temperature, the mixture is allowed to stand, and then the supernatant is extracted, and directly filtered to obtain a precipitate of gallium hydroxide and indium hydroxide, and a copper ammonia supernatant. ;
    步骤E,将铜氨上清液加入硫化钠,并加入稀释后的聚丙烯酰胺,恒温搅拌后过滤,得到硫化铜沉淀;Step E, adding the copper ammonia supernatant to the sodium sulfide, adding the diluted polyacrylamide, stirring at a constant temperature, and filtering to obtain a copper sulfide precipitate;
    步骤F,将步骤E中得到的氢氧化镓和氢氧化铟沉淀加入氢氧化钠溶液,恒温搅拌后静置,随后抽取上清液,直接过滤得到氢氧化铟沉淀和镓酸钠溶液;Step F, the precipitate of the gallium hydroxide and the indium hydroxide obtained in the step E is added to the sodium hydroxide solution, and the mixture is stirred at a constant temperature, and then the supernatant is extracted, and the indium hydroxide precipitate and the sodium gallate solution are directly filtered.
    步骤G,将步骤F中得到的镓酸钠溶液在碱性条件下电解,得到镓单质;Step G, electrolyzing the sodium gallate solution obtained in the step F under alkaline conditions to obtain a simple substance of gallium;
    步骤H,将步骤F中得到的氢氧化铟沉淀用盐酸反溶,用锌板进行置换,得到海绵铟。In step H, the indium hydroxide precipitate obtained in the step F is reversely dissolved with hydrochloric acid and replaced with a zinc plate to obtain a sponge indium.
  2. 如权利要求1所述的铜铟镓硒物料的回收方法,其特征在于,在步骤A中,将铜铟镓硒物料球磨至40目以下,球磨后100℃下烘干4小时。The method for recovering a copper indium gallium selenide material according to claim 1, wherein in step A, the copper indium gallium selenide material is ball milled to 40 mesh or less, and dried at 100 ° C for 4 hours after ball milling.
  3. 如权利要求1或2所述的铜铟镓硒物料的回收方法,其特征在于,在步骤B中,将浓硫酸稀释至25%,将所述烘干料与25%浓硫酸按照固液比1:5混合,将温度升至90℃,按8ml/min速率通入双氧水,搅拌速率600r/min,恒温浸出3小时。 The method for recovering a copper indium gallium selenide material according to claim 1 or 2, wherein in step B, the concentrated sulfuric acid is diluted to 25%, and the dried material and the 25% concentrated sulfuric acid are in a solid-liquid ratio. Mix 1:5, raise the temperature to 90 ° C, pass hydrogen peroxide at a rate of 8 ml / min, stir at 600 r / min, and immerse at constant temperature for 3 hours.
  4. 如权利要求1所述的铜铟镓硒物料的回收方法,其特征在于,在步骤C中,将浸出液升温至65℃后,通入二氧化硫气体,速率10L/min,恒温10小时。The method for recovering a copper indium gallium selenide material according to claim 1, wherein in the step C, the leaching liquid is heated to 65 ° C, and then sulfur dioxide gas is introduced at a rate of 10 L/min for 10 hours.
  5. 如权利要求1所述的铜铟镓硒物料的回收方法,其特征在于,在步骤D中,氨水浓度为20%,常温搅拌20分钟以上,搅拌速率200r/min,静置2小时后抽取上清液,反复洗涤抽取三次,每次洗涤水用水量不超过800ml。The method for recovering a copper indium gallium selenide material according to claim 1, wherein in the step D, the ammonia water concentration is 20%, the mixture is stirred at a normal temperature for 20 minutes or more, the stirring rate is 200 r/min, and the mixture is allowed to stand for 2 hours and then extracted. The clear liquid is washed repeatedly three times, and the water consumption of each wash water does not exceed 800 ml.
  6. 如权利要求1所述的铜铟镓硒物料的回收方法,其特征在于,步骤E中,加入10%稀释后聚丙烯酰胺20ml,温度60℃,搅拌速率200r/min,恒温搅拌20分钟以上。The method for recovering copper indium gallium selenide material according to claim 1, wherein in step E, 20 ml of 10% diluted polyacrylamide is added, the temperature is 60 ° C, the stirring rate is 200 r/min, and the mixture is stirred at a constant temperature for 20 minutes or more.
  7. 如权利要求1所述的铜铟镓硒物料的回收方法,其特征在于,步骤F中,氢氧化镓和氢氧化铟沉淀加入8mol/L氢氧化钠溶液加热至80℃,搅拌速率200r/min,恒温搅拌20min后,静置2小时后抽取上清液,反复洗涤抽取三次,每次洗涤用水量不超过800ml。The method for recovering copper indium gallium selenide material according to claim 1, wherein in step F, the precipitation of gallium hydroxide and indium hydroxide is added to a solution of 8 mol/L sodium hydroxide to 80 ° C, and the stirring rate is 200 r/min. After stirring at a constant temperature for 20 minutes, the supernatant was taken after standing for 2 hours, and washed repeatedly three times, and the water consumption per washing did not exceed 800 ml.
  8. 如权利要求1所述的铜铟镓硒物料的回收方法,其特征在于,步骤G中,镓酸钠溶液直接在碱性条件下电解,电解条件为电流1.5A,电压4.0V,极间距25mm,极板面积50mm×50mm,单阴极双阳极配置,电解时间6小时,即可得到镓单质。The method for recovering copper indium gallium selenide material according to claim 1, wherein in step G, the sodium gallate solution is directly electrolyzed under alkaline conditions, and the electrolysis condition is a current of 1.5 A, a voltage of 4.0 V, and a pole spacing of 25 mm. The plate area is 50mm×50mm, single cathode and double anode configuration, and the electrolysis time is 6 hours, and the gallium element can be obtained.
  9. 如权利要求1所述的铜铟镓硒物料的回收方法,其特征在于,步骤H中,将氢氧化铟沉淀用10%盐酸600ml反溶,溶解后调节PH值至1.5,升温至55℃时恒温搅拌,搅拌速率200r/min,用4N锌板进行置换,置换时间6小时。 The method for recovering copper indium gallium selenide material according to claim 1, wherein in step H, the indium hydroxide precipitate is dissolved in 600 ml of 10% hydrochloric acid, dissolved, adjusted to a pH of 1.5, and heated to 55 ° C. The mixture was stirred under constant temperature at a stirring rate of 200 r/min, and replaced with a 4N zinc plate for a replacement time of 6 hours.
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