CN117701273B - Photoluminescent material based on rare earth super-enriched plants and preparation method and application thereof - Google Patents
Photoluminescent material based on rare earth super-enriched plants and preparation method and application thereof Download PDFInfo
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Abstract
Description
技术领域Technical Field
本发明属于发光材料技术领域。更具体地,涉及一种基于稀土超富集植物得到的光致发光材料及其制备方法与应用。The present invention belongs to the technical field of luminescent materials, and more specifically, relates to a photoluminescent material obtained from rare earth hyperaccumulator plants, and a preparation method and application thereof.
背景技术Background Art
稀土是我国的重要战略资源,在航空航天、高新技术、医疗健康等领域发挥着重要作用。由于稀土离子具有丰富的能级结构与电子跃迁特性,稀土发光材料及光电器件在照明、显示、激光和生物成像等方面有着重大需求。稀土采矿活动随着稀土需求量的激增而不断加剧,在获取资源的同时也会对周围生态环境造成严重破坏。Rare earth is an important strategic resource in my country, playing an important role in aerospace, high-tech, medical and health fields. Since rare earth ions have rich energy level structures and electronic transition characteristics, rare earth luminescent materials and optoelectronic devices are in great demand in lighting, display, laser and bio-imaging. Rare earth mining activities have been intensified with the surge in demand for rare earths, and while obtaining resources, they will also cause serious damage to the surrounding ecological environment.
为了改善稀土采矿活动对土壤的破坏,通过超富集植物吸收、转运稀土元素,可以很好的修复污染土壤,是一种生态友好的稀土矿区污染治理技术。但是,修复后的稀土植物收获物需要资源化、无害化处理,避免二次污染,才能进一步推动植物修复技术的产业化与规模化应用,否则又会造成资源的浪费或环境的污染。目前,植物修复收获物如何更好地进行资源化利用仍存在较大挑战,中国专利申请CN111020239A通过机械破碎、真空热解分段冷凝与稀土浸出沉淀联合工艺从超富集植物中回收稀土氧化物、热解油和热解气,但该工艺所得稀土氧化物纯度不高,无法直接利用。因此,迫切需要提供一种可以充分利用稀土超富集植物中的稀土元素,制备高利用价值材料的方法。In order to improve the damage to the soil caused by rare earth mining activities, the absorption and transport of rare earth elements by super-enriched plants can well repair the contaminated soil, which is an eco-friendly rare earth mining area pollution control technology. However, the rare earth plant harvest after repair needs to be resourced and harmlessly treated to avoid secondary pollution in order to further promote the industrialization and large-scale application of plant restoration technology, otherwise it will cause waste of resources or environmental pollution. At present, there are still great challenges in how to better utilize the harvest of plant restoration resources. Chinese patent application CN111020239A recovers rare earth oxides, pyrolysis oil and pyrolysis gas from super-enriched plants through a combined process of mechanical crushing, vacuum pyrolysis segmented condensation and rare earth leaching precipitation, but the rare earth oxides obtained by this process are of low purity and cannot be directly used. Therefore, it is urgent to provide a method for preparing high-utilization value materials by making full use of the rare earth elements in rare earth super-enriched plants.
发明内容Summary of the invention
本发明要解决的技术问题是克服现有稀土超富集植物处理所得产物纯度不高需要另外加工无法直接利用的缺陷和不足,提供一种可以充分利用稀土超富集植物中的稀土元素,得到高利用价值光致发光材料、气化油与合成气的制备方法。The technical problem to be solved by the present invention is to overcome the defects and shortcomings of the existing products obtained by treating rare earth hyper-enriched plants, which are of low purity and require additional processing and cannot be directly utilized, and to provide a preparation method that can fully utilize the rare earth elements in rare earth hyper-enriched plants to obtain photoluminescent materials, gasified oil and synthesis gas with high utilization value.
本发明的目的是提供所述制备方法制备的光致发光材料。The purpose of the present invention is to provide a photoluminescent material prepared by the preparation method.
本发明另一目的是提供所述光致发光材料的应用。Another object of the present invention is to provide application of the photoluminescent material.
本发明上述目的通过以下技术方案实现:The above-mentioned purpose of the present invention is achieved through the following technical solutions:
一种基于稀土超富集植物得到的光致发光材料的制备方法,具体包括以下步骤:A method for preparing a photoluminescent material obtained from rare earth super-enriched plants, specifically comprising the following steps:
S1、将稀土超富集植物收获物干燥、粉碎,加入硫酸溶液和乙醇,于140~200℃、密闭条件下溶剂热反应完全,冷却、分离,得到固相产物;S1. Drying and crushing the harvested rare earth super-enriched plant material, adding sulfuric acid solution and ethanol, carrying out a solvent thermal reaction at 140-200° C. under a closed condition, cooling and separating to obtain a solid phase product;
S2、将步骤S1所得固相产物进行水蒸气气化,气化温度为750~900℃,水蒸气流量为5~150μL/min,载气为氮气,氮气的流速为50~200mL/min,气化时间为5~30min,所得气化油产物由异丙醇吸收收集,合成气气体由气袋收集;反应结束后,冷却得到光致发光材料。S2. The solid phase product obtained in step S1 is subjected to water vapor gasification, the gasification temperature is 750-900° C., the water vapor flow rate is 5-150 μL/min, the carrier gas is nitrogen, the nitrogen flow rate is 50-200 mL/min, the gasification time is 5-30 min, the obtained gasified oil product is absorbed and collected by isopropanol, and the synthesis gas is collected by an air bag; after the reaction is completed, the photoluminescent material is cooled.
本发明采用稀硫酸与乙醇进行溶剂热处理,将稀土、钙元素以硫酸盐形式选择性地富集于固相产物中,后续采用水蒸气气化脱碳,并调控硫酸钙碳还原为硫化钙,稀土硫酸盐热分解为稀土氧化物,从而制得稀土氧化物掺杂硫化钙的光致发光材料。整个超富集植物资源化利用与无害化处理工艺运用了溶剂热处理与水蒸气气化联合技术,实现了基于稀土超富集植物收获物制备得到稀土光致发光材料、气化油与高值合成气产品的效果;整个过程绿色高效,所得产品光学性能、热值、产值较高,在稀土超富集植物综合资源化利用领域具有广阔的应用前景。The present invention uses dilute sulfuric acid and ethanol for solvent thermal treatment, selectively enriches rare earth and calcium elements in the form of sulfate in the solid phase product, and then uses steam gasification for decarbonization, and regulates the carbon reduction of calcium sulfate to calcium sulfide, and thermally decomposes rare earth sulfate into rare earth oxide, thereby preparing a photoluminescent material doped with rare earth oxide and calcium sulfide. The entire super-enriched plant resource utilization and harmless treatment process uses the combined technology of solvent thermal treatment and steam gasification, and achieves the effect of preparing rare earth photoluminescent materials, gasified oil and high-value syngas products based on the harvest of rare earth super-enriched plants; the whole process is green and efficient, and the optical properties, calorific value and output value of the obtained products are relatively high, and it has broad application prospects in the field of comprehensive resource utilization of rare earth super-enriched plants.
进一步地,步骤S1中,所述硫酸溶液的浓度为0.1~0.5mol/L。优选地,所述硫酸溶液的浓度为0.4mol/L。Furthermore, in step S1, the concentration of the sulfuric acid solution is 0.1-0.5 mol/L. Preferably, the concentration of the sulfuric acid solution is 0.4 mol/L.
更进一步地,步骤S1中,所述硫酸溶液和乙醇的体积比为1:(1~7);优选地,所述硫酸溶液和乙醇的体积比为1:7。Furthermore, in step S1, the volume ratio of the sulfuric acid solution to ethanol is 1:(1-7); preferably, the volume ratio of the sulfuric acid solution to ethanol is 1:7.
进一步地,步骤S1中,所述稀土超富集植物收获物与硫酸溶液和乙醇总体积的比为1:(10~100)g/mL。优选地,所述稀土超富集植物收获物与硫酸溶液和乙醇总体积的比为1:20g/mL。Furthermore, in step S1, the ratio of the rare earth super-enriched plant harvest to the total volume of the sulfuric acid solution and ethanol is 1:(10-100) g/mL. Preferably, the ratio of the rare earth super-enriched plant harvest to the total volume of the sulfuric acid solution and ethanol is 1:20 g/mL.
更进一步地,步骤S1中,所述溶剂热反应的时间为1~3h。优选地,所述溶剂热反应的时间为2h。Furthermore, in step S1, the solvent thermal reaction time is 1 to 3 hours. Preferably, the solvent thermal reaction time is 2 hours.
优选地,步骤S1中,所述固相产物通过真空抽滤收集。Preferably, in step S1, the solid phase product is collected by vacuum filtration.
优选地,步骤S1中,所述溶剂热反应的温度为160℃。Preferably, in step S1, the temperature of the solvothermal reaction is 160°C.
进一步地,步骤S2中,所述合成气气体包括H2、CO、CH4。Furthermore, in step S2, the synthesis gas includes H 2 , CO, and CH 4 .
优选地,步骤S2中,气化温度为850℃,水蒸气流量为100μL/min,载气为氮气,氮气的流速为100mL/min,气化时间为10min。Preferably, in step S2, the vaporization temperature is 850°C, the water vapor flow rate is 100 μL/min, the carrier gas is nitrogen, the flow rate of nitrogen is 100 mL/min, and the vaporization time is 10 min.
本发明采用水蒸气气化工艺,在制备稀土氧化物掺杂硫化钙光致发光材料的同时,还能获得生物质高附加值合成气与气化油。进一步采用氮气为载气的水蒸气气化处理稀硫酸与乙醇溶剂热反应所得固相产物,将引入的硫元素固定到硫化钙中,避免其氧化为二氧化硫或三氧化硫排放到环境中污染空气。同时可通过控制水蒸气流量调控稀土氧化物掺杂硫化钙的晶体结构,进一步调控光致发光材料的发光颜色等性能。The present invention adopts a water vapor gasification process, and while preparing a rare earth oxide doped calcium sulfide photoluminescent material, it can also obtain biomass high value-added synthesis gas and gasified oil. Further, the water vapor gasification with nitrogen as a carrier gas is used to treat the solid phase product obtained by the thermal reaction of dilute sulfuric acid and ethanol solvent, and the introduced sulfur element is fixed to the calcium sulfide to prevent it from being oxidized to sulfur dioxide or sulfur trioxide and discharged into the environment to pollute the air. At the same time, the crystal structure of the rare earth oxide doped calcium sulfide can be regulated by controlling the water vapor flow rate, and the luminous color and other properties of the photoluminescent material can be further regulated.
更进一步地,所述稀土超富集植物选自美洲商陆、芒萁、单叶新月蕨、柔毛山核桃、山核桃、乌毛蕨中的一种或多种。Furthermore, the rare earth hyperaccumulator plants are selected from one or more of American pokeweed, dicranopteris dichotoma, simple-leaved crescent fern, pubescent pecan, pecan, and black-haired fern.
另外的,本发明要求保护所述制备方法制备的光致发光材料。In addition, the present invention claims protection for the photoluminescent material prepared by the preparation method.
进一步地,所述光致发光材料主要为稀土掺杂的CaS,于250~470nm激发光谱下在480~800nm发射荧光。Furthermore, the photoluminescent material is mainly rare earth-doped CaS, which emits fluorescence at 480-800nm under an excitation spectrum of 250-470nm.
另外的,本发明还提供了所述光致发光材料在LED照明、生物荧光成像、材料结构表征、防伪中的应用。In addition, the present invention also provides applications of the photoluminescent material in LED lighting, bioluminescence imaging, material structure characterization, and anti-counterfeiting.
本发明具有以下有益效果:The present invention has the following beneficial effects:
本发明采用稀硫酸与乙醇对稀土超富集植物收获物进行溶剂热处理,将稀土、钙元素以硫酸盐形式选择性地富集于固相产物中,后续采用水蒸气气化脱碳,并调控硫酸钙碳还原为硫化钙,稀土硫酸盐热分解为稀土氧化物,从而制得稀土氧化物掺杂硫化钙的光致发光材料。整个超富集植物资源化利用与无害化处理工艺运用了溶剂热处理与水蒸气气化联合技术,实现了基于稀土超富集植物收获物制备得到稀土光致发光材料、气化油与高值合成气产品的效果;整个过程操作简单、绿色高效,所得产品光学性能、热值、产值较高,兼具经济价值与环境效益,在稀土超富集植物综合资源化利用领域具有广阔的应用前景。The present invention uses dilute sulfuric acid and ethanol to perform solvent thermal treatment on the harvested materials of rare earth super-enriched plants, selectively enriches rare earth and calcium elements in the form of sulfate in the solid phase product, and subsequently uses steam gasification for decarbonization, and regulates the carbon reduction of calcium sulfate to calcium sulfide, and thermally decomposes rare earth sulfate to rare earth oxide, thereby preparing a photoluminescent material doped with rare earth oxide and calcium sulfide. The entire super-enriched plant resource utilization and harmless treatment process uses the combined technology of solvent thermal treatment and steam gasification, and achieves the effect of preparing rare earth photoluminescent materials, gasified oil and high-value syngas products based on the harvested materials of rare earth super-enriched plants; the whole process is simple to operate, green and efficient, and the obtained product has high optical properties, calorific value and output value, and has both economic value and environmental benefits, and has broad application prospects in the field of comprehensive resource utilization of rare earth super-enriched plants.
附图说明BRIEF DESCRIPTION OF THE DRAWINGS
图1为本发明基于稀土超富集植物制备光致发光材料、气化油与合成气的流程图。FIG1 is a flow chart of the present invention for preparing photoluminescent materials, gasified oil and synthetic gas based on rare earth super-enriched plants.
图2为本发明实施例1、2、3所得产物稀土掺杂硫化钙材料的XRD图。FIG. 2 is an XRD diagram of the rare earth-doped calcium sulfide material obtained as the product in Examples 1, 2, and 3 of the present invention.
图3为本发明实施例1所得产物稀土掺杂发光材料的光学性质色坐标图。FIG3 is a color coordinate diagram of the optical properties of the rare earth-doped luminescent material obtained as a product in Example 1 of the present invention.
图4为本发明实施例2所得产物稀土掺杂发光材料的光学性质色坐标图。FIG. 4 is a color coordinate diagram of the optical properties of the rare earth-doped luminescent material obtained as a product in Example 2 of the present invention.
图5为本发明实施例3所得产物稀土掺杂发光材料的光学性质色坐标图。FIG. 5 is a color coordinate diagram of the optical properties of the rare earth-doped luminescent material obtained as a product in Example 3 of the present invention.
图6为本发明实施例4所得产物稀土掺杂发光材料的光学性质色坐标图。FIG. 6 is a color coordinate diagram of the optical properties of the rare earth-doped luminescent material obtained as a product in Example 4 of the present invention.
图7为本发明对比例1所得无稀土掺杂空白样品的光学性质色坐标图。FIG. 7 is a color coordinate diagram of the optical properties of a blank sample without rare earth doping obtained in Comparative Example 1 of the present invention.
具体实施方式DETAILED DESCRIPTION
以下结合说明书附图和具体实施例来进一步说明本发明,但实施例并不对本发明做任何形式的限定。除非特别说明,本发明采用的试剂、方法和设备为本技术领域常规试剂、方法和设备。The present invention is further described below in conjunction with the accompanying drawings and specific examples, but the examples do not limit the present invention in any form. Unless otherwise specified, the reagents, methods and equipment used in the present invention are conventional reagents, methods and equipment in the art.
除非特别说明,以下实施例所用试剂和材料均为市购。Unless otherwise specified, the reagents and materials used in the following examples are commercially available.
本发明实施例制备光致发光材料的流程参见图1,具体步骤参见以下实施例。The process of preparing the photoluminescent material in the embodiment of the present invention is shown in FIG1 , and the specific steps are shown in the following embodiments.
实施例1一种基于稀土超富集植物美洲商陆Ce1制备光致发光材料的方法Example 1 A method for preparing a photoluminescent material based on rare earth hyperaccumulator plant Phytolacca americana Ce1
所述稀土超富集植物美洲商陆Ce1为CeCl3胁迫水培美洲商陆所得,Ce1样品粉末Ce含量为978mg/kg。The rare earth hyperaccumulator plant Phytolacca americana Ce1 is obtained by hydroponically cultivating Phytolacca americana under CeCl 3 stress, and the Ce content of the Ce1 sample powder is 978 mg/kg.
材料制备具体包括以下步骤:The material preparation specifically includes the following steps:
S1、将稀土超富集植物收获物水培美洲商陆Ce1样品风干,采用破碎机破碎成均匀粉末,取用粉末状样品2g置于水热反应釜内衬中,并加入5mL 0.4mol/L硫酸与35mL乙醇,将密闭反应釜置于烘箱中160℃溶剂热反应2h,冷却至室温,收集、分离,得到固相产物;S1. The hydroponic American pokeweed Ce1 sample of the rare earth super-enriched plant harvest was air-dried and crushed into uniform powder using a crusher. 2 g of the powdered sample was placed in the lining of a hydrothermal reactor, and 5 mL of 0.4 mol/L sulfuric acid and 35 mL of ethanol were added. The sealed reactor was placed in an oven for solvothermal reaction at 160°C for 2 h, cooled to room temperature, collected and separated to obtain a solid phase product.
S2、将步骤S1所得固相产物0.53g,采用ICP-OES、ICP-MS分析金属含量,发现95.03%的Ce与92.57%的Ca仍保留在固相产物中;S2. 0.53 g of the solid phase product obtained in step S1 was analyzed for metal content by ICP-OES and ICP-MS, and it was found that 95.03% of Ce and 92.57% of Ca were still retained in the solid phase product;
S3、将步骤S1所得固相产物进行水蒸气气化实验,气化温度为900℃,时间为15min,水蒸气流量为100μL/min,载气为氮气,氮气流速为100mL/min,气化油产物由异丙醇吸收收集,合成气气体由气袋收集,反应结束后,冷却得到淡黄色固体粉末产物;S3, the solid phase product obtained in step S1 was subjected to a water vapor gasification experiment, the gasification temperature was 900°C, the time was 15 min, the water vapor flow rate was 100 μL/min, the carrier gas was nitrogen, the nitrogen flow rate was 100 mL/min, the gasified oil product was absorbed and collected by isopropanol, and the synthesis gas was collected by an air bag. After the reaction was completed, it was cooled to obtain a light yellow solid powder product;
S4、对步骤S3所得淡黄色固体粉末产物进行XRD检测,结果如图2所示,样品衍射峰与CaS(PDF#08-0464)、CeO2(PDF#04-0593)标准卡片匹配,证明固体粉末含CaS、CeO2。对淡黄色固体粉末产物进行荧光光谱分析,数据显示450nm激发光谱下在513nm获得最大的发射光谱,其强度达到367606.63a.u.。光学性质色坐标图如图3所示,其CIE色坐标为(0.4136,0.5265),表明制备得到稀土掺杂CaS光致发光材料具有黄绿色荧光。S4. Perform XRD detection on the light yellow solid powder product obtained in step S3. The result is shown in FIG2. The diffraction peak of the sample matches the standard cards of CaS (PDF#08-0464) and CeO 2 (PDF#04-0593), proving that the solid powder contains CaS and CeO 2. Perform fluorescence spectrum analysis on the light yellow solid powder product. The data show that the maximum emission spectrum is obtained at 513 nm under the 450 nm excitation spectrum, and the intensity reaches 367606.63 au. The optical property color coordinate diagram is shown in FIG3. The CIE color coordinates are (0.4136, 0.5265), indicating that the prepared rare earth doped CaS photoluminescent material has yellow-green fluorescence.
S5、采用气相色谱分析步骤S3所收集合成气,结果显示H2、CO和CH4的产量依次为18.51mL/g、97.87mL/g和2.44mL/g。S5. Analyze the synthesis gas collected in step S3 by gas chromatography. The result shows that the yields of H 2 , CO and CH 4 are 18.51 mL/g, 97.87 mL/g and 2.44 mL/g respectively.
实施例2一种基于稀土超富集植物美洲商陆Ce2制备稀土光致发光材料的方法Example 2 A method for preparing rare earth photoluminescent materials based on rare earth hyperaccumulator plant Phytolacca americana Ce2
所述稀土超富集植物美洲商陆Ce2为CeCl3胁迫水培美洲商陆所得,Ce2样品粉末Ce含量为2026mg/kg。The rare earth hyperaccumulator plant Phytolacca americana Ce2 is obtained by hydroponically cultivating Phytolacca americana under CeCl 3 stress, and the Ce content of the Ce2 sample powder is 2026 mg/kg.
材料制备具体包括以下步骤:The material preparation specifically includes the following steps:
S1、将稀土超富集植物收获物水培美洲商陆Ce2样品风干,采用破碎机破碎成均匀粉末,取用粉末状样品2g置于水热反应釜内衬中,并加入5mL 0.4mol/L硫酸与35mL乙醇,将密闭反应釜置于烘箱中160℃溶剂热反应2h,冷却至室温,收集、分离,得到固相产物;S1. The hydroponic Ce2 sample of rare earth super-enriched plant harvested from American pokeweed was air-dried and crushed into uniform powder using a crusher. 2 g of the powdered sample was placed in the lining of a hydrothermal reactor, and 5 mL of 0.4 mol/L sulfuric acid and 35 mL of ethanol were added. The sealed reactor was placed in an oven at 160°C for solvothermal reaction for 2 h, cooled to room temperature, collected and separated to obtain a solid phase product.
S2、将步骤S1所得固相产物0.67g,采用ICP-OES、ICP-MS分析金属含量,发现97.03%的Ce与94.48%的Ca仍保留在固相产物中;S2. 0.67 g of the solid phase product obtained in step S1 was analyzed for metal content by ICP-OES and ICP-MS, and it was found that 97.03% of Ce and 94.48% of Ca were still retained in the solid phase product;
S3、将步骤S1所得固相产物进行水蒸气气化实验,气化温度为850℃,时间为10min,水蒸气流量为100μL/min,载气为氮气,氮气流速为100mL/min,气化油产物由异丙醇吸收收集,合成气气体由气袋收集,反应结束后,冷却得到淡黄色固体粉末产物;S3, the solid phase product obtained in step S1 was subjected to a water vapor gasification experiment, the gasification temperature was 850°C, the time was 10 min, the water vapor flow rate was 100 μL/min, the carrier gas was nitrogen, the nitrogen flow rate was 100 mL/min, the gasified oil product was absorbed and collected by isopropanol, and the synthesis gas was collected by an air bag. After the reaction was completed, it was cooled to obtain a light yellow solid powder product;
S4、对步骤S3所得淡黄色固体粉末产物进行XRD检测,如图2所示,样品衍射峰与CaS(PDF#08-0464)、CeO2(PDF#04-0593)标准卡片匹配,证明固体粉末含CaS、CeO2。对淡黄色固体粉末产物进行荧光光谱分析,数据显示450nm激发光谱下在510nm获得最大的发射光谱,其强度达到432270.78a.u.。光学性质色坐标图如图4所示,其CIE色坐标为(0.4015,0.5337),表明制备得到稀土掺杂CaS光致发光材料具有黄绿色荧光。S4. Perform XRD detection on the light yellow solid powder product obtained in step S3. As shown in FIG2 , the diffraction peaks of the sample match the standard cards of CaS (PDF#08-0464) and CeO 2 (PDF#04-0593), proving that the solid powder contains CaS and CeO 2 . Fluorescence spectrum analysis is performed on the light yellow solid powder product. The data show that the maximum emission spectrum is obtained at 510 nm under the 450 nm excitation spectrum, and the intensity reaches 432270.78 au. The color coordinate diagram of optical properties is shown in FIG4 , and its CIE color coordinates are (0.4015, 0.5337), indicating that the prepared rare earth doped CaS photoluminescent material has yellow-green fluorescence.
S5、采用气相色谱分析步骤S3所收集合成气,结果显示H2、CO和CH4的产量依次为30.35mL/g、129.34mL/g和2.05mL/g。S5. Analyze the synthesis gas collected in step S3 by gas chromatography. The results show that the yields of H 2 , CO and CH 4 are 30.35 mL/g, 129.34 mL/g and 2.05 mL/g, respectively.
实施例3一种基于稀土超富集植物美洲商陆Ce2制备稀土光致发光材料的方法Example 3 A method for preparing rare earth photoluminescent materials based on rare earth hyperaccumulator plant Phytolacca americana Ce2
所述稀土超富集植物美洲商陆Ce2为CeCl3胁迫水培美洲商陆所得,Ce2样品粉末Ce含量为2026mg/kg。The rare earth hyperaccumulator plant Phytolacca americana Ce2 is obtained by hydroponically cultivating Phytolacca americana under CeCl 3 stress, and the Ce content of the Ce2 sample powder is 2026 mg/kg.
材料制备具体包括以下步骤:The material preparation specifically includes the following steps:
S1、将稀土超富集植物收获物水培美洲商陆Ce2样品风干,采用破碎机破碎成均匀粉末,取用粉末状样品2g置于水热反应釜内衬中,并加入5mL 0.4mol/L硫酸与35mL乙醇,将密闭反应釜置于烘箱中160℃溶剂热反应2h,冷却至室温,收集、分离,得到固相产物;S1. The hydroponic Ce2 sample of rare earth super-enriched plant harvested from American pokeweed was air-dried and crushed into uniform powder using a crusher. 2 g of the powdered sample was placed in the lining of a hydrothermal reactor, and 5 mL of 0.4 mol/L sulfuric acid and 35 mL of ethanol were added. The sealed reactor was placed in an oven at 160°C for solvothermal reaction for 2 h, cooled to room temperature, collected and separated to obtain a solid phase product.
S2、将步骤S1所得固相产物0.67g,采用ICP-OES、ICP-MS分析金属含量,发现97.03%的Ce与94.48%的Ca仍保留在固相产物中;S2. 0.67 g of the solid phase product obtained in step S1 was analyzed for metal content by ICP-OES and ICP-MS, and it was found that 97.03% of Ce and 94.48% of Ca were still retained in the solid phase product;
S3、将步骤S1所得固相产物进行水蒸气气化实验,气化温度为850℃,时间为10min,水蒸气流量为10μL/min,载气为氮气,氮气流速为100mL/min,气化油产物由异丙醇吸收收集,合成气气体由气袋收集,反应结束后,冷却得到淡黄色固体粉末产物;S3, the solid phase product obtained in step S1 is subjected to a water vapor gasification experiment, the gasification temperature is 850°C, the time is 10 min, the water vapor flow rate is 10 μL/min, the carrier gas is nitrogen, the nitrogen flow rate is 100 mL/min, the gasified oil product is absorbed and collected by isopropanol, and the synthesis gas is collected by an air bag. After the reaction is completed, it is cooled to obtain a light yellow solid powder product;
S4、对步骤S3所得淡黄色固体粉末产物进行XRD检测,如图2所示,样品衍射峰与CaS(PDF#08-0464)、CeO2(PDF#04-0593)标准卡片匹配,证明固体粉末含CaS、CeO2。对淡黄色固体粉末产物进行荧光光谱分析,数据显示450nm激发光谱下在515nm获得最大的发射光谱,其强度达到368590.03a.u.。光学性质色坐标图如图5所示,其CIE色坐标为(0.4446,0.5094),表明制备得到稀土掺杂CaS光致发光材料具有黄绿色荧光。S4. Perform XRD detection on the light yellow solid powder product obtained in step S3. As shown in FIG2 , the diffraction peaks of the sample match the standard cards of CaS (PDF#08-0464) and CeO 2 (PDF#04-0593), proving that the solid powder contains CaS and CeO 2 . Fluorescence spectrum analysis is performed on the light yellow solid powder product. The data show that the maximum emission spectrum is obtained at 515 nm under the 450 nm excitation spectrum, and the intensity reaches 368590.03 au. The optical property color coordinate diagram is shown in FIG5 , and its CIE color coordinates are (0.4446, 0.5094), indicating that the prepared rare earth doped CaS photoluminescent material has yellow-green fluorescence.
S5、采用气相色谱分析步骤S3所收集合成气,结果显示H2、CO和CH4的产量依次为24.38mL/g、140.85mL/g和4.91mL/g。S5. Analyze the synthesis gas collected in step S3 by gas chromatography. The results show that the yields of H 2 , CO and CH 4 are 24.38 mL/g, 140.85 mL/g and 4.91 mL/g, respectively.
实施例4一种基于稀土超富集植物美洲商陆La2制备稀土光致发光材料的方法Example 4 A method for preparing rare earth photoluminescent materials based on rare earth hyperaccumulator plant Phytolacca americana La2
所述稀土超富集植物美洲商陆La2为LaCl3胁迫水培美洲商陆所得,La2样品粉末La含量为2042mg/kg。The rare earth hyperaccumulator plant Phytolacca americana La2 is obtained by hydroponically cultivating Phytolacca americana under LaCl 3 stress, and the La content of the La2 sample powder is 2042 mg/kg.
材料制备具体包括以下步骤:The material preparation specifically includes the following steps:
S1、将稀土超富集植物收获物水培美洲商陆La2样品风干,采用破碎机破碎成均匀粉末,取用粉末状样品2g置于水热反应釜内衬中,并加入5mL 0.4mol/L硫酸与35mL乙醇,将密闭反应釜置于烘箱中160℃溶剂热反应2h,冷却至室温,收集、分离,得到固相产物;S1. The La2 sample of the rare earth super-enriched plant harvested from hydroponic culture of American pokeweed was air-dried and crushed into uniform powder using a crusher. 2 g of the powdered sample was placed in the lining of a hydrothermal reactor, and 5 mL of 0.4 mol/L sulfuric acid and 35 mL of ethanol were added. The sealed reactor was placed in an oven for solvothermal reaction at 160°C for 2 h, cooled to room temperature, collected and separated to obtain a solid phase product.
S2、将步骤S1所得固相产物0.56g,采用ICP-OES、ICP-MS分析金属含量,发现90.59%的La与92.44%的Ca仍保留在固相产物中;S2. 0.56 g of the solid phase product obtained in step S1 was analyzed for metal content by ICP-OES and ICP-MS, and it was found that 90.59% of La and 92.44% of Ca were still retained in the solid phase product;
S3、将步骤S1所得固相产物进行水蒸气气化实验,气化温度为850℃,时间为20min,水蒸气流量为100μL/min,载气为氮气,氮气流速为100mL/min,气化油产物由异丙醇吸收收集,合成气气体由气袋收集,反应结束后,冷却得到白色固体粉末产物;S3, the solid phase product obtained in step S1 was subjected to a water vapor gasification experiment, the gasification temperature was 850°C, the time was 20 min, the water vapor flow rate was 100 μL/min, the carrier gas was nitrogen, the nitrogen flow rate was 100 mL/min, the gasified oil product was absorbed and collected by isopropanol, and the synthesis gas was collected by an air bag. After the reaction was completed, it was cooled to obtain a white solid powder product;
S4、对步骤S3所得白色固体粉末产物进行荧光光谱分析,数据显示265nm激发光谱下在591nm获得最大的发射光谱,其强度达到3879978.5a.u.。光学性质色坐标图如图6所示,其CIE色坐标为(0.5407,0.4522),表明制备得到稀土掺杂CaS光致发光材料具有橙黄色荧光。S4. The white solid powder product obtained in step S3 is subjected to fluorescence spectrum analysis. The data show that the maximum emission spectrum is obtained at 591 nm under the 265 nm excitation spectrum, and the intensity reaches 3879978.5 a.u. The optical property color coordinate diagram is shown in FIG6 , and its CIE color coordinate is (0.5407, 0.4522), indicating that the prepared rare earth doped CaS photoluminescent material has orange-yellow fluorescence.
S5、采用气相色谱分析步骤S3所收集合成气,结果显示H2、CO和CH4的产量依次为17.02mL/g、117.73mL/g和1.85mL/g。S5. Analyze the synthesis gas collected in step S3 by gas chromatography. The results show that the yields of H 2 , CO and CH 4 are 17.02 mL/g, 117.73 mL/g and 1.85 mL/g, respectively.
对比例1一种超富集植物美洲商陆CK的处理方法Comparative Example 1 A method for treating a hyperaccumulator plant Phytolacca americana CK
所述超富集植物美洲商陆CK为无稀土胁迫水培美洲商陆所得,是不含稀土的空白样品粉末;处理方法具体包括以下步骤:The hyperaccumulator plant Phytolacca americana CK is obtained by hydroponically cultivating Phytolacca americana without rare earth stress, and is a blank sample powder that does not contain rare earths; the processing method specifically comprises the following steps:
S1、将稀土超富集植物收获物水培美洲商陆CK样品风干,采用破碎机破碎成均匀粉末,取用粉末状样品2g置于水热反应釜内衬中,并加入5mL 0.4mol/L硫酸与35mL乙醇,将密闭反应釜置于烘箱中160℃溶剂热反应2h,冷却至室温,收集、分离,得到固相产物;S1. The hydroponic American pokeweed CK sample of the rare earth super-enriched plant harvest was air-dried and crushed into uniform powder using a crusher. 2 g of the powdered sample was placed in the lining of a hydrothermal reactor, and 5 mL of 0.4 mol/L sulfuric acid and 35 mL of ethanol were added. The sealed reactor was placed in an oven for solvothermal reaction at 160°C for 2 h, cooled to room temperature, collected and separated to obtain a solid phase product.
S2、将步骤S1所得固相产物0.51g,采用ICP-OES分析金属含量,发现87.56%的Ca仍保留在固相产物中;S2. 0.51 g of the solid phase product obtained in step S1 was analyzed for metal content by ICP-OES, and it was found that 87.56% of Ca was still retained in the solid phase product;
S3、将步骤S1所得固相产物进行水蒸气气化实验,气化温度为850℃,时间为10min,水蒸气流量为100μL/min,载气为氮气,氮气流速为100mL/min,气化油产物由异丙醇吸收收集,合成气气体由气袋收集,反应结束后,冷却得到白色固体粉末产物;S3, the solid phase product obtained in step S1 was subjected to a water vapor gasification experiment, the gasification temperature was 850°C, the time was 10 min, the water vapor flow rate was 100 μL/min, the carrier gas was nitrogen, the nitrogen flow rate was 100 mL/min, the gasified oil product was absorbed and collected by isopropanol, and the synthesis gas was collected by an air bag. After the reaction was completed, it was cooled to obtain a white solid powder product;
S4、对步骤S3所得白色固体粉末产物进行荧光光谱分析,如图7所示,其CIE色坐标为(0.5407,0.4522),且该样品在蓝光照射下无明显荧光,表明无稀土掺杂CaS样品不具备实施例中的稀土发光材料的荧光性能。S4. Fluorescence spectrum analysis is performed on the white solid powder product obtained in step S3. As shown in FIG7 , its CIE color coordinates are (0.5407, 0.4522), and the sample has no obvious fluorescence under blue light irradiation, indicating that the non-rare earth-doped CaS sample does not have the fluorescence properties of the rare earth luminescent material in the embodiment.
上述实施例为本发明较佳的实施方式,但本发明的实施方式并不受上述实施例的限制,其他的任何未背离本发明的精神实质与原理下所作的改变、修饰、替代、组合、简化,均应为等效的置换方式,都包含在本发明的保护范围之内。The above embodiments are preferred implementation modes of the present invention, but the implementation modes of the present invention are not limited to the above embodiments. Any other changes, modifications, substitutions, combinations, and simplifications that do not deviate from the spirit and principles of the present invention should be equivalent replacement methods and are included in the protection scope of the present invention.
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