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CN103866129B - A kind of recovery method of CdTe solar module - Google Patents

A kind of recovery method of CdTe solar module Download PDF

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CN103866129B
CN103866129B CN201410090916.0A CN201410090916A CN103866129B CN 103866129 B CN103866129 B CN 103866129B CN 201410090916 A CN201410090916 A CN 201410090916A CN 103866129 B CN103866129 B CN 103866129B
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magnetic polymer
cdte
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cdte solar
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CN103866129A (en
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张腾
董泽斌
古宏伟
屈飞
丁发柱
彭星煜
王洪艳
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Institute of Electrical Engineering of CAS
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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    • Y02P10/00Technologies related to metal processing
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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    • Y02W30/82Recycling of waste of electrical or electronic equipment [WEEE]

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Abstract

一种CdTe太阳能电池组件的回收方法,其特征在于:将去除了EVA封装胶的CdTe太阳能电池玻璃组件浸没于硫酸/双氧水溶液中充分酸蚀后,采用磁性聚合物微球直接、快速地从CdTe的酸蚀溶液中富集Cd和Te元素,获得的高浓度Cd和Te酸蚀溶液可进一步用于电解过程。此回收过程具有富集分离效率高、工艺过程简单和易于实现放大等特点,磁性聚合物微球可再生利用。

A method for recovering CdTe solar cell components, characterized in that: after the CdTe solar cell glass components from which the EVA encapsulation glue has been removed are fully etched in sulfuric acid/hydrogen peroxide solution, magnetic polymer microspheres are used to directly and rapidly remove the CdTe solar cell components Cd and Te elements are enriched in the acid etching solution, and the obtained high concentration Cd and Te etching solution can be further used in the electrolysis process. This recovery process has the characteristics of high enrichment and separation efficiency, simple process and easy realization of scale-up, and the magnetic polymer microspheres can be recycled.

Description

一种CdTe太阳能电池组件的回收方法A kind of recovery method of CdTe solar cell module

技术领域technical field

本发明涉及光伏组件回收技术,特别涉及一种碲化镉薄膜太阳能电池的回收处理方法。The invention relates to the recycling technology of photovoltaic modules, in particular to a method for recycling and processing cadmium telluride thin-film solar cells.

背景技术Background technique

碲化镉(CdTe)是一种适用于太阳能转换的商业化半导体材料,具有极好的吸光特性和高温下出色的组件性能。近年来,随着CdTe电池技术的不断完善,其组件的转换效率已提高至16.1%(0.72m2组件),继晶硅电池之后占据了太阳能电池的第二大市场份额、2012年其组件产能已达1.8GWp。EPIA预计:至2020年,CdTe太阳能电池的市场份额将超过10%。然而,快速增长的产能势必将导致两大问题:一、有毒Cd元素对环境的潜在危害;二、作为稀缺元素的Te在未来供应不足。因此,开发一种针对废弃CdTe电池组件的合适回收方法将显得尤为重要。Cadmium telluride (CdTe) is a commercially available semiconductor material for solar energy conversion, with excellent light-absorbing properties and excellent module performance at high temperatures. In recent years, with the continuous improvement of CdTe battery technology, the conversion efficiency of its components has increased to 16.1% (0.72m 2 components), occupying the second largest market share of solar cells after crystalline silicon cells, and its component production capacity in 2012 Has reached 1.8GWp . EPIA predicts that by 2020, the market share of CdTe solar cells will exceed 10%. However, the rapid growth of production capacity will inevitably lead to two major problems: first, the potential harm of the toxic Cd element to the environment; second, the insufficient supply of Te as a scarce element in the future. Therefore, it will be particularly important to develop a suitable recycling method for waste CdTe battery components.

一系列CdTe太阳能电池的回收技术已被报道和实施。其中,结合酸蚀液溶解和湿法冶金技术不但适合各种类型的废弃CdTe太阳电池,而且容易在短期内实现商业应用。美国FirstSolar公司采用硫酸/双氧水体系酸蚀组件中的CdTe层,随后采用氢氧化钠逐级沉降的方法富集Cd和Te元素;由于Te元素的化合物种类和溶解度受溶液pH值变化影响较大,导致溶液中不可避免的残余大量Te元素、且溶液pH值控制难度高。世界专利No.WO2006/130715A2描述了采用离子交换柱分离的方法分离回收CdTe酸蚀液中的Cd和Te元素,但柱压会限制酸蚀液的处理量;且离子交换过程造成的树脂污染和交换柱堵塞使得交换柱更新过程繁琐。美国专利No.US005997718A描述了采用电解的方法从CdTe酸蚀液中分离Te元素,但对于低浓度的酸蚀液而言电解效率低、经济性较差。因此,亟待开发一种能直接从CdTe酸蚀液中富集Cd和Te离子的高效且处理量大富集分离方法。A series of recycling techniques for CdTe solar cells have been reported and implemented. Among them, the combination of acid etching solution dissolution and hydrometallurgy technology is not only suitable for various types of waste CdTe solar cells, but also easy to realize commercial application in a short period of time. FirstSolar Company of the United States uses sulfuric acid/hydrogen peroxide system to acid-etch the CdTe layer in the module, and then adopts the method of sodium hydroxide step-by-step precipitation to enrich Cd and Te elements; since the compound type and solubility of Te element are greatly affected by the change of solution pH value, This results in an unavoidable large amount of Te element remaining in the solution, and it is difficult to control the pH value of the solution. World Patent No.WO2006/130715A2 describes the separation and recovery of Cd and Te elements in the CdTe etching solution by means of ion exchange column separation, but the column pressure will limit the treatment capacity of the acid etching solution; and the resin pollution caused by the ion exchange process and A clogged exchange column makes the exchange column renewal process cumbersome. US Patent No. US005997718A describes the separation of Te elements from CdTe etching solution by electrolysis, but the electrolysis efficiency is low and the economy is poor for low concentration etching solution. Therefore, it is urgent to develop an efficient and large-capacity enrichment and separation method that can directly enrich Cd and Te ions from the CdTe etching solution.

发明内容Contents of the invention

本发明的目的是克服现有回收技术中需使用大量化学沉淀剂、离子交换柱易污染和堵塞、对低浓度酸蚀液处理效率低等缺点,提出一种碲化镉太阳能电池组件的回收处理方法。The purpose of the present invention is to overcome the disadvantages of using a large amount of chemical precipitant in the existing recovery technology, the ion exchange column is easy to pollute and block, and the treatment efficiency of low-concentration acid etching solution is low, and proposes a recovery process for cadmium telluride solar cell components method.

本发明采用具有磁性的聚合物微球直接快速地从CdTe的酸蚀溶液中富集Cd和Te元素,然后依次通过磁分离和稀酸洗涤的方法获得高浓度含Cd和Te的溶液,该溶液可用于进一步电解分离Cd元素。磁性的聚合物微球经NaOH溶液再生处理后可重复用于上述吸附分离过程。The present invention uses magnetic polymer microspheres to directly and rapidly enrich Cd and Te elements from the CdTe acid etching solution, and then sequentially obtains a solution containing high concentrations of Cd and Te through magnetic separation and dilute acid washing. Can be used for further electrolytic separation of Cd elements. The magnetic polymer microspheres can be reused in the above adsorption separation process after being regenerated with NaOH solution.

首先将去除了EVA封装胶的CdTe太阳能电池玻璃组件浸没在含有硫酸和双氧水的酸蚀液中,随后采用具有磁性的聚合物微球从CdTe的酸蚀溶液中富集Cd和Te元素,并依次通过磁分离和稀酸洗涤的方法获得含Cd和Te的溶液。Firstly, the CdTe solar cell glass assembly from which the EVA encapsulant was removed was immersed in an acid etching solution containing sulfuric acid and hydrogen peroxide, and then the Cd and Te elements were enriched from the CdTe acid etching solution using magnetic polymer microspheres, and sequentially A solution containing Cd and Te was obtained by magnetic separation and dilute acid washing.

本发明具体回收工艺步骤如下:Concrete recovery process step of the present invention is as follows:

(1)首先,将去除了EVA封装胶的CdTe太阳能电池玻璃组件浸没于硫酸/双氧水的复合酸蚀液中充分酸蚀,经固液分离后获得含有Cd和Te元素的酸蚀溶液;所得酸蚀溶液可再次用来酸蚀去除了EVA封装胶的CdTe太阳能电池玻璃组件。其中,去除了EVA封装胶的CdTe太阳能电池玻璃组件、浓度为1.0mol/L硫酸溶液和双氧水的用量比为1kg:478mL:4.8mL;(1) First, immerse the CdTe solar cell glass assembly from which the EVA encapsulant has been removed in a compound acid etching solution of sulfuric acid/hydrogen peroxide and etch fully, and obtain an acid etching solution containing Cd and Te elements after solid-liquid separation; the obtained acid The etching solution can be used again to etch the CdTe solar cell glass assembly from which the EVA encapsulant has been removed. Among them, the dosage ratio of the CdTe solar cell glass module with the EVA encapsulant removed, sulfuric acid solution with a concentration of 1.0mol/L and hydrogen peroxide is 1kg: 478mL: 4.8mL;

(2)其次,将磁性聚合物微球加入到步骤(1)制得的酸蚀液中,充分搅拌10min后,采用磁分离装置分离表面吸附了Cd和Te元素的磁性聚合物微球,分离处理后的溶液中仅含Te元素。磁性聚合物微球的具体结构为:以Fe3O4SiO2为磁核,该磁核包埋于苯乙烯-二乙烯基苯共聚物微球中,微球表面具有磺酸钠基团;(2) Next, add the magnetic polymer microspheres to the acid etching solution prepared in step (1), and after fully stirring for 10 minutes, use a magnetic separation device to separate the magnetic polymer microspheres with Cd and Te elements adsorbed on the surface, and separate The treated solution contains only Te element. The specific structure of magnetic polymer microspheres is as follows: Fe 3 O 4 SiO 2 is used as the magnetic core, which is embedded in styrene-divinylbenzene copolymer microspheres, and the surface of the microspheres has sodium sulfonate groups;

(3)最后,依次采用0.1M稀酸溶液和0.1MNaOH溶液洗涤表面吸附了Cd和Te元素的磁性聚合物微球,可获得含有Cd和Te元素的溶液,吸附了Cd和Te元素的磁性聚合物微球经过酸洗再生后可再次用于吸附过程,即再次用于吸附CdTe酸蚀液。上述吸附-再生过程反复数次可获得含有Cd和Te元素的高浓度洗脱溶液,可被用于进一步电解分离Cd;(3) Finally, the magnetic polymer microspheres with Cd and Te elements adsorbed on the surface are washed sequentially with 0.1M dilute acid solution and 0.1M NaOH solution to obtain a solution containing Cd and Te elements, and the magnetic polymerization of Cd and Te elements is adsorbed After pickling and regenerating, the microspheres can be used again in the adsorption process, that is, they can be used to adsorb CdTe acid etching solution again. The above adsorption-regeneration process is repeated several times to obtain a high-concentration elution solution containing Cd and Te elements, which can be used for further electrolytic separation of Cd;

(4)总之,本工艺采用磁分离方法从酸蚀液中分离Cd和Te元素。(4) In short, this process adopts the magnetic separation method to separate Cd and Te elements from the acid etching solution.

与现有技术相比,本发明的优点是:1)从CdTe酸蚀液中直接富集和去除Cd和Te元素,避免碱溶液分级沉降工艺中溶液pH值控制难、酸碱液用量大的缺点;2)采用磁分离过程分离速度快,数秒钟可实现将金属离子从酸蚀液中分离出来,磁性聚合物微球再生过程方便,避免离子交换柱形式中交换柱堵塞、处理量小的缺点;3)各种浓度的CdTe酸蚀溶液在电解分离过程之前均可采用此过程进行反复富集,工艺过程简单、易于实现放大。Compared with the prior art, the advantages of the present invention are: 1) The Cd and Te elements are directly enriched and removed from the CdTe acid etching solution, avoiding the difficulty in controlling the pH value of the solution and the large amount of acid and alkali solution used in the stepwise sedimentation process of the alkaline solution Disadvantages; 2) The magnetic separation process has a fast separation speed, and the metal ions can be separated from the acid etching solution in a few seconds. The regeneration process of the magnetic polymer microspheres is convenient, and the exchange column blockage in the form of an ion exchange column is avoided, and the processing capacity is small. Disadvantages; 3) Various concentrations of CdTe acid etching solutions can be repeatedly enriched by this process before the electrolytic separation process, and the process is simple and easy to scale up.

附图说明Description of drawings

图1CdTe两次酸蚀过程中Cd和Te浓度与酸蚀时间的关系;Figure 1 The relationship between the concentration of Cd and Te and the etching time during the two acid etching processes of CdTe;

图2磁性聚合物微球用量对CdTe酸蚀液中Cd和Te元素的去除影响;The influence of the amount of magnetic polymer microspheres on the removal of Cd and Te elements in CdTe acid etching solution in Fig. 2;

图3磁性聚合物微球对CdTe酸蚀液中Cd和Te元素的去除能力;The removal ability of Cd and Te elements in CdTe acid etching solution by magnetic polymer microspheres in Fig. 3;

图4磁性聚合物微球的红外光谱;The infrared spectrum of Fig. 4 magnetic polymer microsphere;

图5磁性聚合物微球的扫描电镜照片和能谱分析;Scanning electron micrograph and energy spectrum analysis of Fig. 5 magnetic polymer microsphere;

图6磁性聚合物微球的磁滞回线。Fig. 6 Hysteresis loops of magnetic polymer microspheres.

具体实施方式detailed description

1)将1公斤已去除EVA封装胶的CdTe太阳能电池玻璃组件浸没在含有硫酸和双氧水的酸蚀液中,CdTe太阳能电池组件、1.0M硫酸和双氧水的用量比为1kg:478mL:4.8mL,经过两次酸蚀后Cd和Te的平衡浓度分别为2274ppm和2720ppm如图1所示。1) Immerse 1 kg of CdTe solar cell glass assembly from which the EVA encapsulant has been removed in an acid etching solution containing sulfuric acid and hydrogen peroxide. The equilibrium concentrations of Cd and Te after two times of acid etching are 2274ppm and 2720ppm, respectively, as shown in Figure 1.

2)将磁性聚合物微球加入到CdTe的二次酸蚀液中,充分搅拌10min后采用磁分离装置分离表面已吸附了Cd和Te元素的磁性聚合物微球。考察磁性聚合物微球对5mLCdTe二次酸蚀液中Cd和Te的去除能力可见:随着吸附剂用量的增加,对Cd和Te的去除率显著提高;100%Cd和80%Te能被吸附分离,如见图2所示。将5mLCdTe二次酸蚀液用去离子水稀释5倍后,加入2.5g磁性聚合物微球充分搅拌10min达到吸附平衡;在磁分离后所得的溶液中再次加入2.5g磁性聚合物微球,上述过程反复五次,最终100%Cd和80%Te能被吸附分离,如图3所示。将处理后的溶液中仅含Te元素,可用于再次富集;2) Add the magnetic polymer microspheres into the secondary acid etching solution of CdTe, and after fully stirring for 10 minutes, use a magnetic separation device to separate the magnetic polymer microspheres whose surface has adsorbed Cd and Te elements. Investigating the removal ability of magnetic polymer microspheres to Cd and Te in 5mL CdTe secondary acid etching solution, it can be seen that: with the increase of the amount of adsorbent, the removal rate of Cd and Te is significantly improved; 100% Cd and 80% Te can be adsorbed Separation, as shown in Figure 2. After diluting the 5mL CdTe secondary acid etching solution 5 times with deionized water, add 2.5g magnetic polymer microspheres and stir for 10min to reach adsorption equilibrium; add 2.5g magnetic polymer microspheres again to the solution obtained after magnetic separation, and The process was repeated five times, and finally 100% Cd and 80% Te could be separated by adsorption, as shown in Figure 3. The treated solution only contains Te element, which can be used for re-enrichment;

磁性聚合物微球表面具有磺酸基,如见图4和图5所示。磁性聚合物微球的磁饱和强度可达到8.2emu/g,如图6所示。如图4所示,在磁性聚合物微球的红外光谱中,3033cm-1处和1596,1500,and1447cm-1处的一组峰对应于苯乙烯-二乙烯基苯中苯环上的C-H伸缩振动峰,1195和1045cm-1处两峰对应于磺酸基。由图6磁性聚合物微球的扫描电镜照片和能谱分析结果可见,微球表面具有Fe、S、Si、C、O和Na元素,进一步证实磁性聚合物微球中含有Fe3O4SiO2核壳结构磁性粒子、苯乙烯-二乙烯基苯聚合物树脂基和磺酸钠基团。There are sulfonic acid groups on the surface of the magnetic polymer microsphere, as shown in Fig. 4 and Fig. 5 . The magnetic saturation strength of the magnetic polymer microspheres can reach 8.2emu/g, as shown in Figure 6. As shown in Fig. 4, in the infrared spectrum of magnetic polymer microspheres, a group of peaks at 3033 cm -1 and 1596, 1500, and 1447 cm -1 correspond to the stretching of CH on the benzene ring in styrene-divinylbenzene Vibration peaks, two peaks at 1195 and 1045 cm -1 correspond to sulfonic acid groups. From the scanning electron microscope photos and energy spectrum analysis results of the magnetic polymer microspheres in Figure 6, it can be seen that the surface of the microspheres has Fe, S, Si, C, O and Na elements, which further confirms that the magnetic polymer microspheres contain Fe 3 O 4 SiO 2 Core-shell structure magnetic particles, styrene-divinylbenzene polymer resin base and sodium sulfonate group.

3)将表面已吸附了Cd和Te元素的磁性聚合物微球倒入盛有0.1M稀酸溶液的储罐,搅拌10min后磁分离再生的聚合物微球,随后用0.1MNaOH溶液活化磁性聚合物微球,进而用于下一次吸附分离CdTe的二次酸蚀液。用于再生磁性聚合物的稀酸溶液储罐内,随吸附-磁分离-酸洗再生次数增多,洗脱液中所含Cd和Te离子浓度不断提高,可用做进一步电解分离Cd元素的母液。3) Pour the magnetic polymer microspheres with Cd and Te elements adsorbed on the surface into a storage tank containing a 0.1M dilute acid solution, stir for 10 minutes and magnetically separate the regenerated polymer microspheres, and then activate the magnetic polymerization with a 0.1M NaOH solution The material microspheres are then used for the secondary acid etching solution for the next adsorption and separation of CdTe. In the dilute acid solution storage tank used to regenerate magnetic polymers, as the number of adsorption-magnetic separation-pickling regeneration increases, the concentration of Cd and Te ions contained in the eluent continues to increase, which can be used as a mother solution for further electrolytic separation of Cd elements.

Claims (2)

1. the recovery method of a CdTe solar module, it is characterized in that first the CdTe solar battery glass assembly eliminating EVA packaging plastic being immersed in the pickling solution containing sulfuric acid and hydrogen peroxide, adopt the magnetic polymer microballoon of tool enrichment Cd and Te element from the pickling solution of CdTe subsequently, and obtain by the method for Magneto separate and weak acid scrubbing the solution containing Cd and Te successively; The structure of described magnetic polymer microsphere is: with Fe 3o 4siO 2for magnetic core, magnetic core is embedded in styrene diethylene benzene copoly mer microballoon, and microsphere surface has sodium group.
2. the recovery method of CdTe solar module according to claim 1, is characterized in that: the step of described recovery method is as follows:
(1) the CdTe solar battery glass assembly eliminating EVA packaging plastic is immersed in abundant acid etching in the compound pickling solution of sulfuric acid/hydrogen peroxide, after solid-liquid separation, obtains the pickling solution containing Cd and Te element; In pickling solution, eliminate the CdTe solar battery glass assembly of EVA packaging plastic, amount ratio that concentration is 1.0mol/L sulphuric acid soln and hydrogen peroxide is 1kg:478mL:4.8mL;
(2) magnetic polymer microsphere is joined in the obtained pickling solution of step (1), after abundant stirring 10min, magnetic separating device release surface is adopted to adsorb the magnetic polymer microsphere of Cd and Te element, only containing Te element in the pickling solution after separating treatment;
(3) 0.1M dilute acid soln and the 0.1MNaOH solution washing surface adsorption magnetic polymer microsphere of Cd and Te element is adopted successively; Obtain the solution containing Cd and Te element;
(4) magnetism separate method is adopted to be separated from pickling solution by Cd with Te element;
Above-mentioned absorption-Magneto separate-acid cleaning process can obtain for several times the higher elute soln of concentration containing Cd and Te element repeatedly;
Magnetic polymer microsphere in described step (3) can be recycled and reused for adsorption process after NaOH solution manipulation of regeneration.
CN201410090916.0A 2014-03-12 2014-03-12 A kind of recovery method of CdTe solar module Expired - Fee Related CN103866129B (en)

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