CN103131862B - Extraction of High Purity Rare Earth Oxide from Phosphor Powder Waste by Pretreatment Decomposition - Google Patents

Extraction of High Purity Rare Earth Oxide from Phosphor Powder Waste by Pretreatment Decomposition Download PDF

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CN103131862B
CN103131862B CN201310079030.1A CN201310079030A CN103131862B CN 103131862 B CN103131862 B CN 103131862B CN 201310079030 A CN201310079030 A CN 201310079030A CN 103131862 B CN103131862 B CN 103131862B
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龚跃民
刘勇
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Longnan Zhongli Renewable Resources Development Co ltd
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Longnan County Zhongli Regeneration Resource Development Co ltd
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Abstract

The high-purity rare earth oxide is extracted from the fluorescent powder waste by a pretreatment decomposition method, and the high-purity rare earth oxide is extracted from the fluorescent powder waste by the processes of fluorescent powder waste pretreatment, oxidizing roasting, acidolysis, extraction, precipitation and ignition. The invention improves the recovery rate of the rare earth in the waste by controlling the reaction temperature and adding the cosolvent; liquid caustic soda is used as a saponification extracting agent, so that the wastewater is free from ammonia and nitrogen emission, and the environmental pollution is reduced; the quality of the recovered product is improved, the production cost is reduced, and the process technology has certain innovativeness.

Description

预处理分解法从荧光粉废料中提取高纯稀土氧化物 Extraction of High Purity Rare Earth Oxide from Phosphor Powder Waste by Pretreatment Decomposition

技术领域 technical field

本发明涉及荧光粉废料的回收利用技术领域,具体为一种预处理分解法从荧光粉废料中提取高纯稀土氧化物。 The invention relates to the technical field of recycling fluorescent powder waste, in particular to a pretreatment decomposition method for extracting high-purity rare earth oxides from fluorescent powder waste.

背景技术 Background technique

目前由于生产和使用因素,国内因荧光粉生产及产品报废达数十万吨。荧光粉废料当中普遍存在稀土配分相差,有低品味和高品味之分,然而,低品味荧光粉废料厂家只能弃之或存放之,只能处理高品味荧光粉废料。目前从荧光粉废料中回收有价元素的生产工艺通常是 :焙烧→酸溶或碱浸→净化除杂→萃取分离、提纯。普遍存在稀土废料酸溶收率低,回收稀土所用的化工辅料最终以氨、氮废水形式排放等问题,造成了大量有价资源的浪费,并对环境造成了严重污染。 At present, due to production and use factors, domestic phosphor production and product scrapping amount to hundreds of thousands of tons. Phosphor powder waste generally has a difference in the distribution of rare earths, which can be divided into low-grade and high-grade phosphor waste. However, manufacturers of low-grade phosphor waste can only discard or store them, and can only deal with high-grade phosphor waste. At present, the production process for recovering valuable elements from phosphor waste is usually: roasting→acid dissolution or alkali leaching→purification and impurity removal→extraction separation and purification. There are common problems such as low acid dissolution rate of rare earth waste, and the chemical auxiliary materials used in the recovery of rare earth are finally discharged in the form of ammonia and nitrogen wastewater, resulting in the waste of a large amount of valuable resources and serious pollution to the environment.

发明内容 Contents of the invention

本发明所解决的技术问题在于提供一种预处理分解法从荧光粉废料中提取高纯稀土氧化物,以解决上述背景技术中的问题。 The technical problem to be solved by the present invention is to provide a pretreatment decomposition method to extract high-purity rare earth oxides from fluorescent powder waste, so as to solve the above-mentioned problems in the background technology.

本发明所解决的技术问题采用以下技术方案来实现: The technical problem solved by the present invention adopts following technical scheme to realize:

预处理分解法从荧光粉废料中提取高纯稀土氧化物,包括以下6个步骤: The pretreatment decomposition method extracts high-purity rare earth oxides from phosphor waste, including the following six steps:

(1)荧光粉废料预处理;将荧光粉废料加入搪瓷反应锅内加水搅拌后调成浆液后,加温至40~80℃;缓慢加入盐酸至搪瓷反应锅内溶解运行12~20h,澄清后排放上清液;再加入自来水进行二次除杂,水洗完成后加入纯稀土溶液搅拌,恒温20~40min后加入草酸把部分溶解出的稀土进行沉淀,直至检测清液当中无稀土元素时放入板框压滤机进行板框压滤,滤液至废水处理,滤饼至氧化焙烧; (1) Phosphor powder waste pretreatment; add phosphor powder waste to the enamel reaction pot, add water and stir to make a slurry, heat to 40-80°C; slowly add hydrochloric acid to the enamel reaction pot to dissolve and run for 12-20h, after clarification Drain the supernatant; then add tap water for secondary impurity removal, add pure rare earth solution and stir after washing, keep the temperature for 20 to 40 minutes, add oxalic acid to precipitate part of the dissolved rare earth until it is detected that there are no rare earth elements in the clear liquid. Plate and frame filter press for plate and frame filter press, filtrate to wastewater treatment, filter cake to oxidation roasting;

(2)氧化焙烧;经过预处理出来的滤饼加入氢氧化钠溶液搅拌混合均匀后,通过窑炉进行焙烧氧化,控制焙烧温度为700~900℃,保温至废料焙烧完全; (2) Oxidative roasting: After the pretreated filter cake is mixed with sodium hydroxide solution and mixed evenly, it is roasted and oxidized in a kiln, and the roasting temperature is controlled at 700-900°C, and the heat is kept until the waste is roasted completely;

(3)酸解;在酸溶罐中将焙烧后的废料加水制成浆液,然后加盐酸溶解,并加入助溶剂助溶,溶液经板框压滤机过滤得到氯化稀土料液,除杂; (3) Acid hydrolysis: Add water to the roasted waste to make a slurry in an acid-dissolving tank, then add hydrochloric acid to dissolve, and add a cosolvent to aid in dissolution, and the solution is filtered through a plate and frame filter press to obtain a rare earth chloride feed liquid, and remove impurities ;

(4)萃取;利用液碱作为萃取皂化剂,往氯化稀土料液中投入液碱后并除杂即得稀土氯化物溶液,且达到废水无氨、氮排放; (4) Extraction: use liquid caustic soda as the extraction saponification agent, put liquid caustic soda into the rare earth chloride feed solution and remove impurities to obtain rare earth chloride solution, and achieve no ammonia and nitrogen discharge in wastewater;

(5)沉淀;向步骤(4)得到的稀土氯化物溶液缓慢投入纯稀土料液和草酸,温度控制60℃~70℃,利用反应釜和抽滤池通过沉淀剂进行快速沉淀得到稀土草酸物; (5) Precipitation; Slowly add pure rare earth feed solution and oxalic acid to the rare earth chloride solution obtained in step (4), control the temperature at 60°C to 70°C, and use the reaction kettle and suction filter to conduct rapid precipitation through the precipitant to obtain the rare earth oxalate ;

(6)灼烧;利用窑炉对步骤(5)得到的稀土草酸物进行1000℃高温灼烧,再经脱水、碳化、氧化得到高纯稀土氧化物。 (6) Burning: use a kiln to burn the rare earth oxalate obtained in step (5) at a high temperature of 1000°C, and then undergo dehydration, carbonization, and oxidation to obtain high-purity rare earth oxides.

有益效果: Beneficial effect:

本发明通过控制反应温度和添加助溶剂,提高了废料中稀土的回收率;采用液碱作为皂化萃取剂,达到废水无氨、氮排放,减轻了环境污染;提高回收产品质量,降低了生产成本,工艺技术具有一定的创新性。 The invention improves the recovery rate of rare earths in waste by controlling the reaction temperature and adding co-solvent; adopts liquid caustic soda as a saponification extraction agent, achieves no ammonia and nitrogen discharge in waste water, and reduces environmental pollution; improves the quality of recycled products and reduces production costs , the process technology has a certain degree of innovation.

具体实施方式 detailed description

为了使本发明的技术手段、创作特征、工作流程、使用方法达成目的与功效易于明白了解,下面进一步阐述本发明。 In order to make it easy to understand the technical means, creative features, work flow, and use methods of the present invention to achieve the purpose and effect, the present invention will be further elaborated below.

预处理分解法从荧光粉废料中提取高纯稀土氧化物,包括以下6个步骤: The pretreatment decomposition method extracts high-purity rare earth oxides from phosphor waste, including the following six steps:

(1)荧光粉废料预处理;取300g荧光粉废料加入搪瓷反应锅内,加入800ml水搅拌调成浆液后,加温至75℃;缓慢加入盐酸至搪瓷反应锅内溶解运行20h,澄清后排放上清液,再加入自来水进行二次除杂,水洗完成后加入纯稀土溶液搅拌,75℃恒温35min后加入草酸把部分溶解出的稀土进行沉淀,直至检测清液当中无稀土元素时放入板框压滤机进行板框压滤,滤液至废水处理,滤饼至氧化焙烧; (1) Phosphor powder waste pretreatment; take 300g of phosphor powder waste and add it to the enamel reaction pot, add 800ml of water and stir to make a slurry, then heat to 75°C; slowly add hydrochloric acid to the enamel reaction pot to dissolve and run for 20 hours, and discharge after clarification Add tap water to the supernatant for secondary impurity removal. After washing, add pure rare earth solution and stir. After 35 minutes at 75°C, add oxalic acid to precipitate part of the dissolved rare earth until it is detected that there is no rare earth element in the supernatant. Frame filter press for plate and frame filter press, filtrate to wastewater treatment, filter cake to oxidation roasting;

(2)氧化焙烧;经过预处理出来的滤饼加入氢氧化钠溶液搅拌混合均匀后,通过窑炉进行焙烧氧化,控制焙烧温度为700~900℃,保温至废料焙烧完全; (2) Oxidative roasting: After the pretreated filter cake is mixed with sodium hydroxide solution and mixed evenly, it is roasted and oxidized in a kiln, and the roasting temperature is controlled at 700-900°C, and the heat is kept until the waste is roasted completely;

(3)酸解;在酸溶罐中将焙烧后的废料加入1L水制成浆液,然后加盐酸溶解,并加入助溶剂助溶,溶液经板框压滤机过滤得到氯化稀土料液,除杂; (3) Acid hydrolysis: Add 1L of water to the roasted waste in an acid-dissolving tank to make a slurry, then add hydrochloric acid to dissolve, and add a cosolvent to aid in dissolution. The solution is filtered through a plate and frame filter press to obtain a rare earth chloride feed solution. cleaning;

(4)萃取;利用液碱作为萃取皂化剂,往氯化稀土料液中投入液碱后,机械搅拌后除杂即得稀土氯化物溶液,且达到废水无氨、氮排放; (4) Extraction: use liquid caustic soda as the extraction saponification agent, put liquid caustic soda into the rare earth chloride feed liquid, remove impurities after mechanical stirring to obtain rare earth chloride solution, and achieve no ammonia and nitrogen discharge in wastewater;

(5)沉淀;向步骤(4)得到的稀土氯化物溶液缓慢投入纯稀土料液和草酸,温度控制65℃,利用反应釜和抽滤池通过沉淀剂进行快速沉淀得到稀土草酸物; (5) Precipitation: Slowly add pure rare earth feed liquid and oxalic acid to the rare earth chloride solution obtained in step (4), control the temperature at 65°C, and use the reaction kettle and suction filter tank to conduct rapid precipitation through a precipitant to obtain rare earth oxalic acid;

(6)灼烧;利用窑炉对步骤(5)得到的稀土草酸物进行1000℃高温灼烧,再经脱水、碳化、氧化得到高纯稀土氧化物。 (6) Burning: use a kiln to burn the rare earth oxalate obtained in step (5) at a high temperature of 1000°C, and then undergo dehydration, carbonization, and oxidation to obtain high-purity rare earth oxides.

以上显示和描述了本发明的基本原理、主要特征及本发明的优点。本行业的技术人员应该了解,本发明不受上述实施例的限制,上述实施例和说明书中描述的只是说明本发明的原理,在不脱离本发明精神和范围的前提下,本发明还会有各种变化和改进,这些变化和改进都落入要求保护的本发明范围内。本发明的要求保护范围由所附的权利要求书及其等效物界定。 The basic principles, main features and advantages of the present invention have been shown and described above. Those skilled in the industry should understand that the present invention is not limited by the above-mentioned embodiments, and what described in the above-mentioned embodiments and the description only illustrates the principles of the present invention, and the present invention will also have other functions without departing from the spirit and scope of the present invention. Variations and improvements all fall within the scope of the claimed invention. The claimed scope of the present invention is defined by the appended claims and their equivalents.

Claims (1)

1. pretreatment decomposition method extracts high purity rare earth oxides from fluorescent powder scrap, it is characterized in that: include following 6 steps:
(1) fluorescent powder scrap pretreatment;Add water in fluorescent powder scrap is added enamel reaction pot after being slurried after stirring, be heated up to 40~80 DEG C;Being slowly added to hydrochloric acid and dissolve operation 12~20h to enamel reaction pot, clarification heel row puts clear liquid;Add tap water and carry out secondary remove impurity, pure rare earth solution stirring is added after having washed, add oxalic acid after constant temperature 20~40min the rare earth being partly dissolved out is precipitated, until in the middle of detection clear liquid without rare earth element time put into filter press and carry out filter press, filtrate processes to waste water, and filter cake is to oxidizing roasting;
(2) oxidizing roasting;After pretreatment filter cake addition sodium hydroxide solution out is uniformly mixed, carrying out roasting oxidation by kiln, controlling sintering temperature is 700~900 DEG C, is incubated complete to waste material roasting;
(3) acidolysis;Being added water by waste material after roasting in sour molten tank and make serosity, then add dissolving with hydrochloric acid, and add cosolvent hydrotropy, solution is filtrated to get rare earth chloride liquid, remove impurity through filter press;
(4) extraction;Utilize liquid caustic soda as extraction saponification agent, put into after liquid caustic soda in rare earth chloride liquid and remove impurity i.e. obtains rare-earth chloride solution, and reach waste water without ammonia, nitrogen discharged;
(5) precipitation;The rare-earth chloride solution obtained to step (4) slowly puts into pure rare earth feed liquid and oxalic acid, and temperature controls 60 DEG C~70 DEG C, utilizes reactor and sucking filtration pond to carry out rapid precipitation by precipitant and obtains rare earth oxalic acid thing;
(6) calcination;The rare earth oxalic acid thing utilizing kiln to obtain step (5) carries out 1000 DEG C of high temperature sinterings, then obtains high purity rare earth oxides through dehydration, carbonization, oxidation.
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CN105039698A (en) * 2015-04-21 2015-11-11 南京林业大学 Method of high-effectively recycling rare earth from waste CRT fluorescent powder
CN104946896B (en) * 2015-07-15 2017-07-14 江西理工大学 A kind of method of the Extraction of rare earth from useless fluorescent RE powder
CN105200250A (en) * 2015-09-30 2015-12-30 中铝广西国盛稀土开发有限公司 Method of recovering rare-earth elements from oxalic acid precipitate rare-earth mother liquor
CN110627104A (en) * 2019-08-30 2019-12-31 赣州市恒源科技股份有限公司 Method for preparing high-purity rare earth oxide by recovering fluorescent powder waste
CN110923439A (en) * 2019-12-09 2020-03-27 四川省冕宁县方兴稀土有限公司 Method for improving rare earth ore conversion rate in rare earth wet smelting
CN111392756A (en) * 2020-05-06 2020-07-10 龙南县中利再生资源开发有限公司 Process for extracting high-purity rare earth oxide from fluorescent powder waste

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