• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    A method for recycling silver present in a photovoltaic cell comprising the following successive steps: a) grinding the photovoltaic cell, so as to form a grind containing silver particles, b) dissolving the silver contained in the ground material in a solution containing: ○ at least one ionic liquid, ○ a redox mediator, ○ optionally water, the dissolution leading to the formation of silver ions in solution, c) separating the ground material from the solution, d) performing an electrolysis of the solution to reduce silver ions and to regenerate the redox mediator.
    公开号:FR3044941A1
    申请号:FR1562252
    申请日:2015-12-11
    公开日:2017-06-16
    发明作者:Emmanuel Billy
    申请人:Commissariat a lEnergie Atomique CEA；Commissariat a lEnergie Atomique et aux Energies Alternatives CEA；
    IPC主号:
    专利说明:

    Method for recycling money present in a photovoltaic cell.
    TECHNICAL FIELD OF THE INVENTION The invention relates to a process for recycling silver present in a photovoltaic cell, and more particularly to a recycling process by means of green chemistry. State of the art
    Photovoltaic panels have one or two sides receiving solar radiation, and typically include: - photovoltaic cells, generally silicon, - electrodes, for example copper, to collect the electrical current generated by the photovoltaic cells, - connectors electrodes connecting the electrodes to the outside of the photovoltaic panel, - a polymer, of the EVA (ethylene vinyl acetate) type, used to encapsulate the photovoltaic cells, - a frame and a transparent protective material, generally made of glass, covering the cells, electrodes, and electrical connectors.
    Photovoltaic panels are mainly composed of glass (74% of the total weight), aluminum used for the realization of the frame and often electrical connectors (10%), polymer (about 6.5%), silicon (about 3 %), other metals such as zinc, lead, copper and silver represent a small part of the mass.
    Due to the development of photovoltaic panels and the rising cost of raw materials, the question of their recycling has become fundamental, especially since the Directive of 13 August 2012 on Waste Electrical and Electronic Equipment (WEEE) has has been extended to photovoltaic panels.
    It is necessary to ensure an industrial and reliable recycling process that meets the economic and environmental challenges.
    The minimum targets for recovery and recycling are easily achieved by the only recovery of the glass and the aluminum frame of the photovoltaic panel.
    To improve the quantity of recycled components, the current processes focus on the dismantling of the modules by chemical or thermal means and on the recovery of one or more elements of the module by specialized waste treatment routes.
    The first recycling path consists in dissolving non-selectively the different constituents of the photovoltaic cells. The total dissolution of the oxide layers, silicon, and metal elements (such as Cu, Ag, Sn, Pb, Al, ...) requires the use of harmful and dangerous solutions. The treatment baths are, conventionally, composed of concentrated acid mixtures, generally boiled: mixture of nitric acid and hydrofluoric acid (JP2005311178), mixture of HF, HNO3, H2SO4 and CH3COOH (KR101092259 and KR101256574).
    A succession of different baths of organic solvent, of oxidizing acid, of hydrochloric acid makes it possible, respectively, to remove the conduction grid, the metal residues, and to complex the metal ions (CN102343352).
    These different processes require total dissolution of the photovoltaic module, through complex and expensive processes. The waste (organic solvent, strong acid) resulting from the process must, in addition, be treated.
    It is, moreover, particularly important to be able to recycle the money present in the photovoltaic modules. Indeed, silver represents the metal constituting the highest added value, nearly 90% of the value of the module. Multi-step processes are needed to enhance this element. For example, the document CN102851506 describes a multi-step process comprising the following steps: the aluminum is removed with hydrochloric acid, the silver is dissolved in the presence of water, the silicon nitride is removed by adding hydrofluoric acid, the silver is precipitated in solution by adding iron powder. Although this method makes it possible to recover the silver, the process requires the use of numerous steps and therefore many reagents which must then be treated in order to limit the environmental impact.
    If a real way of solution and valuation of money by green chemistry does not seem to have been considered, it seems sensible in view of current treatments and economic and environmental issues concerning the valuation of money.
    OBJECT OF THE INVENTION The object of the invention is to overcome the drawbacks of the prior art and, in particular, to propose a method for recycling silver present in a photovoltaic cell by green chemistry, which does not require use of highly concentrated acids.
    This object is achieved by a method of recycling the silver present in a photovoltaic cell comprising the following successive steps: a) grinding the photovoltaic cell, so as to form a grind containing silver particles, b) dissolving the silver contained in the ground material in a solution containing: o at least one ionic liquid, o a redox mediator, o optionally water, the dissolution leading to the formation of silver ions in solution, c) separating the ground material from the solution, d) Electrolyze the solution to reduce silver ions and regenerate the redox mediator.
    BRIEF DESCRIPTION OF THE DRAWINGS Other advantages and features will emerge more clearly from the following description of particular embodiments of the invention given by way of nonlimiting examples and represented in the appended figures in which: FIG. graphs giving the current density as a function of the potential vs Ag / AgCl, during the electrodeposition of the silver in an ionic liquid for different anions: DCA, Cl, Br, I, - Figure 2 represents an image, obtained scanning electron microscope, electrodeposited silver, according to the method of the invention; the scale represents 20 μm, FIG. 3 represents a spectrum, obtained by energy dispersive analysis, of the silver deposit of FIG.
    Description of a preferred embodiment of the invention
    The process for recycling the silver present in a photovoltaic cell comprises the following successive steps: a) crushing the photovoltaic cell, so as to form a grind containing silver particles, b) dissolving the silver contained in the ground material in a solution containing: o at least one ionic liquid, o a redox mediator, o possibly water, the dissolution leading to the formation of silver ions in solution, c) separating the ground material from the solution, d) performing an electrolysis of the solution to reduce the silver ions and to regenerate the redox mediator. The silver can thus be recycled, through a chemical dissolution step and an electrochemical deposition step, without the use of acids or concentrated bases. All these steps b) to d) take place in the same solution containing at least one ionic liquid. The solution at the end of the process is regenerated and can be used to upgrade the silver of another photovoltaic cell.
    Dissolving ores containing gold and silver in an ionic liquid of the type bmim + (X) (with X '= Cl', HSO4 ', CH3SO3', N (CN) 2) in the presence of thiourea, or of another sulfur compound, and iron (III) sulfate has been previously studied (Whitehead et al., Green Chem., 2004, 6, 313-315 and Whitehead et al., Hydrometallurgy, 2007, 88, 109-120). ).
    Some articles relate to the recovery of silver by electroplating in chloroaluminate ionic liquids (Xu et al., J. Electrochem Soc., 1992, 139, 5, 1295-1300), and in ionic liquid-based liquids. choline chloride (Abbott et al., Phys Chem Chem Phys., 2007, 9, 3735-3743).
    These articles concern either the dissolution of silver or the electrodeposition of silver, but none discloses a process combining these two stages.
    The method of the invention relates to the recycling of photovoltaic cells and couples, advantageously, both the dissolution and the electrolytic recovery of silver in the same ionic liquid, in the presence of a redox mediator. This process by green chemistry does not use sulfur compounds.
    The recycling process is applicable to photovoltaic cells of crystalline type, of crystalline silicon for example, or of polycrystalline type, polycrystalline silicon for example. It can also be used for any type of amorphous silicon substrate containing silver.
    Photovoltaic cells come from a photovoltaic panel or module.
    The photovoltaic cell is recovered after separation and separation of the photovoltaic cells of a photovoltaic panel and after removal of the junction boxes, and the metal frame of the photovoltaic panel. Once the photovoltaic cells are disconnected, they are advantageously disconnected from each other and possibly electrical connectors containing no money. The silver, present in the photovoltaic cells, comes especially from the electrodes, made for example with a silver metallization paste, as well as electrical connectors. The connectors are for example formed of a copper core coated with Sn62Pb36Ag2.
    Before step a), a heat treatment is advantageously carried out so as to eliminate the polymer elements, for example ethyl vinyl acetate (EVA) present in the photovoltaic cell. The heat treatment can be carried out in an oven.
    The remaining elements of the photovoltaic cell are then milled during step a), so as to obtain a ground material containing the silver particles.
    By silver particles is meant silver in solid form. The particles may have different dimensions depending on the grinding conditions chosen. They will nevertheless be small enough to have a large surface area and be dissolved in the dissolution solution more easily.
    They will advantageously have a size less than 1 centimeter. Size is the largest dimension of the particle, usually the diameter or length.
    Some photovoltaic cells include an aluminum frame and / or aluminum connectors.
    In this particular embodiment, after step a) and before step b), a step of dealumination in aqueous medium is advantageously carried out. For this, the ground material is immersed in an acidic solution, having a pH ranging from 0 to 4, to dissolve the aluminum present in the photovoltaic cell and separate it from the ground material.
    The solid / liquid ratio is between 1% and 45%, and preferably the solid / liquid ratio is between 1% and 30%. This ratio is noted S / L. Preferably, the S / L ratio is of the order of 10%. By 10% is meant 10% ± 1%.
    The solid phase corresponds to the aluminum to be dissolved. The liquid phase corresponds to the acidic solution.
    This ratio corresponds to the mass of solid, i.e. the mass of metal oxide, in grams, divided by the volume of the solution, in milliliters.
    Thus, a S / L ratio of between 1% and 30% corresponds to a mass concentration of the metal oxide in the acid solution of between 0.01 g / ml and 0.3 g / ml.
    For S / L values below 1%, the dissolution efficiency is also high. However, the amount of acid used is considerably high relative to the amount of metal to be dissolved, and the amount of reagents lost is substantial.
    The temperature of the acid solution is advantageously between 20 ° C and 80 ° C. It is preferably of the order of 25 ° C to minimize the toxicity and reduce the energy consumption of the process. Silver is not or very little dissolved in the acid solution. It is considered that the dissolution of silver is negligible during this stage.
    In step b), the silver is dissolved in a solution containing at least one ionic liquid and a redox mediator and, optionally, water.
    Ionic liquid is understood to mean a solvent comprising at least one cation and an anion whose combination generates a liquid with a melting point below 100 ° C. An ionic liquid is a non-volatile and non-flammable liquid.
    The cation is advantageously chosen from the following families: imidazolium, pyrrolidinium, ammonium, piperidinium and phosphonium.
    Preferably, the cation is an imidazolium. This cation is stable up to a cathodic potential large enough to achieve electrochemical deposition of silver, during step d).
    Its combination with different anions meets the requirements of thermal stability (above 200 ° C) and chemical stability (no hydrolysis). It is liquid at room temperature with many associations of anions. Its conductivity is satisfactory for a large number of anions.
    By ambient temperature is meant a temperature of the order of 20-25 ° C. The anion can be organic or inorganic. The anion is preferably a complexing agent of the silver metal. There is no need to introduce in addition, in solution, another complexing agent.
    The solution is advantageously free of sulfur compounds. It has been discovered that the anion of the ionic liquid is sufficiently complexing not to use sulfur compounds, as in the prior art. The complexing species can remain in solution throughout the process and the solution, after electrodeposition and regeneration, can be used again for a recycling process. The anion is advantageously chosen from halides (Cl '' Br ', Γ), thiocyanate, tricyanomethanide and dicyanamide.
    These particular complexing agents, intrinsically present in the ionic liquid, advantageously have improved solubility and chemical stability with respect to sulfur-containing complexing agents such as thiourea or thiosulfate. Preferably, the anion is a halide, and even more preferentially, it is the chloride anion.
    Advantageously, the anodic stability of the chlorides is greater than that of many other complexing agents. More powerful oxidants can therefore be used to improve the kinetics of leaching.
    An ionic liquid containing chlorides, iodides or bromides will be soluble in a solution containing water, since this small anion can more easily form hydrogen bonds with water. The chloride anion will be preferred for a green chemistry process.
    High purity metallic silver (99.99%) was chemically dissolved in ionic liquids BMIM [X] ([X] = [DCA], [Cl], [Br] and [I]). BMIM represents the 1-butyl-3-methylimidazolium cation and DCA represents the dicyanamide anion.
    The silver dissolution rates were set at room temperature for stirring at 400 rpm and under an inert atmosphere.
    The knowledge of the surface of the immersed silver wires has made it possible to define an average dissolution rate of silver over a period of 5 hours (in mgAg.h'1.cm'2) assuming that the surface variation is negligible. . The dissolution results indicate that the rate decreases according to the anion of the ionic liquid such that: Γ (8,15 mgAg.cm'2Ag.h'1)> Cl '(5,45) * Br' (5,40) > DCA '(1,55) For comparison, tests in HNO3 medium were carried out at 1 mol.L'1 and 4 mol.L'1 under the same operating conditions. The results show that at room temperature the dissolution of silver is zero in these environments.
    The ionic liquid has a concentration of between 0.1 mol / l and 10 mol / l, preferably between 1 mol / l and 10 mol / l, and even more preferably between 1 mol / l and 5 mol / l.
    Such concentrations represent a good compromise between the amount of reagents necessary to promote the complexation of silver in solution, and the obtaining of a solution having good transport properties. Such concentrations promote the dissolution kinetics of silver.
    According to one particular embodiment, the solution comprises two ionic liquids, the first ionic liquid acting as a neutral support and the second ionic liquid acting as a complexing agent.
    The first ionic liquid is, for example, bis (trifluoromethane) sulfonamide imide, also called NTf2.
    Advantageously, such an ionic liquid does not present a problem of hydrolysis with water, as is the case, for example, for ionic liquids comprising anions of tetrafluoroborate, which during hydrolysis lead to the formation of HF. .
    In addition to the ionic liquid, the solution comprises a redox mediator.
    Redox mediator means an ion in solution capable of being reduced during the leaching or dissolution of silver and being oxidized during electrolysis.
    The redox mediator is, advantageously, a dissolved metal salt in solution, chosen from iron, copper, ruthenium, silver, tin, cobalt, vanadium, chromium, cobalt, and manganese.
    The metal salt is preferably an iron (III) salt, for example FeCl3, or a copper (II) salt, such as copper (II) sulphate.
    These salts are soluble in ionic liquids in their two oxidation states (Fe2 + / Fe3 + or Cu + / Cu2 +). They do not degrade ionic liquids and are not toxic, unlike conventional reducing agents which degrade during the dissolution reaction, as is the case, for example with HNO3 which causes the generation and irreversible consumption of nitrates with NOx formation.
    These redox mediators have adequate redox potentials. Adequate means that the redox potentials of the couples are sufficiently high without reaching the anode window of the ionic liquids.
    These redox mediators do not settle with silver during electroplating. They remain in solution, which allows a full recovery of money in pure form.
    According to a preferred embodiment, the solution further comprises water. The presence of water improves the transport conditions (viscosity, ionic conductivity) of the solution.
    The solution may comprise from 0% to 90% molar water.
    The percentage of water relative to the ionic liquid is advantageously less than 50 mol%, and preferably of the order of 10 mol%.
    The amount of water added depends on the nature of the ionic liquids. The water will be added to the ionic liquid as much as possible until the ionic liquid is saturated with water.
    For a solution containing water, the cation of the ionic liquid is, advantageously, an imidazolinium and the anion is a halide, and even more preferably, a chloride anion.
    These elements are, advantageously, soluble in water. In addition, this type of ionic liquid has a complexing power strong enough to promote leaching while not requiring too much energy to perform the electroplating of silver. The introduction of the silver particles into the solution containing at least the ionic liquid and the redox mediator causes the immediate dissolution of the silver by a redox mechanism with the mediator - step b). The dissolution step is carried out at a temperature between 15 ° C and 80 ° C, and preferably at room temperature, that is to say of the order of 25 ° C. There is, advantageously, no need for thermal energy input to achieve the dissolution of silver. However, an increase in temperature can be advantageously carried out to improve the dissolution rate without degradation of the medium (for temperatures between 15 and 80 ° C).
    The process steps are also carried out at ambient pressure, that is to say at a pressure of the order of 1 bar.
    The process is carried out under air.
    The solid / liquid ratio, during the dissolution of silver, is between 1% and 45%, and preferably, the solid / liquid ratio is between 1% and 30%. Preferably, this ratio is of the order of 10%. By 10% is meant 10% ± 1%.
    The solid phase is money. The liquid phase corresponds to the solution.
    After dissolution of the silver, the ground material, free of silver, is extracted from the bath by solid-liquid separation - step c). The silver can then be recovered and the redox mediator can be regenerated by electrolysis during step d). At the negative electrode, silver is deposited in metallic form. Simultaneously, the positive electrode is the seat of oxidation of the redox mediator which is regenerated. The negative electrode is, advantageously, stainless steel, carbon, titanium, silver or a noble metal. The positive electrode is, advantageously, steel, carbon or a noble metal.
    Advantageously, during this step, the ionic liquid plays the role of ionic conductor, thus avoiding the supply of conductive salt.
    As shown in FIG. 1, silver was electrodeposited in ionic liquids BMIM [X] ([X] = [DCA], [Cl], [Br] and [I]). All these ionic liquids are suitable for the electrochemical deposition of silver. The potentials differ according to the nature of the anion of the ionic liquid:
    Edca (0.1 V vs. Ag / AgCl)> ECi (-0.25V)> EBr (-0.60V)> E, (-0.80V) The energy supply will advantageously be limited to electroplate silver in an ionic liquid whose anion is a chloride ion.
    After step d), the solution containing the ionic liquid and the regenerated redox mediator is then usable for a new treatment.
    The process will now be described with the aid of the following example given by way of illustration and not limitation.
    The photovoltaic cells are first heat-treated to burn the EVA and separate the cells from the connectors. This step takes place in an oven under air at 500 ° C for 1 hour.
    The collected cells are then milled using a ball mill (step a). The cells are immersed in a sulfuric acid solution at 1 mol.L'1 with a solid / liquid ratio of 10% (g / ml) and with constant control of the pH. The reaction lasted 24 h at 25 ° C. with stirring at 400 rpm.
    The solid and liquid phases are then separated by centrifugation and filtration.
    The volume of the liquid phase was adjusted in a volumetric flask and the solution was analyzed by plasma torch spectrometry coupled to optical emission spectrometry (or ICP-OES for Inductively Coupled Plasma Optical Emission Spectrometry). ). At the end of the treatment, aluminum, zinc and boron were completely dissolved.
    The solid phase was put in an oven. The solid is then introduced into an ionic liquid medium of butyl-methyl-imidazolium chloride (BMIMCI) in which iron chloride (FeCl 3) is dissolved at a concentration of 0.15 mol.l -1 with 10 mol% of water. (step b). The solution is liquid at room temperature. The solid is immersed in the ionic liquid solution with a solid / liquid ratio of 10% (g / ml). The reaction lasted 24 h at 25 ° C. with stirring at 400 rpm. The solid (silicon enriched) and liquid phases were then separated by filtration after complete dissolution of the silver (step c).
    The liquid phase was then used to deposit silver on glassy carbon (step d). A three electrode mounting is used. The working electrode and the counter electrode are glassy carbon. The potential is maintained at -1.2V for three hours (potentiostatic mode) with stirring at 100rpm, which makes it possible, preferentially, to reduce the silver on the vitreous carbon electrode. The deposition is directly analyzed by scanning electron microscopy (SEM) and by energy dispersive analysis (EDX) analysis ("Energy-dispersive X-ray spectroscopy"). Figure 2 shows a snapshot of the microstructure of the deposit. The structure of the silver deposit is of the "cauliflower" type. The EDX analysis in Figure 3 confirms that this is a deposit of money. This deposit of silver contains some impurities of lead, iron and chlorides. These residual impurities will be mostly removed after a washing of the silver deposit in water. The deposit of silver is insoluble in water.
    Before washing, the semi-quantitative analysis by EDX indicates that the silver content is greater than 90% to reach a higher grade, after washing the trapped elements in the silver deposit. There is also the absence of copper and aluminum in the deposit. Unlike the existing processes, this method of valorization of silver by green chemistry does not use concentrated acid or concentrated base and can be carried out at room temperature, which reduces the energy input necessary for realization of the different stages. There is no release of harmful gases.
    权利要求:
    Claims (18)
    [1" id="c-fr-0001]
    claims
    1. Method for recycling the silver present in a photovoltaic cell comprising the following successive steps: a) crushing the photovoltaic cell, so as to form a ground containing silver particles, b) dissolving the silver contained in the ground material in a solution containing: o at least one ionic liquid, o a redox mediator, o optionally water, the dissolution leading to the formation of silver ions in solution, c) separating the ground material from the solution, d) carrying out a electrolysis of the solution to reduce silver ions and regenerate the redox mediator.
    [2" id="c-fr-0002]
    2. Method according to the preceding claim, characterized in that the dissolving step is carried out at a temperature between 15 ° C and 80 ° C, and preferably of the order of 25 ° C.
    [3" id="c-fr-0003]
    3. Method according to any one of the preceding claims, characterized in that the redox mediator is a metal salt selected from iron, copper, ruthenium, silver, tin, cobalt, vanadium, chromium, cobalt, and manganese.
    [4" id="c-fr-0004]
    4. Method according to the preceding claim, characterized in that the metal salt is an iron salt (III) or a copper salt (II).
    [5" id="c-fr-0005]
    5. Method according to any one of the preceding claims, characterized in that the ionic liquid is formed of a cation and an anion, the cation being chosen from imidazolium, pyrrolidinium, ammonium, piperidinium and phosphonium, the anion being selected from halides, thiocyanate, tricyanomethanide and dicyanamide.
    [6" id="c-fr-0006]
    6. Method according to the preceding claim, characterized in that the cation is an imidazolium and in that the anion is a halide.
    [7" id="c-fr-0007]
    7. Method according to any one of the preceding claims, characterized in that the solution is free of sulfur compounds.
    [8" id="c-fr-0008]
    8. Method according to any one of the preceding claims, characterized in that during step d), the negative electrode is made of stainless steel, carbon, titanium, silver or a noble metal.
    [9" id="c-fr-0009]
    9. Method according to any one of the preceding claims, characterized in that during step d), the positive electrode is steel, carbon or a noble metal.
    [10" id="c-fr-0010]
    10. Method according to any one of the preceding claims, characterized in that the photovoltaic cell is a crystalline silicon cell or polycrystalline silicon.
    [11" id="c-fr-0011]
    11. Method according to any one of the preceding claims, characterized in that, before step a), a heat treatment is performed so as to remove the polymer elements present in the photovoltaic cell.
    [12" id="c-fr-0012]
    12. Method according to any one of the preceding claims, characterized in that, after step a), the ground material is immersed in an acidic solution, having a pH ranging from 0 to 4, to dissolve aluminum present in the photovoltaic cell and separate it from the ground.
    [13" id="c-fr-0013]
    13. Method according to the preceding claim, characterized in that the temperature of the acid solution is between 20 ° C and 80 ° C.
    [14" id="c-fr-0014]
    14. Method according to one of claims 12 and 13, characterized in that the solid / liquid ratio is between 1% and 30%, and preferably, the solid / liquid ratio is of the order of 10%.
    [15" id="c-fr-0015]
    15. Process according to any one of the preceding claims, characterized in that the percentage of water, in the solution, relative to the ionic liquid is less than 50 mol%, and preferably of the order of 10 mol%. .
    [16" id="c-fr-0016]
    16. Process according to any one of the preceding claims, characterized in that the ionic liquid has a concentration of between 0.1 mol / l and 10 mol / l, preferably between 1 mol / l and 10 mol / l, and even more preferentially between 1 mol / L and 5mol / L.
    [17" id="c-fr-0017]
    17. Process according to any one of the preceding claims, characterized in that the solution comprises two ionic liquids, the first ionic liquid acting as a neutral support and the second ionic liquid acting as a complexing agent.
    [18" id="c-fr-0018]
    18. Method according to the preceding claim, characterized in that the first ionic liquid is bis (trifluoromethane) sulfonamide imide.
    类似技术:
    公开号 | 公开日 | 专利标题
    EP3178576B1|2020-09-30|Method for recycling the silver contained in a photovoltaic cell
    US20100101964A1|2010-04-29|Method of Recovering Valuable Metal from Scrap Containing Conductive Oxide
    US8308932B2|2012-11-13|Method of recovering valuable metals from IZO scrap
    US20100282615A1|2010-11-11|Method of Recovering Valuable Metals from IZO Scrap
    CN102839391B|2015-10-21|High purity indium preparation method
    EP3023158B1|2017-04-26|Method for recovering silver contained in a silicon substrate
    Liu et al.2021|Recycling and recovery of perovskite solar cells
    EP3263744B1|2019-05-15|Process for the recovery of platinum, electrochemically, from a material which contains same
    CH679158A5|1991-12-31|
    EP2901495A2|2015-08-05|Mixed bismuth and copper oxides and sulphides for photovoltaic use
    JP4323297B2|2009-09-02|Method for producing electrolytic copper powder
    FR3065230B1|2019-06-14|PROCESS FOR RECOVERING SILVER PRESENT ON A SUBSTRATE, ELECTROCHEMICALLY, IN THE PRESENCE OF AN IONIC LIQUID
    RU2423557C2|2011-07-10|Procedure for production of high and nano dispersed powder of metals or alloys
    FR2691980A1|1993-12-10|Direct electrochemical refining process of copper waste.
    EP3388555B1|2020-02-12|Process for selective recovery of silver in the presence of aluminium, electrochemically and in aqueous solution
    KR101629918B1|2016-06-13|Electrolytic apparatus for electro-refining and recovery of platinum metals, and method thereof
    FR3065228B1|2019-06-14|PROCESS FOR RECOVERING SILVER PRESENT ON SUBSTRATE, ELECTROCHEMICALLY AND IN AQUEOUS SOLUTION
    EP3555345B1|2021-07-07|Electrolytic method for extracting tin or simultaneously extracting tin and lead contained in an electrically conductive mixture
    Pruksathorn et al.2005|Lead recovery from waste frit glass residue of electronic plant by chemical-electrochemical methods
    JP2011106010A|2011-06-02|Method for separating indium from tin by using organic solvent
    WO2018071856A1|2018-04-19|Metal deposits, compositions, and methods for making the same
    Popescu et al.2016|Preliminary Study for Copper Recovery in WEEE Leachate by Using Ionic Liquids Based on Choline Chloride
    FR3099492A1|2021-02-05|PROCESS FOR RECOVERING RHODIUM BY ELECTROCHEMICAL
    Stepanov et al.2013|Synthesis of layered metal dichalcogenides with organic cations by electrochemical reduction in suspensions
    US11274374B2|2022-03-15|Metal deposits, compositions, and methods for making the same
    同族专利:
    公开号 | 公开日
    ES2828980T3|2021-05-28|
    EP3178576A1|2017-06-14|
    FR3044941B1|2018-02-02|
    EP3178576B1|2020-09-30|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    DE2025211A1|1970-05-23|1971-12-02|Kraft J|Selective anodic recovery of silver - from scrap by electro - -deposition from aq soln|
    US4288304A|1975-04-21|1981-09-08|Societe Miniere Et Metallurgique De Penarroya|Hydrometallurgical process for treatment of sulphur ores|
    CA2908046A1|2013-03-28|2014-10-02|Yava Technologies Inc.|Integrated recovery of metals from complex substrates|CN111719050A|2020-07-07|2020-09-29|昆明理工大学|Method for comprehensively recovering water-soluble zinc and silver in zinc leaching residues|JP2005311178A|2004-04-23|2005-11-04|Sharp Corp|Extraction method of solar cell board material, regenerating method of solar cell, and formation method of ingot for solar cell|
    KR101092259B1|2009-12-18|2011-12-12|한국화학연구원|Methode for recycling silicon from waste solar cell|
    CN102343352B|2010-07-26|2014-03-12|比亚迪股份有限公司|Recovery method for solar silicon slice|
    KR101256574B1|2011-11-14|2013-04-19|한국화학연구원|Method for recycling silicon from waste solar module|
    CN102851506A|2012-08-12|2013-01-02|安阳市凤凰光伏科技有限公司|Method for extracting and recovering silver from waste solar cell|CN107312942B|2017-07-04|2018-10-23|东北大学|The method of extraction and separation vanadium and chromium from vanadium chromium slag pickle liquor|
    CN108893602A|2018-07-12|2018-11-27|汉能新材料科技有限公司|The separation method of the solar battery of de- envelope|
    CN111621648B|2019-02-28|2021-08-31|中国科学院化学研究所|Silver solution and preparation method thereof|
    FR3102679A1|2019-10-31|2021-05-07|Commissariat A L'energie Atomique Et Aux Energies Alternatives|PROCESS FOR RECOVERING PLATINOID PARTICLES CONTAINED IN AN ELECTRICALLY INSULATING SUPPORT|
    法律状态:
    2016-12-29| PLFP| Fee payment|Year of fee payment: 2 |
    2017-06-16| PLSC| Publication of the preliminary search report|Effective date: 20170616 |
    2018-01-02| PLFP| Fee payment|Year of fee payment: 3 |
    2019-12-31| PLFP| Fee payment|Year of fee payment: 5 |
    2020-12-28| PLFP| Fee payment|Year of fee payment: 6 |
    2021-12-31| PLFP| Fee payment|Year of fee payment: 7 |
    优先权:
    申请号 | 申请日 | 专利标题
    FR1562252|2015-12-11|
    FR1562252A|FR3044941B1|2015-12-11|2015-12-11|PROCESS FOR RECYCLING SILVER PRESENT IN A PHOTOVOLTAIC CELL|FR1562252A| FR3044941B1|2015-12-11|2015-12-11|PROCESS FOR RECYCLING SILVER PRESENT IN A PHOTOVOLTAIC CELL|
    ES16202859T| ES2828980T3|2015-12-11|2016-12-08|Procedure for recycling the silver present in a photovoltaic cell|
    EP16202859.1A| EP3178576B1|2015-12-11|2016-12-08|Method for recycling the silver contained in a photovoltaic cell|
    [返回顶部]