CN105355710B - A kind of solar cell machining process - Google Patents
A kind of solar cell machining process Download PDFInfo
- Publication number
- CN105355710B CN105355710B CN201510698101.5A CN201510698101A CN105355710B CN 105355710 B CN105355710 B CN 105355710B CN 201510698101 A CN201510698101 A CN 201510698101A CN 105355710 B CN105355710 B CN 105355710B
- Authority
- CN
- China
- Prior art keywords
- solar cells
- silver
- waste liquid
- silicon
- aluminum
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Classifications
-
- H—ELECTRICITY
- H10—SEMICONDUCTOR DEVICES; ELECTRIC SOLID-STATE DEVICES NOT OTHERWISE PROVIDED FOR
- H10F—INORGANIC SEMICONDUCTOR DEVICES SENSITIVE TO INFRARED RADIATION, LIGHT, ELECTROMAGNETIC RADIATION OF SHORTER WAVELENGTH OR CORPUSCULAR RADIATION
- H10F71/00—Manufacture or treatment of devices covered by this subclass
- H10F71/121—The active layers comprising only Group IV materials
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/50—Photovoltaic [PV] energy
- Y02E10/547—Monocrystalline silicon PV cells
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
Landscapes
- Photovoltaic Devices (AREA)
Abstract
本发明公开了一种能够降低生产成本且能够减少生产过程中废弃物排放的太阳能电池片加工工艺。该工艺包括硅片检测、表面制绒、扩散制结、去磷硅玻璃、湿法刻蚀、镀减反射膜、丝网印刷、快速烧结,利用太阳能电池片生产过程中产生的各种废液用于回收处理报废失效以及生产过程中产生的不合格太阳能电池片,不但避免了大量废液排放以及不合格太阳能电池片销毁造成的环境污染,同时回收的硅片、银包铜粉、铝浆可直接供应给太阳能电池片生产线,既做到了废液的重复利用,同时还减少了废弃物的产生,更加利用环保生产,可以大大降低太阳能电池片加工过程中原料的使用量,从而降低了太阳能电池片的生产成本。适合在太阳能电池领域推广应用。The invention discloses a solar cell sheet processing technology capable of reducing production cost and waste discharge in the production process. The process includes silicon wafer inspection, surface texturing, diffusion junction, phosphorus silicon glass removal, wet etching, anti-reflection coating, screen printing, rapid sintering, and the use of various waste liquids generated during the production of solar cells It is used to recycle and dispose of unqualified solar cells produced in the production process, which not only avoids a large amount of waste liquid discharge and environmental pollution caused by the destruction of unqualified solar cells, but also recycles silicon wafers, silver-coated copper powder, and aluminum paste. It can be directly supplied to the production line of solar cells, which not only achieves the reuse of waste liquid, but also reduces the generation of waste, and makes more use of environmentally friendly production, which can greatly reduce the amount of raw materials used in the processing of solar cells, thereby reducing solar energy. Production cost of cells. It is suitable for popularization and application in the field of solar cells.
Description
技术领域technical field
本发明涉及太阳能电池领域,尤其是一种太阳能电池片加工工艺。The invention relates to the field of solar cells, in particular to a process for processing solar cells.
背景技术Background technique
随着社会和经济的飞速发展,能源的需要日益增加,化石能源的日趋枯竭和给生态环境造成的污染,严重威胁着社会和经济的可持续发展。因此,迫切需要采用可再生能源进行替代。太阳能作为一种取之不尽,用之不竭的绿色可再生能源,已经在世界范围内得到了广泛的关注。With the rapid development of society and economy, the demand for energy is increasing day by day, the depletion of fossil energy and the pollution to the ecological environment are seriously threatening the sustainable development of society and economy. Therefore, there is an urgent need to replace it with renewable energy. As an inexhaustible and inexhaustible green renewable energy source, solar energy has received widespread attention worldwide.
太阳能电池原理主要是以半导体材料硅为基体,利用扩散工艺在硅晶体中掺入杂质:当掺入硼、磷等杂质时,硅晶体中就会存在着一个空穴,形成n型半导体;同样,掺入磷原子以后,硅晶体中就会有一个电子,形成p型半导体,p型半导体与n型半导体结合在一起形成pn结,当太阳光照射硅晶体后,pn结中n型半导体的空穴往p型区移动,而p型区中的电子往n型区移动,从而形成从n型区到p型区的电流,在pn结中形成电势差,这就形成了太阳能电池。The principle of solar cells is mainly based on the semiconductor material silicon, and impurities are doped into the silicon crystal by means of a diffusion process: when impurities such as boron and phosphorus are doped, there will be a hole in the silicon crystal to form an n-type semiconductor; , after doping phosphorus atoms, there will be an electron in the silicon crystal to form a p-type semiconductor, and the p-type semiconductor and n-type semiconductor will combine to form a pn junction. When sunlight irradiates the silicon crystal, the n-type semiconductor in the pn junction Holes move to the p-type region, while electrons in the p-type region move to the n-type region, thereby forming a current from the n-type region to the p-type region, forming a potential difference in the pn junction, which forms a solar cell.
太阳能电池片的加工工艺分为硅片检测——表面制绒——扩散制结——去磷硅玻璃——湿法刻蚀——镀减反射膜——丝网印刷——快速烧结等。具体介绍如下:The processing technology of solar cells is divided into silicon wafer detection - surface texturing - diffusion junction - dephosphorous silicon glass - wet etching - anti-reflection coating - screen printing - rapid sintering, etc. The details are as follows:
一、硅片检测1. Wafer detection
硅片是太阳能电池片的载体,硅片质量的好坏直接决定了太阳能电池片转换效率的高低,因此需要对来料硅片进行检测。该工序主要用来对硅片的一些技术参数进行在线测量,这些参数主要包括硅片表面不平整度、少子寿命、电阻率、P/N型和微裂纹等。该组设备分自动上下料、硅片传输、系统整合部分和四个检测模块。其中,光伏硅片检测仪对硅片表面不平整度进行检测,同时检测硅片的尺寸和对角线等外观参数;微裂纹检测模块用来检测硅片的内部微裂纹;另外还有两个检测模组,其中一个在线测试模组主要测试硅片体电阻率和硅片类型,另一个模块用于检测硅片的少子寿命。在进行少子寿命和电阻率检测之前,需要先对硅片的对角线、微裂纹进行检测,并自动剔除破损硅片。硅片检测设备能够自动装片和卸片,并且能够将不合格品放到固定位置,从而提高检测精度和效率。Silicon wafers are the carrier of solar cells. The quality of silicon wafers directly determines the conversion efficiency of solar cells. Therefore, it is necessary to inspect incoming silicon wafers. This process is mainly used for on-line measurement of some technical parameters of silicon wafers, these parameters mainly include silicon wafer surface roughness, minority carrier lifetime, resistivity, P/N type and micro cracks, etc. This group of equipment is divided into automatic loading and unloading, silicon wafer transmission, system integration and four detection modules. Among them, the photovoltaic silicon wafer detector detects the surface roughness of the silicon wafer, and at the same time detects the appearance parameters such as the size and diagonal of the silicon wafer; the micro crack detection module is used to detect the internal micro cracks of the silicon wafer; there are two other Detection modules, one of the online testing modules mainly tests the bulk resistivity and type of silicon wafers, and the other module is used to detect the minority carrier lifetime of silicon wafers. Before the detection of minority carrier lifetime and resistivity, it is necessary to detect the diagonal lines and micro cracks of silicon wafers, and automatically remove damaged silicon wafers. The silicon wafer inspection equipment can automatically load and unload wafers, and can put unqualified products in a fixed position, thereby improving the detection accuracy and efficiency.
二、表面制绒2. Surface cashmere
单晶硅绒面的制备是利用硅的各向异性腐蚀,在每平方厘米硅表面形成几百万个四面方锥体也即金字塔结构。由于入射光在表面的多次反射和折射,增加了光的吸收,提高了电池的短路电流和转换效率。硅的各向异性腐蚀液通常用热的碱性溶液来制备绒面硅,在腐蚀绒面后,进行一般的化学清洗。经过表面准备的硅片都不宜在水中久存,以防沾污,应尽快扩散制结。The preparation of the monocrystalline silicon texture is to use the anisotropic etching of silicon to form millions of tetrahedral pyramids, that is, pyramid structures, on the silicon surface per square centimeter. Due to the multiple reflection and refraction of the incident light on the surface, the absorption of light is increased, and the short-circuit current and conversion efficiency of the battery are improved. The anisotropic etching solution of silicon usually uses hot alkaline solution to prepare textured silicon, and after etching the textured surface, general chemical cleaning is carried out. Surface-prepared silicon wafers should not be stored in water for a long time to prevent contamination, and should be diffused and formed as soon as possible.
三、扩散制结3. Diffusion knot
太阳能电池需要一个大面积的PN结以实现光能到电能的转换,而扩散炉即为制造太阳能电池PN结的专用设备。管式扩散炉主要由石英舟的上下载部分、废气室、炉体部分和气柜部分等四大部分组成。扩散一般用三氯氧磷液态源作为扩散源。把P型硅片放在管式扩散炉的石英容器内,在850---900摄氏度高温下使用氮气将三氯氧磷带入石英容器,通过三氯氧磷和硅片进行反应,得到磷原子。经过一定时间,磷原子从四周进入硅片的表面层,并且通过硅原子之间的空隙向硅片内部渗透扩散,形成了N型半导体和P型半导体的交界面,也就是PN结。这种工艺制出的PN结均匀性好,方块电阻的不均匀性小于百分之十,少子寿命可大于10ms。制造PN结是太阳电池生产最基本也是最关键的工序。因为正是PN结的形成,才使电子和空穴在流动后不再回到原处,这样就形成了电流,用导线将电流引出,就是直流电。Solar cells need a large-area PN junction to convert light energy into electrical energy, and the diffusion furnace is a special equipment for manufacturing PN junctions of solar cells. The tubular diffusion furnace is mainly composed of four parts: the upper and lower parts of the quartz boat, the exhaust gas chamber, the furnace body part and the gas cabinet part. Diffusion generally uses a liquid source of phosphorus oxychloride as a diffusion source. Put the P-type silicon chip in the quartz container of the tubular diffusion furnace, use nitrogen gas to bring phosphorus oxychloride into the quartz container at a high temperature of 850-900 degrees Celsius, and react with the silicon chip to obtain phosphorus atom. After a certain period of time, phosphorus atoms enter the surface layer of the silicon wafer from all sides, and permeate and diffuse into the silicon wafer through the gaps between the silicon atoms, forming the interface between the N-type semiconductor and the P-type semiconductor, that is, the PN junction. The PN junction produced by this process has good uniformity, the non-uniformity of sheet resistance is less than 10%, and the minority carrier lifetime can be greater than 10ms. Manufacture of PN junction is the most basic and critical process in solar cell production. Because it is the formation of the PN junction that the electrons and holes no longer return to the original place after flowing, thus forming a current, and the current is drawn out with a wire, which is direct current.
四、去磷硅玻璃4. Phospho-silicate glass
该工艺用于太阳能电池片生产制造过程中,通过化学腐蚀法也即把硅片放在酸性溶液中浸泡,使其产生化学反应生成可溶性的络和物,以去除扩散制结后在硅片表面形成的一层磷硅玻璃。This process is used in the production and manufacturing process of solar cells. The silicon wafer is soaked in an acidic solution by chemical etching to cause a chemical reaction to form a soluble complex to remove the surface of the silicon wafer after diffusion and junction. A layer of phosphosilicate glass is formed.
五、湿法刻蚀5. Wet etching
由于在扩散过程中,即使采用背靠背扩散,硅片的所有表面包括边缘都将不可避免地扩散上磷。PN结的正面所收集到的光生电子会沿着边缘扩散有磷的区域流到PN结的背面,而造成短路。因此,必须对太阳能电池周边的掺杂硅进行刻蚀,以去除电池边缘的PN结。通常采用湿法刻蚀技术完成这一工艺。Because in the diffusion process, even if the back-to-back diffusion is adopted, phosphorus will inevitably be diffused on all surfaces of the silicon wafer including the edges. The photogenerated electrons collected on the front side of the PN junction will flow to the back side of the PN junction along the area diffused with phosphorus along the edge, causing a short circuit. Therefore, the doped silicon around the solar cell must be etched to remove the PN junction at the edge of the cell. This process is usually accomplished using wet etching techniques.
六、镀减反射膜6. Anti-reflection coating
抛光硅表面的反射率为35%,为了减少表面反射,提高电池的转换效率,需要沉积一层氮化硅减反射膜。工业生产中常采用PECVD设备制备减反射膜。PECVD即等离子增强型化学气相沉积。它的技术原理是利用低温等离子体作能量源,样品置于低气压下辉光放电的阴极上,利用辉光放电使样品升温到预定的温度,然后通入适量的反应气体SiH4和NH3,气体经一系列化学反应和等离子体反应,在样品表面形成固态薄膜即氮化硅薄膜。一般情况下,使用这种等离子增强型化学气相沉积的工艺沉积的薄膜厚度在70nm左右。这样厚度的薄膜具有光学的功能性。利用薄膜干涉原理,可以使光的反射大为减少,电池的短路电流和输出就有很大增加,效率也有相当的提高。The reflectivity of the polished silicon surface is 35%. In order to reduce the surface reflection and improve the conversion efficiency of the cell, a layer of silicon nitride anti-reflection film needs to be deposited. In industrial production, PECVD equipment is often used to prepare anti-reflection coatings. PECVD stands for plasma enhanced chemical vapor deposition. Its technical principle is to use low-temperature plasma as an energy source. The sample is placed on the cathode of glow discharge under low pressure, and the sample is heated to a predetermined temperature by glow discharge, and then an appropriate amount of reaction gas SiH4 and NH3 is introduced. After a series of chemical reactions and plasma reactions, a solid film, that is, a silicon nitride film, is formed on the surface of the sample. Generally, the film thickness deposited by this plasma-enhanced chemical vapor deposition process is about 70nm. A film of this thickness has optical functionality. Using the principle of thin film interference, the reflection of light can be greatly reduced, the short-circuit current and output of the battery will be greatly increased, and the efficiency will also be considerably improved.
七、丝网印刷7. Screen printing
太阳电池经过制绒、扩散及PECVD等工序后,已经制成PN结,可以在光照下产生电流,为了将产生的电流导出,需要在电池表面上制作正、负两个电极。制造电极的工艺很多,而丝网印刷是目前制作太阳电池电极最普遍的一种生产工艺。丝网印刷是采用压印的方式将预定的图形印刷在基板上,该设备由电池背面银铝浆印刷、电池背面铝浆印刷和电池正面银浆印刷三部分组成。其工作原理为:利用丝网图形部分网孔透过浆料,用刮刀在丝网的浆料部位施加一定压力,同时朝丝网另一端移动。油墨在移动中被刮刀从图形部分的网孔中挤压到基片上。由于浆料的粘性作用使印迹固着在一定范围内,印刷中刮板始终与丝网印版和基片呈线性接触,接触线随刮刀移动而移动,从而完成印刷行程。After the process of texturing, diffusion and PECVD, the solar cell has been made into a PN junction, which can generate current under light. In order to export the generated current, it is necessary to make positive and negative electrodes on the surface of the cell. There are many processes for manufacturing electrodes, and screen printing is currently the most common production process for making solar cell electrodes. Screen printing is to print predetermined graphics on the substrate by embossing. The equipment consists of three parts: silver and aluminum paste printing on the back of the battery, aluminum paste printing on the back of the battery and silver paste printing on the front of the battery. Its working principle is: use part of the mesh of the screen pattern to penetrate the slurry, apply a certain pressure on the slurry part of the screen with a scraper, and move towards the other end of the screen at the same time. The ink is squeezed from the mesh of the graphics part to the substrate by the scraper during the movement. Due to the viscosity of the slurry, the imprint is fixed within a certain range, and the squeegee is always in linear contact with the screen printing plate and the substrate during printing, and the contact line moves with the movement of the squeegee, thus completing the printing process.
八、快速烧结Eight, rapid sintering
经过丝网印刷后的硅片,不能直接使用,需经烧结炉快速烧结,将有机树脂粘合剂燃烧掉,剩下几乎纯粹的、由于玻璃质作用而密合在硅片上的银电极。当银电极和晶体硅在温度达到共晶温度时,晶体硅原子以一定的比例融入到熔融的银电极材料中去,从而形成上下电极的欧姆接触,提高电池片的开路电压和填充因子两个关键参数,使其具有电阻特性,以提高电池片的转换效率。The silicon wafer after screen printing cannot be used directly. It needs to be sintered quickly in a sintering furnace to burn off the organic resin binder, leaving almost pure silver electrodes tightly bonded to the silicon wafer due to the effect of glass. When the silver electrode and crystalline silicon reach the eutectic temperature, the crystalline silicon atoms are blended into the molten silver electrode material in a certain proportion, thereby forming an ohmic contact between the upper and lower electrodes, and improving the open circuit voltage and fill factor of the cell. The key parameters make it have resistance characteristics to improve the conversion efficiency of the cell.
烧结炉分为预烧结、烧结、降温冷却三个阶段。预烧结阶段目的是使浆料中的高分子粘合剂分解、燃烧掉,此阶段温度慢慢上升;烧结阶段中烧结体内完成各种物理化学反应,形成电阻膜结构,使其真正具有电阻特性,该阶段温度达到峰值;降温冷却阶段,玻璃冷却硬化并凝固,使电阻膜结构固定地粘附于基片上。The sintering furnace is divided into three stages: pre-sintering, sintering, and cooling. The purpose of the pre-sintering stage is to decompose and burn the polymer binder in the slurry, and the temperature rises slowly at this stage; in the sintering stage, various physical and chemical reactions are completed in the sintered body to form a resistive film structure, so that it truly has resistive characteristics At this stage, the temperature reaches a peak value; in the cooling stage, the glass is cooled, hardened and solidified, so that the resistive film structure is fixedly adhered to the substrate.
上述太阳能电池片的加工工艺在实际使用中存在以下问题:在利用热的碱性溶液来制备绒面硅过程中会产生大量的碱性废液,在去磷硅玻璃过程中会产生大量的酸性废液,在湿法刻蚀过程中会产生大量的氢氟酸废液和硝酸废液,目前,对于这些废液的处理大都是采用酸碱中和处理后直接排放掉,致使太阳能电池片的生产成本较高,不但造成了原料的浪费,同时还会对环境造成污染,不环保。The processing technology of the above-mentioned solar cells has the following problems in actual use: a large amount of alkaline waste liquid will be produced in the process of preparing suede silicon with hot alkaline solution, and a large amount of acid will be produced in the process of removing phosphorus silicon glass. Waste liquid, a large amount of hydrofluoric acid waste liquid and nitric acid waste liquid will be produced in the wet etching process. At present, most of these waste liquids are treated by acid-base neutralization and then discharged directly, resulting in the damage of solar cells. The production cost is higher, which not only causes waste of raw materials, but also pollutes the environment and is not environmentally friendly.
另外,太阳能电池片的寿命周期一般为25年,当转化效率降低到一定程度时,太阳能电池片失效成为不合格太阳能电池片,需要报废更新合格的太阳能电池片,一般情况下,太阳能被视为一种废物产生量最小的能源,在组件的使用过程中不会产生对环境有害的废物,但太阳能电池片报废后产生的固体废弃物也不能够忽视。从2020年之后,我国的太阳能电池的固体废弃物会出现大幅度增长,累计废弃量也逐渐增加,太阳能电池的处理处置和回收利用将会成为一个重要的环保课题。同时,在太阳能电池片的生产过程中由于各种各样的原因会产生大量的不合格太阳能电池片,目前,对于使用过后失效的不合格太阳能电池片以及生产过程中产生的不合格太阳能电池片大都是采用集中销毁的方式,太阳能电池片主要含有的材料为硅、银、铝等,硅、银、铝都是太阳能电池片生产过程中所需要的原料,如果直接将不合格太阳能电池片直接销毁,不但会造成原材料的巨大浪费,同时,销毁后的电池片残渣还会对环境产生污染,不环保。In addition, the life cycle of solar cells is generally 25 years. When the conversion efficiency drops to a certain level, the solar cells fail and become unqualified solar cells, which need to be scrapped and updated. In general, solar energy is regarded as An energy source with minimal waste generation, no waste that is harmful to the environment will be generated during the use of the components, but the solid waste generated after the solar cells are scrapped cannot be ignored. After 2020, the solid waste of solar cells in my country will increase significantly, and the cumulative amount of waste will also gradually increase. The treatment, disposal and recycling of solar cells will become an important environmental protection issue. At the same time, a large number of unqualified solar cells will be produced due to various reasons in the production process of solar cells. Most of them adopt the method of centralized destruction. The main materials contained in solar cells are silicon, silver, aluminum, etc. Silicon, silver, and aluminum are all raw materials needed in the production process of solar cells. If unqualified solar cells are directly Destruction will not only cause a huge waste of raw materials, but at the same time, the battery residue after destruction will also pollute the environment, which is not environmentally friendly.
发明内容Contents of the invention
本发明所要解决的技术问题是提供一种能够降低生产成本且能够减少生产过程中废弃物排放的太阳能电池片加工工艺。The technical problem to be solved by the present invention is to provide a solar cell chip processing technology that can reduce production cost and waste discharge in the production process.
本发明解决其技术问题所采用的技术方案是:该太阳能电池片加工工艺,包括以下步骤:The technical solution adopted by the present invention to solve the technical problems is: the solar cell processing technology comprises the following steps:
A、对需要加工的硅片进行检测,去除不合格硅片;A. Detect silicon wafers that need to be processed and remove unqualified silicon wafers;
B、将经过检测的合格硅片放入碱性溶液中进行表面制绒处理,并将制绒处理后残余的碱性废液收集起来;B. Put the tested qualified silicon wafers into the alkaline solution for surface texture treatment, and collect the residual alkaline waste liquid after the texture treatment;
C、将制绒处理过的硅片放入扩散设备中进行扩散制结处理;C. Put the textured silicon wafer into the diffusion equipment for diffusion and junction processing;
D、将经过扩散制结处理的硅片放入酸性溶液中进行去磷硅玻璃处理,并将去磷硅玻璃处理后残余的酸性废液收集起来;D. Put the silicon wafers processed by diffusion into an acidic solution for dephosphorous silicon glass treatment, and collect the residual acidic waste liquid after the dephosphorous silicon glass treatment;
E、对扩散制结后得到的硅片进行湿法刻蚀处理;先使用氢氟酸对扩散制结后得到的硅片的各个表面进行润洗并将润洗后残余的氢氟酸废液收集起来,将步骤D中得到的去磷硅玻璃太阳能电池片清洗后;然后将硅片放入硝酸溶液中进行刻蚀并将刻蚀后残余的硝酸废液收集起来,接着用碱性溶液对刻蚀后的硅片进行清洗并将清洗后残余的碱性溶液收集起来,最后利用纯水对硅片进行清洗并进行干燥处理;E. Carry out wet etching treatment on the silicon wafers obtained after diffusion bonding; first use hydrofluoric acid to rinse each surface of the silicon wafers obtained after diffusion bonding and rinse the residual hydrofluoric acid waste liquid Collect it, after cleaning the dephosphorous silicon glass solar cells obtained in the step D; then put the silicon wafer into a nitric acid solution for etching and collect the residual nitric acid waste liquid after etching, and then use an alkaline solution to Clean the etched silicon wafer and collect the residual alkaline solution after cleaning, and finally clean the silicon wafer with pure water and dry it;
F、利用PECVD设备在经过湿法刻蚀处理的硅片表面制备氮化硅反射层;F, using PECVD equipment to prepare a silicon nitride reflective layer on the surface of the silicon wafer that has been wet-etched;
G、将镀有减反射膜的硅片采用丝网印刷的方式在硅片的上下表面印制正、负电极;G. Print positive and negative electrodes on the upper and lower surfaces of the silicon wafer coated with the anti-reflection film by screen printing;
H、将经过丝网印刷的硅片放入烧结设备中进行烧结处理后得到太阳能电池片;H. Putting the screen-printed silicon wafer into a sintering device to obtain a solar cell after sintering treatment;
I、将不合格的太阳能电池片放入收集起来的碱性废液中除去太阳能电池片铝背场的部分铝层,再将经过碱性废液浸泡的不合格太阳能电池片放入收集起来的酸性废液中除去太阳能电池片的剩余铝层得到去铝太阳能电池片以及含铝废液,含铝废液通过化学方式转化为氧化铝进而用于制备电子铝浆,所述电子铝浆用于步骤G中丝网印刷的浆料;去铝太阳能电池片经过清洗后,浸泡在收集起来的硝酸废液中将去铝太阳能电池片表面的银浸出,得到去银太阳能电池片以及含银酸液;将去银太阳能电池片放入收集起来的氢氟酸废液中除去去银太阳能电池片表面的氮化硅反射层,得到去氮化硅太阳能电池片清洗后得到纯净的硅片,所述硅片经过步骤A至H后被加工成合格的太阳能电池片;含银酸液中加入铜粉制成银包铜粉用于制备电子浆料,所述电子浆料用于步骤G中丝网印刷的浆料。I. Put the unqualified solar cells into the collected alkaline waste liquid to remove part of the aluminum layer of the aluminum back field of the solar cells, and then put the unqualified solar cells soaked in the alkaline waste liquid into the collected The remaining aluminum layer of the solar cells is removed from the acidic waste liquid to obtain aluminum-free solar cells and aluminum-containing waste liquid. The aluminum-containing waste liquid is chemically converted into alumina and then used to prepare electronic aluminum paste. The electronic aluminum paste is used for The slurry for screen printing in step G; after cleaning the aluminum-removing solar cells, immerse in the collected nitric acid waste liquid to leach the silver on the surface of the aluminum-removing solar cells to obtain the silver-removing solar cells and the silver-containing acid solution put into the collected hydrofluoric acid waste liquid to remove the silver solar cells to remove the silicon nitride reflective layer on the surface of the silver solar cells, and obtain pure silicon chips after cleaning the silicon nitride solar cells. Silicon wafers are processed into qualified solar cells after steps A to H; copper powder is added to silver-containing acid solution to make silver-coated copper powder for preparing electronic paste, which is used for screen in step G Printed paste.
进一步的是,所述含银酸液中加入铜粉制成银包铜粉的具体方法如下所述:在含银酸液中加入铜粉得到固液混合物,所述含银酸液与铜粉的重量比为1.5~3,将固液混合物抽入研磨设备中循环研磨20~50分钟即可得到银包铜粉。Further, the specific method of adding copper powder to the silver-containing acid solution to make silver-coated copper powder is as follows: adding copper powder to the silver-containing acid solution to obtain a solid-liquid mixture, the silver-containing acid solution and copper powder The weight ratio is 1.5-3, and the solid-liquid mixture is pumped into the grinding equipment and circulated for 20-50 minutes to obtain silver-coated copper powder.
进一步的是,所述含银酸液与铜粉的重量比为2。Further, the weight ratio of the silver-containing acid solution to the copper powder is 2.
进一步的是,所述铜粉的粒径为2~3微米。Further, the particle size of the copper powder is 2-3 microns.
进一步的是,所述固液混合物抽入研磨设备中循环研磨的时间为30分钟。Further, the time for the solid-liquid mixture to be sucked into the grinding equipment for circulation and grinding is 30 minutes.
进一步的是,所述含银酸液的温度为20℃。Further, the temperature of the silver-containing acid solution is 20°C.
进一步的是,所述步骤B中收集起来的碱性废液浓度为5%。Further, the concentration of the alkaline waste liquid collected in the step B is 5%.
进一步的是,所述步骤D中收集起来的酸性废液浓度为5%。Further, the concentration of the acid waste liquid collected in the step D is 5%.
进一步的是,所述步骤E中收集起来的氢氟酸废液浓度为0.5%。Further, the concentration of the hydrofluoric acid waste liquid collected in the step E is 0.5%.
进一步的是,所述步骤E中收集起来的硝酸废液浓度为1.5%。Further, the concentration of the nitric acid waste liquid collected in the step E is 1.5%.
本发明的有益效果是:该太阳能电池片加工工艺通过将加工过程中产生的大量碱性废液、酸性废液、氢氟酸废液、硝酸废液收集起来,将报废失效以及生产过程中产生的不合格太阳能电池片放入收集起来的碱性废液中除去太阳能电池片铝背场的部分铝层,再将经过碱性废液浸泡的不合格太阳能电池片放入收集起来的酸性废液中除去太阳能电池片的剩余铝层得到去铝太阳能电池片以及含铝废液,含铝废液通过化学方式转化为氧化铝进而用于制备电子铝浆,所述电子铝浆用于丝网印刷的浆料;去铝太阳能电池片经过清洗后,浸泡在收集起来的硝酸废液中将去铝太阳能电池片表面的银浸出,得到去银太阳能电池片以及含银酸液;将去银太阳能电池片放入收集起来的氢氟酸废液中除去去银太阳能电池片表的氮化硅反射层,得到去氮化硅太阳能电池片清洗后得到纯净的硅片,所述硅片可重新用于太阳能电池片的加工原料,含银酸液中加入铜粉制成银包铜粉用于制备电子浆料,所述电子浆料用于丝网印刷的浆料,该工艺利用太阳能电池片生产过程中产生的各种废液用于回收处理报废失效以及生产过程中产生的不合格太阳能电池片,不但避免了大量废液排放以及不合格太阳能电池片销毁造成的环境污染,同时回收的硅片、银包铜粉、铝浆可直接供应给太阳能电池片生产线,既做到了废液的重复利用,同时还减少了废弃物的产生,更加利用环保生产,可以大大降低太阳能电池片加工过程中原料的使用量,从而降低了太阳能电池片的生产成本。The beneficial effects of the present invention are: the solar cell processing technology collects a large amount of alkaline waste liquid, acid waste liquid, hydrofluoric acid waste liquid, and nitric acid waste liquid generated in the processing process, so as to eliminate scrap failure and waste generated in the production process. Put the unqualified solar cells into the collected alkaline waste liquid to remove part of the aluminum layer of the aluminum back field of the solar cells, and then put the unqualified solar cells soaked in the alkaline waste liquid into the collected acidic waste liquid Remove the remaining aluminum layer of the solar cells in the process to obtain aluminum-free solar cells and aluminum-containing waste liquid. The aluminum-containing waste liquid is chemically converted into alumina and then used to prepare electronic aluminum paste. The electronic aluminum paste is used for screen printing The slurry of the aluminum-removing solar cell is cleaned, soaked in the collected nitric acid waste liquid, and the silver on the surface of the aluminum-removing solar cell is leached to obtain a silver-removing solar cell and silver-containing acid solution; the silver-removing solar cell is Put the sheet into the collected hydrofluoric acid waste liquid to remove the silicon nitride reflective layer on the surface of the silver-removed solar cell sheet, and obtain a pure silicon sheet after cleaning the silicon-nitride solar cell sheet, and the silicon sheet can be reused The raw material for processing solar cells, adding copper powder to the silver-containing acid solution to make silver-coated copper powder is used to prepare electronic paste, which is used for screen printing paste. This process utilizes the production process of solar cells The various waste liquids generated in the process are used to recycle and treat the scrapped and failed solar cells produced during the production process, which not only avoids a large amount of waste liquid discharge and environmental pollution caused by the destruction of unqualified solar cells, but also recycles Silver-coated copper powder and aluminum paste can be directly supplied to the solar cell production line, which not only achieves the reuse of waste liquid, but also reduces the generation of waste, and makes more use of environmentally friendly production, which can greatly reduce the waste of raw materials in the process of solar cell processing. usage, thereby reducing the production cost of solar cells.
具体实施方式detailed description
该太阳能电池片加工工艺,包括以下步骤:The solar cell processing technology includes the following steps:
A、对需要加工的硅片进行检测,去除不合格硅片;A. Detect silicon wafers that need to be processed and remove unqualified silicon wafers;
B、将经过检测的合格硅片放入碱性溶液中进行表面制绒处理,并将制绒处理后残余的碱性废液收集起来;B. Put the tested qualified silicon wafers into the alkaline solution for surface texture treatment, and collect the residual alkaline waste liquid after the texture treatment;
C、将制绒处理过的硅片放入扩散设备中进行扩散制结处理;C. Put the textured silicon wafer into the diffusion equipment for diffusion and junction processing;
D、将经过扩散制结处理的硅片放入酸性溶液中进行去磷硅玻璃处理,并将去磷硅玻璃处理后残余的酸性废液收集起来;D. Put the silicon wafers processed by diffusion into an acidic solution for dephosphorous silicon glass treatment, and collect the residual acidic waste liquid after the dephosphorous silicon glass treatment;
E、对扩散制结后得到的硅片进行湿法刻蚀处理;先使用氢氟酸对扩散制结后得到的硅片的各个表面进行润洗并将润洗后残余的氢氟酸废液收集起来,将步骤D中得到的去磷硅玻璃太阳能电池片清洗后;然后将硅片放入硝酸溶液中进行刻蚀并将刻蚀后残余的硝酸废液收集起来,接着用碱性溶液对刻蚀后的硅片进行清洗并将清洗后残余的碱性溶液收集起来,最后利用纯水对硅片进行清洗并进行干燥处理;E. Carry out wet etching treatment on the silicon wafers obtained after diffusion bonding; first use hydrofluoric acid to rinse each surface of the silicon wafers obtained after diffusion bonding and rinse the residual hydrofluoric acid waste liquid Collect it, after cleaning the dephosphorous silicon glass solar cells obtained in the step D; then put the silicon wafer into a nitric acid solution for etching and collect the residual nitric acid waste liquid after etching, and then use an alkaline solution to Clean the etched silicon wafer and collect the residual alkaline solution after cleaning, and finally clean the silicon wafer with pure water and dry it;
F、利用PECVD设备在经过湿法刻蚀处理的硅片表面制备氮化硅反射层;F, using PECVD equipment to prepare a silicon nitride reflective layer on the surface of the silicon wafer that has been wet-etched;
G、将镀有减反射膜的硅片采用丝网印刷的方式在硅片的上下表面印制正、负电极;G. Print positive and negative electrodes on the upper and lower surfaces of the silicon wafer coated with the anti-reflection film by screen printing;
H、将经过丝网印刷的硅片放入烧结设备中进行烧结处理后得到太阳能电池片;H. Putting the screen-printed silicon wafer into a sintering device to obtain a solar cell after sintering treatment;
I、将不合格的太阳能电池片放入收集起来的碱性废液中除去太阳能电池片铝背场的部分铝层,再将经过碱性废液浸泡的不合格太阳能电池片放入收集起来的酸性废液中除去太阳能电池片的剩余铝层得到去铝太阳能电池片以及含铝废液,含铝废液通过化学方式转化为氧化铝进而用于制备电子铝浆,所述电子铝浆用于步骤G中丝网印刷的浆料;去铝太阳能电池片经过清洗后,浸泡在收集起来的硝酸废液中将去铝太阳能电池片表面的银浸出,得到去银太阳能电池片以及含银酸液;将去银太阳能电池片放入收集起来的氢氟酸废液中除去去银太阳能电池片表面的氮化硅反射层,得到去氮化硅太阳能电池片清洗后得到纯净的硅片,所述硅片经过步骤A至H后被加工成合格的太阳能电池片;含银酸液中加入铜粉制成银包铜粉用于制备电子浆料,所述电子浆料用于步骤G中丝网印刷的浆料。I. Put the unqualified solar cells into the collected alkaline waste liquid to remove part of the aluminum layer of the aluminum back field of the solar cells, and then put the unqualified solar cells soaked in the alkaline waste liquid into the collected The remaining aluminum layer of the solar cells is removed from the acidic waste liquid to obtain aluminum-free solar cells and aluminum-containing waste liquid. The aluminum-containing waste liquid is chemically converted into alumina and then used to prepare electronic aluminum paste. The electronic aluminum paste is used for The slurry for screen printing in step G; after cleaning the aluminum-removing solar cells, immerse in the collected nitric acid waste liquid to leach the silver on the surface of the aluminum-removing solar cells to obtain the silver-removing solar cells and the silver-containing acid solution put into the collected hydrofluoric acid waste liquid to remove the silver solar cells to remove the silicon nitride reflective layer on the surface of the silver solar cells, and obtain pure silicon chips after cleaning the silicon nitride solar cells. Silicon wafers are processed into qualified solar cells after steps A to H; copper powder is added to silver-containing acid solution to make silver-coated copper powder for preparing electronic paste, which is used for screen in step G Printed paste.
该太阳能电池片加工工艺通过将加工过程中产生的大量碱性废液、酸性废液、氢氟酸废液、硝酸废液收集起来,将报废失效以及生产过程中产生的不合格太阳能电池片放入收集起来的碱性废液中除去太阳能电池片铝背场的部分铝层,再将经过碱性废液浸泡的不合格太阳能电池片放入收集起来的酸性废液中除去太阳能电池片的剩余铝层得到去铝太阳能电池片以及含铝废液,含铝废液通过化学方式转化为氧化铝进而用于制备电子铝浆,所述电子铝浆用于丝网印刷的浆料;去铝太阳能电池片经过清洗后,浸泡在收集起来的硝酸废液中将去铝太阳能电池片表面的银浸出,得到去银太阳能电池片以及含银酸液;将去银太阳能电池片放入收集起来的氢氟酸废液中除去去银太阳能电池片表的氮化硅反射层,得到去氮化硅太阳能电池片清洗后得到纯净的硅片,所述硅片可重新用于太阳能电池片的加工原料,含银酸液中加入铜粉制成银包铜粉用于制备电子浆料,所述电子浆料用于丝网印刷的浆料,该工艺利用太阳能电池片生产过程中产生的各种废液用于回收处理报废失效以及生产过程中产生的不合格太阳能电池片,不但避免了大量废液排放以及不合格太阳能电池片销毁造成的环境污染,同时回收的硅片、银包铜粉、铝浆可直接供应给太阳能电池片生产线,既做到了废液的重复利用,同时还减少了废弃物的产生,更加利用环保生产,可以大大降低太阳能电池片加工过程中原料的使用量,从而降低了太阳能电池片的生产成本。The solar cell processing technology collects a large amount of alkaline waste liquid, acid waste liquid, hydrofluoric acid waste liquid, and nitric acid waste liquid generated during the processing process, and puts the scrapped and invalid solar cells produced during the production process into the collected alkaline waste liquid to remove part of the aluminum layer of the aluminum back field of the solar cells, and then put the unqualified solar cells soaked in the alkaline waste liquid into the collected acidic waste liquid to remove the remaining parts of the solar cells The aluminum layer is obtained from aluminum-removed solar cells and aluminum-containing waste liquid, which is chemically converted into alumina and then used to prepare electronic aluminum paste, which is used for screen printing paste; aluminum-removed solar energy After the cells are cleaned, they are soaked in the collected nitric acid waste solution to leach the silver on the surface of the de-aluminum solar cells to obtain the de-silvered solar cells and the silver-containing acid solution; put the de-silvered solar cells into the collected hydrogen Remove the silicon nitride reflective layer on the surface of the desilvered solar cell sheet in the hydrofluoric acid waste liquid to obtain a pure silicon chip after cleaning the silicon nitride solar cell sheet, and the silicon chip can be reused as a processing raw material for the solar cell sheet. Copper powder is added to the silver-containing acid solution to make silver-coated copper powder for the preparation of electronic paste, which is used for screen printing paste. This process utilizes various waste liquids generated during the production of solar cells It is used to recycle and dispose of unqualified solar cells produced in the production process, which not only avoids a large amount of waste liquid discharge and environmental pollution caused by the destruction of unqualified solar cells, but also recycles silicon wafers, silver-coated copper powder, and aluminum paste. It can be directly supplied to the production line of solar cells, which not only achieves the reuse of waste liquid, but also reduces the generation of waste, and makes more use of environmentally friendly production, which can greatly reduce the amount of raw materials used in the processing of solar cells, thereby reducing solar energy. Production cost of cells.
在上述实施方式中,所述含银酸液中加入铜粉制成银包铜粉的具体方法可以采用现有的化学法制备银粉然后包裹在铜粉表面制得,但是这种化学法制备方式制成的银包铜粉含银量较低,银包覆层致密性低,导电性差且生产成本较高、效率较低。本发明提供提供了一种新的银包铜粉制备方法:即在含银酸液中加入铜粉得到固液混合物,所述含银酸液与铜粉的重量比为1.5~3,将固液混合物抽入研磨设备中循环研磨20~50分钟即可得到银包铜粉。该方法只需将铜粉按照一定的重量比加入到含银酸液中,然后将其抽入研磨设备中循环研磨20~50分钟即可,铜粉与含银酸液的固液混合物在研磨过程中发生化学反应,部分铜粉与含银酸液发生置换反应将银离子置换出来生成银粉,生成的银粉沉积在铜粉颗粒的表面,由于固液混合物在研磨过程中同时还受到研磨设备的研磨作用力,在研磨作用力下更多的银粉被沉积在铜粉的表面,而且在研磨作用力下铜粉颗粒表面形成的银层会更加致密,包覆性好,进而银包铜粉的导电性也大大提高,经过试验验证,利用上述方法得到的银包铜粉中银含量可以达到55%以上,大大提高了银包铜粉的综合性能,从而降低银包铜粉的消耗量,降低了生产成本,提高了产品效益。In the above embodiment, the specific method of adding copper powder to the silver-containing acid solution to make silver-coated copper powder can be obtained by using the existing chemical method to prepare silver powder and then wrapping it on the surface of copper powder, but this chemical preparation method The prepared silver-coated copper powder has low silver content, low density of the silver coating layer, poor electrical conductivity, high production cost and low efficiency. The present invention provides a new preparation method of silver-coated copper powder: adding copper powder to silver-containing acid solution to obtain a solid-liquid mixture, the weight ratio of the silver-containing acid solution to copper powder is 1.5-3, and the solid The liquid mixture is pumped into the grinding equipment and circularly ground for 20 to 50 minutes to obtain silver-coated copper powder. This method only needs to add copper powder into the silver-containing acid solution according to a certain weight ratio, and then pump it into the grinding equipment for 20-50 minutes of circular grinding. The solid-liquid mixture of copper powder and silver-containing acid solution is grinding A chemical reaction occurs during the process, and part of the copper powder undergoes a substitution reaction with the silver-containing acid solution to replace the silver ions to form silver powder. The resulting silver powder is deposited on the surface of the copper powder particles. Since the solid-liquid mixture is also subjected to grinding equipment during the grinding process Grinding force, more silver powder is deposited on the surface of the copper powder under the grinding force, and the silver layer formed on the surface of the copper powder particles under the grinding force will be denser and better in coating, and the silver-coated copper powder The conductivity is also greatly improved. It has been verified by experiments that the silver content in the silver-coated copper powder obtained by the above method can reach more than 55%, which greatly improves the overall performance of the silver-coated copper powder, thereby reducing the consumption of silver-coated copper powder and reducing the consumption of silver-coated copper powder. Production costs are improved, and product benefits are improved.
为了保证能够置换出所有的银离子并且在铜粉颗粒表面沉积足够的银粉,所述含银酸液与铜粉的重量比为2。In order to ensure that all the silver ions can be substituted and enough silver powder is deposited on the surface of the copper powder particles, the weight ratio of the silver-containing acid solution to the copper powder is 2.
为了最大限度的提高银包铜粉中银的含量,所述铜粉的粒径为2~3微米,这样铜粉颗粒具有足够大的相对表面积可以沉积更多的银粉。In order to maximize the silver content in the silver-coated copper powder, the particle size of the copper powder is 2-3 microns, so that the copper powder particles have a large enough relative surface area to deposit more silver powder.
为了使置换反应更加充分,同时使更多的银粉能够沉积在铜粉颗粒表面,所述固液混合物抽入研磨设备中循环研磨的时间优选为30分钟。进一步的是,所述含银酸液的温度为20℃。In order to make the replacement reaction more complete and allow more silver powder to be deposited on the surface of the copper powder particles, the time for the solid-liquid mixture to be pumped into the grinding equipment for circular grinding is preferably 30 minutes. Further, the temperature of the silver-containing acid solution is 20°C.
为了在保证制绒效果的同时,进一步降低太阳能电池片的生产成本,所述步骤B中使用的碱性溶液优选为氢氧化钠溶液,由于氢氧化钠溶液价格便宜,且容易获得,可以大大降低其生产成本。为了保证去铝效果,所述步骤B中收集起来的氢氧化钠废液浓度为3~7%。进一步的是,为了保证去铝效果,同时尽量降低成本,所述步骤B中收集起来的氢氧化钠废液浓度为5%。In order to further reduce the production cost of solar cells while ensuring the texturing effect, the alkaline solution used in the step B is preferably sodium hydroxide solution. Because sodium hydroxide solution is cheap and easy to obtain, it can greatly reduce its production cost. In order to ensure the effect of removing aluminum, the concentration of the sodium hydroxide waste liquid collected in the step B is 3-7%. Further, in order to ensure the effect of removing aluminum and reduce the cost as much as possible, the concentration of the sodium hydroxide waste liquid collected in the step B is 5%.
为了保证去磷硅玻璃处理的效果,同时进一步的降低太阳能电池片的生产成本,所述步骤D中使用的酸性溶液为盐酸,盐酸腐蚀性强,可以保证去磷硅玻璃处理的效果,同时,盐酸的价格相对便宜,可以大大降低其生产成本。为了保证去铝效果,同时尽量降低成本,所述步骤D中收集起来的盐酸废液浓度为3~7%。进一步的是,为了保证去铝效果,同时尽量降低成本,所述步骤D中收集起来的盐酸废液浓度为5%。In order to ensure the effect of dephosphorous silicon glass treatment and further reduce the production cost of solar cells, the acidic solution used in the step D is hydrochloric acid, which is highly corrosive and can ensure the effect of dephosphorous silicon glass treatment. At the same time, The price of hydrochloric acid is relatively cheap, which can greatly reduce its production cost. In order to ensure the aluminum removal effect and reduce the cost as much as possible, the concentration of the hydrochloric acid waste liquid collected in the step D is 3-7%. Further, in order to ensure the effect of removing aluminum and reduce the cost as much as possible, the concentration of the hydrochloric acid waste liquid collected in the step D is 5%.
为了保证去银效果,所述步骤E中收集起来的硝酸废液浓度为1~2%。为了使太阳能电池片表面的银全部溶解去除,同时尽量降低成本,所述步骤E中收集起来的硝酸废液浓度优选为1.5%。In order to ensure the desilvering effect, the concentration of the nitric acid waste liquid collected in the step E is 1-2%. In order to dissolve and remove all the silver on the surface of the solar cells and reduce the cost as much as possible, the concentration of the nitric acid waste liquid collected in the step E is preferably 1.5%.
为了保证去氮化硅效果,所述步骤E中收集起来的氢氟酸废液浓度为0.2~0.8%。为了使太阳能电池片表面的氮化硅膜全部去除,同时尽量降低成本,所述步骤E中收集起来的氢氟酸废液浓度为0.5%。In order to ensure the silicon nitride removal effect, the concentration of the hydrofluoric acid waste liquid collected in the step E is 0.2-0.8%. In order to completely remove the silicon nitride film on the surface of the solar cells and reduce the cost as much as possible, the concentration of the hydrofluoric acid waste liquid collected in the step E is 0.5%.
实施例Example
将100kg太阳能电池片用收集起来的100L浓度为5%的氢氧化钠废液处理,反应至中性,除去部分铝层,再将太阳能电池片浸泡于收集起来的300L浓度为5%的盐酸废液中,直至铝层完全去除;然后将去铝太阳能电池片投入收集起来的100L浓度为1.5%的硝酸废液,使银溶解完全得到含银酸液;把去银太阳能电池片投入到20L浓度为0.5%的氢氟酸废液中除去氮化硅,得到纯净的硅片80kg,回收率约为90%;最后将含铝溶液中的铝转化为氧化铝,得到约20kg氧化铝回收率约为93%,将含银酸液的温度控制在20℃,并加入粒径为2-3微米的片状铜粉混合后形成固液混合物,加入的片状铜粉的质量为含银酸液质量的一半,将混合后形成的固液混合物抽入砂磨机高速循环研磨30min,得到含银量约55%银色银包铜粉,D50=1-2微米,导电率为1.5×10-5Ω·cm。Treat 100kg of solar cells with 100L of collected 5% sodium hydroxide waste solution, react until neutral, remove part of the aluminum layer, and then soak the solar cells in 300L of collected 5% hydrochloric acid waste solution until the aluminum layer is completely removed; then put the collected 100L nitric acid waste solution with a concentration of 1.5% into the aluminum-removed solar cells to completely dissolve the silver to obtain a silver-containing acid solution; put the silver-removed solar cells into a concentration of 20L Silicon nitride is removed in 0.5% hydrofluoric acid waste liquid to obtain 80kg of pure silicon chips with a recovery rate of about 90%; finally, the aluminum in the aluminum-containing solution is converted into alumina to obtain about 20kg of alumina with a recovery rate of about to 93%, the temperature of the silver-containing acid solution is controlled at 20°C, and flake copper powder with a particle size of 2-3 microns is added to form a solid-liquid mixture after mixing. The quality of the added flake copper powder is Half of the mass, the solid-liquid mixture formed after mixing is pumped into a sand mill for high-speed circular grinding for 30 minutes to obtain silver-colored silver-coated copper powder with a silver content of about 55%, D50=1-2 microns, and a conductivity of 1.5×10-5Ω cm.
Claims (10)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510698101.5A CN105355710B (en) | 2015-10-23 | 2015-10-23 | A kind of solar cell machining process |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510698101.5A CN105355710B (en) | 2015-10-23 | 2015-10-23 | A kind of solar cell machining process |
Publications (2)
Publication Number | Publication Date |
---|---|
CN105355710A CN105355710A (en) | 2016-02-24 |
CN105355710B true CN105355710B (en) | 2017-04-05 |
Family
ID=55331639
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201510698101.5A Active CN105355710B (en) | 2015-10-23 | 2015-10-23 | A kind of solar cell machining process |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN105355710B (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106098860A (en) * | 2016-08-27 | 2016-11-09 | 浙江中晶新能源有限公司 | A kind of production technology of solar battery sheet |
CN107321766A (en) * | 2017-08-14 | 2017-11-07 | 通威太阳能(安徽)有限公司 | A kind of refuse battery piece recovery process |
CN108054244A (en) * | 2017-12-19 | 2018-05-18 | 温州海旭科技有限公司 | A kind of manufacturing process of solar battery sheet |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102956749A (en) * | 2012-11-20 | 2013-03-06 | 泰通(泰州)工业有限公司 | Manufacturing Preparation process of solar cell electrode |
CN103779441A (en) * | 2013-11-13 | 2014-05-07 | 河南科技学院 | Cleaning recovery treatment process of solar cell sheet |
CN103606595B (en) * | 2013-11-21 | 2016-04-06 | 英利集团有限公司 | The recycling of the rear defective Monocrystalline silicon cell piece of sintering and grid line recovery method thereof |
CN104988317A (en) * | 2015-06-23 | 2015-10-21 | 中国电器科学研究院有限公司 | Method for extracting metallic silver from waste circuit board |
-
2015
- 2015-10-23 CN CN201510698101.5A patent/CN105355710B/en active Active
Also Published As
Publication number | Publication date |
---|---|
CN105355710A (en) | 2016-02-24 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN105206711B (en) | A kind of solaode slice processing method | |
Neuhaus et al. | Industrial silicon wafer solar cells | |
Lee et al. | Photovoltaic performance of c-Si wafer reclaimed from end-of-life solar cell using various mixing ratios of HF and HNO3 | |
CN105185873B (en) | Solar battery sheet production technology | |
CN102181935B (en) | Method and corrosive liquid for making texture surface of monocrystalline silicon | |
CN102629644B (en) | Reworking technology of finished crystalline silicon solar cell | |
CN105355541A (en) | Solar cell recycling method | |
CN105355710B (en) | A kind of solar cell machining process | |
CN101582467A (en) | Method for grooving and grid burying of crystalline silicon solar cell | |
CN103647000A (en) | Surface texturing technology for crystalline silicon solar cell | |
CN102157585B (en) | Method for manufacturing uniform shallow emitter solar cell | |
Lorenz et al. | Flexographic printing–high throughput technology for fine line seed layer printing on silicon solar cells | |
CN103606595A (en) | Reutilization method and grating line recovery method of defective monocrystalline silicon battery sheet after sintering | |
CN108172642A (en) | A single crystal gallium-doped double-sided solar cell and its preparation method | |
CN108133976A (en) | A kind of monocrystalline mixes gallium back of the body passivating solar battery and preparation method thereof | |
CN104037262A (en) | Manufacturing process of ultrathin crystal silicon flexible solar cell | |
CN105304758B (en) | A method of it reduces and leaks electricity at back contacts photovoltaic cell perforation electrode | |
CN105826408B (en) | Local back surface field N-type solar cell and preparation method and component, system | |
CN102903786A (en) | Novel ultra-shallow junction crystalline silicon solar cell | |
CN104269468B (en) | A kind of preparation method of selective emitter solar cell | |
Teppe et al. | Progress in the industrial evaluation of the mc-Si PERCT technology based on boron diffusion | |
CN103094409B (en) | A kind of edge etching process being applied to polysilicon solar cell | |
CN106816496A (en) | The manufacture method of photovoltaic battery panel | |
CN206697494U (en) | A kind of solar panel | |
CN102623568B (en) | Removing method of diffusing dead layers of crystalline silicon solar cell |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |