CN105755288B - A kind of method that zinc in discarded cathodic ray-tube fluorescent powder is reclaimed based on self-propagating reaction and rare earth is enriched with - Google Patents
A kind of method that zinc in discarded cathodic ray-tube fluorescent powder is reclaimed based on self-propagating reaction and rare earth is enriched with Download PDFInfo
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Abstract
Description
技术领域technical field
本发明涉及从废弃阴极射线管荧光粉中回收锌的方法,特别是涉及采用自蔓延反应绿色回收废弃阴极射线管荧光粉中的锌并富集稀土的方法,属于锌的回收技术领域。The invention relates to a method for recovering zinc from waste cathode ray tube fluorescent powder, in particular to a method for recycling zinc in waste cathode ray tube fluorescent powder by self-propagating reaction green and enriching rare earth, belonging to the technical field of zinc recovery.
背景技术Background technique
伴随着显示器技术的飞速发展,阴极射线管显示器已经进入大量报废阶段。据有关统计,仅2013年我国阴极射线管显示器报废量就超过了3000万台。平均每台完整的阴极射线管屏玻璃中一般含有荧光粉的质量为1-7g,废弃阴极射线管荧光粉主要成分为w(ZnS)55~60%,w(Y2O2S:Eu)25~30%,w(SiO2)2~8%,w(Al)2~5%及少量其他微量杂质元素。锌等重金属通常具有急性或慢性毒性,焚烧、填埋或随意丢弃不仅造成资源浪费,并且导致土壤或水体污染,对动植物造成极大危害。With the rapid development of display technology, cathode ray tube displays have entered a large number of scrapping stages. According to relevant statistics, in 2013 alone, more than 30 million CRT monitors were scrapped in my country. The average mass of fluorescent powder contained in each complete cathode ray tube screen glass is 1-7g, and the main components of waste cathode ray tube fluorescent powder are w(ZnS) 55-60%, w(Y 2 O 2 S:Eu) 25-30%, w(SiO 2 ) 2-8%, w(Al) 2-5%, and a small amount of other trace impurity elements. Heavy metals such as zinc are usually acutely or chronically toxic. Incineration, landfilling or random discarding not only cause waste of resources, but also lead to soil or water pollution, causing great harm to animals and plants.
目前,针对废弃阴极射线管荧光粉的回收利用研究尚处于起步阶段,现有研究主要集中于阴极射线管荧光粉回收稀土元素,针对锌的回收利用谈及较少(专利申请发明专利201210300550.6、201210134477.X)。马琳提出的回收阴极射线管荧光粉方法中(专利申请201110140164.0),采用稀硫酸溶解稀土及锌等元素,用氢氟酸过滤回收稀土氟化物,同时提到通过调节滤液PH获得铝、锌、镉的混合氢氧化物,但此方法并未提出具体分离回收锌的步骤,同时浸出过程放出大量有毒气体H2S,导致严重的环境污染及安全问题,增加了废气处理难度。王勤在专利中(专利申请201110143325.1)指出,首先煅烧氧化处理,加酸浸出金属元素,磷酸根回收稀土,采用碳酸钠沉淀回收锌元素,此方法虽然避免了H2S的排放,但煅烧过程产生大量SO2,同样造成严重的环境污染及安全问题,增加了废气处理难度。张深根提出一种去除废旧稀土荧光粉中玻璃渣和硅铝氧化物的方法(专利申请201410022560.7),提出采用筛分和热碱浸出工艺去除废旧稀土荧光粉中的粗中细颗粒玻璃渣和其他硅铝氧化物杂质,为本专利提供前期预处理工艺支撑。At present, the research on the recycling of waste cathode ray tube phosphor powder is still in its infancy. The existing research mainly focuses on the recovery of rare earth elements from cathode ray tube phosphor powder, and there is little talk about the recycling of zinc (patent application for invention patent 201210300550.6, 201210134477 .X). In the method of recycling cathode ray tube fluorescent powder proposed by Ma Lin (patent application 201110140164.0), dilute sulfuric acid is used to dissolve elements such as rare earth and zinc, and rare earth fluoride is recovered by filtration with hydrofluoric acid. At the same time, it is mentioned that aluminum, zinc, and cadmium can be obtained by adjusting the pH of the filtrate. However, this method does not propose a specific step for separating and recovering zinc. At the same time, a large amount of toxic gas H 2 S is released during the leaching process, which leads to serious environmental pollution and safety problems, and increases the difficulty of waste gas treatment. Wang Qin pointed out in the patent (patent application 201110143325.1) that firstly the calcination oxidation treatment is carried out, the metal elements are leached out by adding acid, the rare earth is recovered by phosphate, and the zinc element is recovered by sodium carbonate precipitation. Although this method avoids the emission of H 2 S, the calcination process A large amount of SO 2 is produced, which also causes serious environmental pollution and safety problems, and increases the difficulty of waste gas treatment. Zhang Shengen proposed a method for removing glass slag and silicon-aluminum oxides in waste rare earth phosphors (patent application 201410022560.7), and proposed to use screening and hot alkali leaching process to remove coarse, medium and fine particles of glass slag and other silica in waste rare earth phosphors. Aluminum oxide impurities provide support for the pre-treatment process for this patent.
可见,现有废弃阴极射线管荧光粉回收研究尚存在较多问题。首先,现有回收过程普遍能耗较高,如煅烧预处理工艺,且对设备要求严格,如碱熔等步骤;其次,回收过程不可避免的造成硫元素污染问题,如酸浸过程产生危险气体H2S,而煅烧处理又不可避免产生大量SO2,在高能耗的同时造成严重的环境及安全问题;同时,现有研究集中体现在稀土元素的回收利用,而主要元素Zn同样以离子形式与稀土元素共同进入到溶液中,回收过程不仅造成了稀土离子与Zn离子的分离问题,同时在回收稀土后导致大量锌资源的浪费。It can be seen that there are still many problems in the existing research on the recycling of phosphor powder from waste cathode ray tubes. First of all, the existing recovery process generally consumes a lot of energy, such as the calcination pretreatment process, and has strict requirements on equipment, such as alkali fusion and other steps; secondly, the recovery process inevitably causes sulfur pollution, such as the acid leaching process produces dangerous gases H 2 S, and the calcination process inevitably produces a large amount of SO 2 , which causes serious environmental and safety problems while high energy consumption; at the same time, the existing research focuses on the recovery and utilization of rare earth elements, and the main element Zn is also in the form of ions Into the solution together with rare earth elements, the recovery process not only caused the separation of rare earth ions and Zn ions, but also caused a lot of waste of zinc resources after recovery of rare earth ions.
本发明的目的主要解决废弃阴极射线管荧光粉中锌回收问题,不仅能够保证有效回收锌有价金属,而且实现稀土资源的有效富集,在提高回收经济价值的同时,实现处理工艺流程短、能耗低、二次污染少等工艺优势。采用自蔓延法回收废弃阴极射线管荧光粉中的锌可有效避免现有工艺带来的环境、安全、能耗等问题,自蔓延为自发反应,反应速度快、反应能耗低,产物稳定,可以回收大量的锌资源,提高附加值,同时富集稀土资源,相对现有技术大大提高后续稀土回收的效率。The purpose of the present invention is mainly to solve the problem of zinc recovery in waste cathode ray tube fluorescent powder, not only to ensure the effective recovery of zinc valuable metals, but also to achieve effective enrichment of rare earth resources, while improving the economic value of recovery, to achieve a short process flow, Low energy consumption, less secondary pollution and other process advantages. Using the self-spreading method to recover zinc in waste cathode ray tube phosphors can effectively avoid the environmental, safety, energy consumption and other problems caused by the existing process. Self-spreading is a spontaneous reaction with fast reaction speed, low reaction energy consumption and stable products. A large amount of zinc resources can be recovered, the added value can be increased, and rare earth resources can be enriched at the same time, which greatly improves the efficiency of subsequent rare earth recovery compared with the existing technology.
发明内容Contents of the invention
本发明的目的主要解决废弃阴极射线管荧光粉中锌回收问题,不仅能够保证有效回收锌有价金属,而且实现稀土资源的有效富集,在提高回收经济价值的同时,实现处理工艺流程短、能耗低、二次污染少等工艺优势。The purpose of the present invention is mainly to solve the problem of zinc recovery in waste cathode ray tube fluorescent powder, not only to ensure the effective recovery of zinc valuable metals, but also to achieve effective enrichment of rare earth resources, while improving the economic value of recovery, to achieve a short process flow, Low energy consumption, less secondary pollution and other process advantages.
本发明所述的种基于自蔓延反应回收废弃阴极射线管荧光粉中锌的方法如下:A method of reclaiming zinc in waste cathode ray tube fluorescent powder based on self-propagating reaction of the present invention is as follows:
步骤一:预处理除铝硅Step 1: Pretreatment to remove aluminum and silicon
将回收获得的废弃阴极射线管荧光粉进行初级筛分,采用热碱液浸出其中的细玻璃渣和铝及其他硅铝杂质;Perform primary screening on the recovered waste cathode ray tube fluorescent powder, and use hot alkaline solution to leach the fine glass slag, aluminum and other silicon-aluminum impurities;
步骤二:自蔓延反应Step 2: Self-propagating reaction
将步骤一碱浸渣干燥后得到的初级富集粉细磨,与氧化剂(氧化剂为过氧化钠、过氧化钾等碱金属过氧化物或超氧化物中的一种或混合物)按照质量比1:0.5~1:5混合,搅拌均匀;将混合粉置于耐高温反应容器中,引发自蔓延反应;在此步骤中,通过自蔓延氧化还原反应,硫化锌中锌元素转化为可溶于碱性溶液的锌盐,而硫元素直接被氧化生成硫酸盐而避免了酸浸和高温焙烧处理时产生硫化氢、二氧化硫等有毒有害气体,大大降低了回收过程的二次污染。Finely grind the primary enrichment powder obtained after step one alkali leaching residue is dried, and oxidant (oxidant is one or a mixture of alkali metal peroxides or superoxides such as sodium peroxide and potassium peroxide) according to the mass ratio of 1 : 0.5~1:5 mixing, stirring evenly; put the mixed powder in a high temperature resistant reaction container to trigger a self-propagating reaction; in this step, through a self-propagating redox reaction, the zinc element in zinc sulfide is transformed into a soluble The zinc salt of the neutral solution, and the sulfur element is directly oxidized to form sulfate, which avoids the generation of toxic and harmful gases such as hydrogen sulfide and sulfur dioxide during acid leaching and high-temperature roasting, and greatly reduces the secondary pollution in the recycling process.
步骤三:选择性浸取锌Step 3: Selective leaching of zinc
步骤二冷却后的反应产物与去离子水按固液比1:20~1:100(g/mL)混合浸取,水溶液呈碱性,直接用于体系中Zn的浸出,搅拌结束后过滤,以碱液和水依次冲洗沉淀,洗液并入此过程的滤液,获得含锌滤液,滤渣收集后干燥获得稀土富集渣。特别的,可通过补加NaOH调节浸出过程浸出溶液中NaOH质量浓度2%~10%,以保证ZnO全部浸出。进一步的,浸取体系在20~80℃下进行搅拌处理,搅拌时间0.5~4h。The cooled reaction product in step 2 is mixed and leached with deionized water at a solid-to-liquid ratio of 1:20 to 1:100 (g/mL). The aqueous solution is alkaline and is directly used for the leaching of Zn in the system. After the stirring is completed, filter. Rinse the precipitate with lye and water in sequence, add the washing liquid to the filtrate of this process to obtain a zinc-containing filtrate, collect the filter residue and dry it to obtain a rare earth enriched residue. In particular, the mass concentration of NaOH in the leaching solution during the leaching process can be adjusted to 2%-10% by adding NaOH to ensure that all ZnO is leached. Further, the leaching system is stirred at 20-80° C. for 0.5-4 hours.
经过以上步骤一到步骤三过程,稀土富集渣中稀土元素质量含量由初始的<10%提高到>60%。Through the above steps 1 to 3, the mass content of rare earth elements in the rare earth enriched slag is increased from <10% initially to >60%.
步骤四:回收制备氧化锌Step 4: Recovery and preparation of zinc oxide
步骤三中的含锌滤液中含有高浓度的Zn(OH)4 2-,通过加酸调节PH使其以Zn(OH)2形式沉淀,杂质元素Na+和SO4 2-留在滤液中,过滤后煅烧制备ZnO粉末。The zinc-containing filtrate in step 3 contains a high concentration of Zn(OH) 4 2- , which is precipitated in the form of Zn(OH) 2 by adding acid to adjust the pH, and the impurity elements Na + and SO 4 2- remain in the filtrate, Calcination after filtration to prepare ZnO powder.
自蔓延引发方式采用化学点火、燃烧波点火、局部加热点火、激光点火、热爆点火或微波点火等方法中的一种。The self-propagating initiation method adopts one of methods such as chemical ignition, combustion wave ignition, local heating ignition, laser ignition, thermal explosion ignition or microwave ignition.
采用预处理-硫化锌自蔓延反应-水浸提锌-沉淀煅烧制备再生氧化锌的绿色回收废弃阴极射线管荧光粉中锌的方法。将回收获得的废弃阴极射线管荧光粉进行预处理除铝硅,除铝硅后的废弃阴极射线管荧光粉与氧化剂混合,置于耐高温反应容器中,引发自蔓延反应;水溶反应产物并搅拌,过滤混合液获得含锌浸取液和稀土富集渣;浸取液调节pH,沉淀回收Zn(OH)2;煅烧Zn(OH)2获得ZnO粉末,锌综合回收率高达98%。本发明具有工艺简单易行,所用原料和设备都比较常见且廉价;能耗极低且实现内部循环利用;绿色环保,避免有害气体SO2、H2S的产生;有效回收有价金属锌,同时实现了稀土资源的高效富集。A green method for recovering zinc in waste cathode ray tube fluorescent powder by using pretreatment-zinc sulfide self-propagating reaction-water leaching to extract zinc-precipitation and calcination to prepare regenerated zinc oxide. The waste cathode ray tube fluorescent powder obtained by recycling is pretreated to remove aluminum and silicon, and the waste cathode ray tube fluorescent powder after aluminum and silicon removal is mixed with an oxidant, and placed in a high temperature resistant reaction container to initiate a self-propagating reaction; the reaction product is dissolved in water and stirred , filter the mixed solution to obtain zinc-containing leaching solution and rare earth enrichment slag; adjust the pH of the leaching solution, precipitate and recover Zn(OH) 2 ; calcinate Zn(OH) 2 to obtain ZnO powder, and the comprehensive recovery rate of zinc is as high as 98%. The invention has the advantages of simple and easy process, and the raw materials and equipment used are relatively common and cheap; the energy consumption is extremely low and the internal recycling can be realized; the environmental protection can avoid the generation of harmful gases SO 2 and H 2 S; the valuable metal zinc can be recovered effectively, At the same time, the efficient enrichment of rare earth resources is realized.
本发明具有工艺简单易行,所用原料和设备都比较常见且廉价,能耗极低且实现内部循环利用,在回收有价金属锌的同时,实现了稀土资源的高效富集。The invention has the advantages of simple and easy process, common and cheap raw materials and equipment, extremely low energy consumption, internal recycling, and efficient enrichment of rare earth resources while recovering the valuable metal zinc.
附图说明Description of drawings
图1表示一种基于自蔓延反应回收废弃阴极射线管荧光粉中的锌并富集稀土的方法的流程图。Fig. 1 shows a flow chart of a method for recovering zinc in waste cathode ray tube phosphors and enriching rare earths based on self-propagating reaction.
具体实施方式detailed description
下面结合实施例对本发明进行说明,但本发明并不仅限于以下实施例。The present invention is described below in conjunction with the examples, but the present invention is not limited to the following examples.
实施例1Example 1
将回收获得的废弃阴极射线管荧光粉进行初级筛分,采用热碱液浸出其中的细玻璃渣和铝及其他硅铝杂质。除铝硅后的废弃阴极射线管荧光粉与过氧化钠按质量比1:0.5混合,置于耐高温反应容器中,滴水引发自蔓延反应;按固液比1:20(g/mL)水溶反应产物,补加10g氢氧化钠固体,75℃搅拌4h后,过滤混合液获得含锌浸取液和稀土富集渣;浸取液调节pH,沉淀回收Zn(OH)2;煅烧Zn(OH)2获得ZnO粉末,锌的回收率为98.3%。Primary screening is carried out on the waste cathode ray tube fluorescent powder obtained from recovery, and the fine glass slag, aluminum and other silicon-aluminum impurities are leached with hot alkali solution. After removing aluminum and silicon, the waste cathode ray tube fluorescent powder is mixed with sodium peroxide at a mass ratio of 1:0.5, placed in a high-temperature resistant reaction vessel, and dripping water triggers a self-propagating reaction; water-soluble at a solid-to-liquid ratio of 1:20 (g/mL) For the reaction product, add 10g of sodium hydroxide solid, stir at 75°C for 4 hours, filter the mixed solution to obtain zinc-containing leaching solution and rare earth enrichment slag; adjust the pH of the leaching solution, and recover Zn(OH) 2 by precipitation; calcining Zn(OH) ) 2 to obtain ZnO powder, the recovery rate of zinc is 98.3%.
实施例2Example 2
将回收获得的废弃阴极射线管荧光粉进行初级筛分,采用热碱液浸出其中的细玻璃渣和铝及其他硅铝杂质。除铝硅后的废弃阴极射线管荧光粉与过氧化钠按质量比1:1混合,置于耐高温反应容器中,滴酒精引发自蔓延反应;按固液比1:35(g/mL)水溶反应产物,补加5g氢氧化钠固体,80℃搅拌2.5h后,过滤混合液获得含锌浸取液和稀土富集渣;浸取液调节pH,沉淀回收Zn(OH)2;煅烧Zn(OH)2获得ZnO粉末,锌的回收率为98.6%。Primary screening is carried out on the waste cathode ray tube fluorescent powder obtained from recovery, and the fine glass slag, aluminum and other silicon-aluminum impurities are leached with hot alkali solution. The discarded cathode ray tube fluorescent powder after removing aluminum and silicon is mixed with sodium peroxide at a mass ratio of 1:1, placed in a high-temperature resistant reaction vessel, and dripped with alcohol to initiate a self-propagating reaction; at a solid-to-liquid ratio of 1:35 (g/mL) For the water-soluble reaction product, add 5g of sodium hydroxide solid, stir at 80°C for 2.5 hours, filter the mixed solution to obtain zinc-containing leaching solution and rare earth enrichment slag; adjust the pH of the leaching solution, and recover Zn(OH) 2 by precipitation; calcining Zn (OH) 2 to obtain ZnO powder, the recovery rate of zinc is 98.6%.
实施例3Example 3
将回收获得的废弃阴极射线管荧光粉进行初级筛分,采用热碱液浸出其中的细玻璃渣和铝及其他硅铝杂质。除铝硅后的废弃阴极射线管荧光粉与过氧化钠按质量比1:2混合,置于耐高温反应容器中,钨丝点燃引发自蔓延反应;按固液比1:40(g/mL)水溶反应产物,补加7.5g氢氧化钠固体,20℃搅拌3.5h后,过滤混合液获得含锌浸取液和稀土富集渣;浸取液调节pH,沉淀回收Zn(OH)2;煅烧Zn(OH)2获得ZnO粉末,锌的回收率为99.1%。Primary screening is carried out on the waste cathode ray tube fluorescent powder obtained from recovery, and the fine glass slag, aluminum and other silicon-aluminum impurities are leached with hot alkali solution. The discarded cathode ray tube fluorescent powder after removing aluminum and silicon is mixed with sodium peroxide at a mass ratio of 1:2, placed in a high-temperature resistant reaction vessel, and tungsten wire is ignited to initiate a self-propagating reaction; according to a solid-liquid ratio of 1:40 (g/mL ) water-soluble reaction product, add 7.5g sodium hydroxide solid, after stirring at 20°C for 3.5h, filter the mixed solution to obtain zinc-containing leaching solution and rare earth enrichment slag; the leaching solution adjusts pH, and precipitation recovers Zn(OH) 2 ; Calcining Zn(OH) 2 to obtain ZnO powder, the recovery rate of zinc is 99.1%.
实施例4Example 4
将回收获得的废弃阴极射线管荧光粉进行初级筛分,采用热碱液浸出其中的细玻璃渣和铝及其他硅铝杂质。除铝硅后的废弃阴极射线管荧光粉与过氧化钠按质量比1:3混合,置于耐高温反应容器中,镍洛合金线圈点燃引发自蔓延反应;按固液比1:45(g/mL)水溶反应产物,补加3g氢氧化钠固体,35℃搅拌3h后,过滤混合液获得含锌浸取液和稀土富集渣;浸取液调节pH,沉淀回收Zn(OH)2;煅烧Zn(OH)2获得ZnO粉末,锌的回收率为97.9%。Primary screening is carried out on the waste cathode ray tube fluorescent powder obtained from recovery, and the fine glass slag, aluminum and other silicon-aluminum impurities are leached with hot alkali solution. The discarded cathode ray tube fluorescent powder after removing aluminum and silicon is mixed with sodium peroxide in a mass ratio of 1:3, placed in a high-temperature resistant reaction vessel, and the nickel alloy coil is ignited to cause a self-propagating reaction; according to a solid-to-liquid ratio of 1:45 (g /mL) water-soluble reaction product, add 3g sodium hydroxide solid, after stirring at 35°C for 3h, filter the mixed solution to obtain zinc-containing leaching solution and rare earth enrichment slag; the leaching solution adjusts pH, and precipitation recovers Zn(OH) 2 ; Calcining Zn(OH) 2 to obtain ZnO powder, the recovery rate of zinc is 97.9%.
实施例5Example 5
将回收获得的废弃阴极射线管荧光粉进行初级筛分,采用热碱液浸出其中的细玻璃渣和铝及其他硅铝杂质。除铝硅后的废弃阴极射线管荧光粉与过氧化钠按质量比1:4混合,置于耐高温反应容器中,激光局部加热引发自蔓延反应;按固液比1:65(g/mL)水溶反应产物,补加4g氢氧化钠固体,45℃搅拌2h后,过滤混合液获得含锌浸取液和稀土富集渣;浸取液调节pH,沉淀回收Zn(OH)2;煅烧Zn(OH)2获得ZnO粉末,锌的回收率为98.5%。Primary screening is carried out on the waste cathode ray tube fluorescent powder obtained from recovery, and the fine glass slag, aluminum and other silicon-aluminum impurities are leached with hot alkali solution. The discarded cathode ray tube fluorescent powder after removing aluminum and silicon is mixed with sodium peroxide at a mass ratio of 1:4, placed in a high-temperature resistant reaction vessel, and locally heated by a laser triggers a self-propagating reaction; according to a solid-liquid ratio of 1:65 (g/mL ) water-soluble reaction product, add 4g of sodium hydroxide solid, and after stirring at 45°C for 2 hours, filter the mixed solution to obtain zinc-containing leaching solution and rare earth enrichment slag; adjust the pH of the leaching solution, and recover Zn(OH) 2 by precipitation; calcining Zn (OH) 2 to obtain ZnO powder, the recovery rate of zinc is 98.5%.
实施例6Example 6
将回收获得的废弃阴极射线管荧光粉进行初级筛分,采用热碱液浸出其中的细玻璃渣和铝及其他硅铝杂质。除铝硅后的废弃阴极射线管荧光粉与过氧化钠按质量比1:5混合,置于耐高温反应容器中,电热板加热引发自蔓延反应;按固液比1:80(g/mL)水溶反应产物,补加6g氢氧化钠固体,50℃搅拌1.5h后,过滤混合液获得含锌浸取液和稀土富集渣;浸取液调节pH,沉淀回收Zn(OH)2;煅烧Zn(OH)2获得ZnO粉末,锌的回收率为99.3%。Primary screening is carried out on the waste cathode ray tube fluorescent powder obtained from recovery, and the fine glass slag, aluminum and other silicon-aluminum impurities are leached with hot alkali solution. The waste cathode ray tube fluorescent powder after removing aluminum and silicon is mixed with sodium peroxide at a mass ratio of 1:5, placed in a high temperature resistant reaction vessel, and heated by an electric heating plate to cause a self-propagating reaction; according to a solid-liquid ratio of 1:80 (g/mL ) water-soluble reaction product, add 6g of sodium hydroxide solid, after stirring at 50°C for 1.5h, filter the mixed solution to obtain zinc-containing leaching solution and rare earth enrichment slag; adjust the pH of the leaching solution, and recover Zn(OH) 2 by precipitation; calcining Zn(OH) 2 obtains ZnO powder, and the recovery rate of zinc is 99.3%.
实施例7Example 7
将回收获得的废弃阴极射线管荧光粉进行初级筛分,采用热碱液浸出其中的细玻璃渣和铝及其他硅铝杂质。除铝硅后的废弃阴极射线管荧光粉与过氧化钠按质量比1:4.5混合,置于耐高温反应容器中,微波加热引发自蔓延反应;按固液比1:90水溶反应产物,补加8g氢氧化钠固体,60℃搅拌1h后,过滤混合液获得含锌浸取液和稀土富集渣;浸取液调节pH,沉淀回收Zn(OH)2;煅烧Zn(OH)2获得ZnO粉末,锌的回收率为98.5%。Primary screening is carried out on the waste cathode ray tube fluorescent powder obtained from recovery, and the fine glass slag, aluminum and other silicon-aluminum impurities are leached with hot alkali solution. The discarded cathode ray tube fluorescent powder after removing aluminum and silicon is mixed with sodium peroxide at a mass ratio of 1:4.5, placed in a high-temperature resistant reaction vessel, and heated by microwaves to cause a self-propagating reaction; water-soluble reaction product at a solid-to-liquid ratio of 1:90, replenished Add 8g of sodium hydroxide solid, stir at 60°C for 1 hour, filter the mixed solution to obtain zinc-containing leaching solution and rare earth enrichment slag; adjust the pH of the leaching solution, precipitate and recover Zn(OH) 2 ; calcinate Zn(OH) 2 to obtain ZnO powder, the recovery rate of zinc is 98.5%.
实施例8Example 8
将回收获得的废弃阴极射线管荧光粉进行初级筛分,采用热碱液浸出其中的细玻璃渣和铝及其他硅铝杂质。除铝硅后的废弃阴极射线管荧光粉与过氧化钠按质量比1:5混合,置于耐高温反应容器中,热爆点燃引发自蔓延反应;按固液比1:100(g/mL)水溶反应产物,65℃搅拌0.5h后,过滤混合液获得含锌浸取液和稀土富集渣;浸取液调节pH,沉淀回收Zn(OH)2;煅烧Zn(OH)2获得ZnO粉末,锌的回收率为98.3%。Primary screening is carried out on the waste cathode ray tube fluorescent powder obtained from recovery, and the fine glass slag, aluminum and other silicon-aluminum impurities are leached with hot alkali solution. The discarded cathode ray tube fluorescent powder after removing aluminum and silicon is mixed with sodium peroxide at a mass ratio of 1:5, placed in a high temperature resistant reaction vessel, and thermal detonation is ignited to trigger a self-propagating reaction; according to a solid-liquid ratio of 1:100 (g/mL ) water-soluble reaction product, after stirring at 65°C for 0.5h, filter the mixed solution to obtain zinc-containing leaching solution and rare earth enrichment slag; adjust the pH of the leaching solution, precipitate and recover Zn(OH) 2 ; calcinate Zn(OH) 2 to obtain ZnO powder , The recovery rate of zinc is 98.3%.
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