CN101299446A - Selenide forerunner thin film and method for producing film cell through rapid selenium vulcanizing thermal treatment - Google Patents
Selenide forerunner thin film and method for producing film cell through rapid selenium vulcanizing thermal treatment Download PDFInfo
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- CN101299446A CN101299446A CNA2008100533566A CN200810053356A CN101299446A CN 101299446 A CN101299446 A CN 101299446A CN A2008100533566 A CNA2008100533566 A CN A2008100533566A CN 200810053356 A CN200810053356 A CN 200810053356A CN 101299446 A CN101299446 A CN 101299446A
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- selenium
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Images
Classifications
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- 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
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- Photovoltaic Devices (AREA)
Abstract
Description
技术领域 technical field
本发明涉及化合物半导体薄膜器件的制备,更具体地说,涉及非真空低成本法制备铜铟镓硒硫[Cu(In0.7,Ga0.3)Se2-xSX简写为CIGS]薄膜太阳电池的硒化物前驱薄膜,并对其进行真空快速硒硫化热处理后,直接、连续化地制备出薄膜太阳电池或光伏集成组件的方法。The present invention relates to the preparation of compound semiconductor thin film devices, more specifically, to the preparation of copper indium gallium selenide sulfur [Cu(In 0.7 , Ga 0.3 )Se 2-x S X abbreviated as CIGS] thin film solar cells by a non-vacuum low-cost method A method for preparing a thin-film solar cell or a photovoltaic integrated module directly and continuously after a selenide precursor thin film is subjected to vacuum rapid selenium sulfidation heat treatment.
背景技术 Background technique
太阳能电池发电方式是可再生的能源技术,产生电能的过程中对环境影响最小。太阳能发电技术要取得商业上的成功,必须使太阳能电池具有更高的效率、更低的成本、更好的耐候性,并且不增加其它的环境问题。传统晶体硅太阳电池技术的发展得益于电子硅半导体材料的不断技术进步,制造它需要单晶硅上游材料中的多晶硅材料,晶体硅太阳能电池的经济附加值并不高,是一种靠长期累积获取收益的产品,大规模地运用分流了硅半导体电了行业的材料来源,势必进一步加剧全球性资源性的短缺,促使其价格更加地昂贵;从另一方面来说,今天的晶体硅太阳电池产品与技术还占据着统治地位,它基本能满足上述太阳电池技术提及的多项要求,但却不能以低成本方式生产太阳电池,其在生产过程中硅材料的浪费高达70%,并且还需要消耗大量的一次能源,势必对环境造成不利的影响;相对而言,生产晶体硅太阳电池的能源消耗需要三年多的发电才能回收,即使最便宜的晶体硅太阳能电池每瓦特能量输出的制造成本也要3美元,现阶段制约太阳电池发展的最大瓶颈是过高的原材料成本和生产成本。Solar cell power generation is a renewable energy technology that has the least impact on the environment in the process of generating electricity. For solar power technology to be commercially successful, solar cells must be more efficient, lower cost, better weather-resistant, and not add to other environmental concerns. The development of traditional crystalline silicon solar cell technology benefits from the continuous technological progress of electronic silicon semiconductor materials. To manufacture it requires polycrystalline silicon materials in the upstream materials of monocrystalline silicon. The economic added value of crystalline silicon solar cells is not high. It is a long-term The large-scale use of products that have accumulated income has diverted the material sources of the silicon semiconductor industry, which will inevitably further aggravate the global resource shortage and make its price more expensive; on the other hand, today's crystalline silicon solar Battery products and technologies still occupy a dominant position. It can basically meet the multiple requirements mentioned in the above-mentioned solar cell technology, but it cannot produce solar cells at low cost. The waste of silicon materials in the production process is as high as 70%, and It also needs to consume a large amount of primary energy, which will inevitably have an adverse impact on the environment; relatively speaking, the energy consumption of producing crystalline silicon solar cells requires more than three years of power generation to recover, even if the cheapest crystalline silicon solar cells output 1 watt of energy output The manufacturing cost is also 3 US dollars. The biggest bottleneck restricting the development of solar cells at this stage is the high raw material cost and production cost.
基于薄膜技术的太阳电池是个正处于发展阶段的技术,它们提供了一种太阳电池成本大幅度降低的技术可能性。制造硅薄膜太阳电池的原材料与电子单晶硅半导体器件制造过程所用原材料是一致的,其来源是多晶硅提纯过程中的中间气态产品,制造硅薄膜太阳电池过程的材料利用率较高;但是,硅薄膜太阳电池的光电转换效率较低和耐久性差(使用过程中的性能衰退),虽然通过技术进步缓解了这种缺陷,却无法彻底根治。基于化合物半导体Cu(In,Ga)Se2薄膜太阳电池是一个非常有前途的太阳电池技术,CIGS薄膜的带隙宽度可根据Ga含量在1.04~1.68eV的范围内变化;对可见光的吸收系数高达105/cm,1-2μm厚的薄膜就可以吸收绝大部分阳光,适合于作为廉价太阳电池的吸收层。CIGS薄膜太阳电池具有无衰退、抗辐射、寿命长等特点,最高效率已达19.9%,接近多晶硅太阳电池20.3%的最高光电转换效率,是所有薄膜太阳电池中最高的。并且它可以沉积在大面积廉价衬底-玻璃、不锈钢、钛箔或PI塑料薄膜等基底材料上,与晶体硅太阳电池相比,减少了生产工序,因而在降低成本方面具有独特的优势,如果真空共蒸发和溅射金属预置层技术路线达到生产设计要求,其成本只有晶体硅电池的1/3~1/2。经过二十多年的研究开发,CIGS薄膜太阳电池已基本实现了产业化。Solar cells based on thin-film technology are a technology that is in the development stage, and they offer a technical possibility for a substantial reduction in the cost of solar cells. The raw materials for manufacturing silicon thin-film solar cells are the same as those used in the manufacturing process of electronic monocrystalline silicon semiconductor devices. Thin-film solar cells have low photoelectric conversion efficiency and poor durability (performance degradation during use). Although this defect has been alleviated through technological progress, it cannot be completely cured. Based on the compound semiconductor Cu(In,Ga)Se 2 thin film solar cell is a very promising solar cell technology, the bandgap width of CIGS thin film can be changed in the range of 1.04-1.68eV according to the Ga content; the absorption coefficient of visible light is as high as 10 5 /cm, 1-2μm thick film can absorb most of the sunlight, which is suitable as the absorbing layer of cheap solar cells. CIGS thin-film solar cells have the characteristics of no fading, anti-radiation, and long life. The highest efficiency has reached 19.9%, which is close to the highest photoelectric conversion efficiency of polycrystalline silicon solar cells of 20.3%, and is the highest among all thin-film solar cells. And it can be deposited on a large area of cheap substrates - glass, stainless steel, titanium foil or PI plastic film and other base materials. Compared with crystalline silicon solar cells, it reduces the production process, so it has unique advantages in reducing costs. If The technical route of vacuum co-evaporation and sputtering metal pre-layer meets the production design requirements, and its cost is only 1/3 to 1/2 of that of crystalline silicon cells. After more than 20 years of research and development, CIGS thin film solar cells have basically achieved industrialization.
虽然CIGS薄膜太阳电池具有低成本的潜力,但是,二十多年高效CIGS薄膜电池开发技术均是以真空设备为基础,真空溅射金属预置层后硒化技术仅是为了减少共蒸发的控制难度,适合于大面积制备薄膜电池的均匀性和易于工业化连续地生产而开发成功的,其原材料相对利用率更低、所需真空制造设备更多。由于蒸发法和溅射后硒化法都是以真空设备为主,设备庞大、造价昂贵,建立薄膜电池生产线的前期投入大。而且,沉积薄膜的原材料利用率仅为30~60%,其薄膜制备与靶材成本部分就占总成本的45.3%。抵消了CIGS薄膜太阳电池可制备成薄膜的低价优势,也是目前CIGS薄膜电池成本没有达到人们预期那么低的主要原因。Although CIGS thin-film solar cells have low-cost potential, the development technology of high-efficiency CIGS thin-film solar cells for more than 20 years is based on vacuum equipment, and the selenization technology after vacuum sputtering metal pre-layer is only to reduce the control of co-evaporation Difficulty, suitable for the uniformity of large-scale preparation of thin-film batteries and the ease of industrialized continuous production and successful development, the relative utilization rate of raw materials is lower, and more vacuum manufacturing equipment is required. Since the evaporation method and the selenization method after sputtering are mainly based on vacuum equipment, the equipment is huge and expensive, and the initial investment in establishing a thin film battery production line is large. Moreover, the utilization rate of raw materials for depositing thin films is only 30-60%, and the cost of thin film preparation and target materials accounts for 45.3% of the total cost. Offset CIGS thin-film solar cells can be prepared as a low-cost thin film advantage, but also the current cost of CIGS thin-film solar cells is not as low as people expected the main reason.
低成本法制备CIGS薄膜电池的主要目的是大量减少使用昂贵的真空设备、降低制造过程中一次能源消耗和提高原材料的利用率。目前,非真空法制备CIGS薄膜主要有两种途径,一种是先将Cu-In-Ga-Se原料制备成纳米涂料,再用湿法涂覆在合适的衬底上干燥成膜,然后进行热处理;另一种是水浴电沉积制备CIGS薄膜后再热处理。这两种技术途径有着共同的特点,都是从水溶性原料中得到CIGS薄膜的预置层,然后进行加热后处理;共同的优点是:(1)设备简单、投资小、成本低;(2)、原材料利用率高达95%以上;(3)可以大面积、连续、低温法沉积薄膜前驱物。这种方法目前已经取得较大的突破,国外已经有多个公司开始产业化进程。但是,这种方法还存在薄膜质量多孔、夹杂,加热硒化处理后出现裂纹等现象。The main purpose of low-cost preparation of CIGS thin-film batteries is to reduce the use of expensive vacuum equipment, reduce primary energy consumption in the manufacturing process and improve the utilization of raw materials. At present, there are two main ways to prepare CIGS thin films by non-vacuum method. One is to prepare Cu-In-Ga-Se raw materials into nano-coatings, and then wet-coat them on a suitable substrate to dry to form a film, and then carry out Heat treatment; the other is heat treatment after preparing CIGS thin film by water bath electrodeposition. These two technical approaches have common characteristics, all are to obtain the preset layer of CIGS film from water-soluble raw materials, and then carry out post-heating treatment; common advantages are: (1) simple equipment, small investment, low cost; (2) ), the utilization rate of raw materials is as high as 95% or more; (3) the thin film precursor can be deposited in a large area, continuous and low temperature method. This method has already made great breakthroughs, and many foreign companies have begun the process of industrialization. However, this method also has phenomena such as porous film quality, inclusions, and cracks after heating and selenization treatment.
涂覆法是将Cu-In-Ga-Se以一定的比例混合制成不同组成的纳米粒子涂料,再采用不同的涂覆技术在衬底上干燥形成前驱薄膜。美国ISET公司的V.K.Kapur等人将最终薄膜所需Cu、In、Ga元素按CuIn0.7Ga0.3Se2化学式计量的Cu/(In+Ga)比例混合物溶解在酸性溶液中,加入碱溶液中和反应而形成金属氢氧化物,再用水冲洗除去副产物,干燥制成金属氧化物纳米粒子,与水和分散剂混合形成纳米涂料,用印刷滚涂等方式在Mo/玻璃衬底上涂覆成膜与干燥,然后在500~550℃的H2和N2混合气氛中进行还原反应,得到致密的Cu-In-Ga合金薄膜,再在420~450℃的H2Se和N2混合气氛中硒化形成CIGS薄膜。涂覆的湿膜厚度约12μm,干燥后形成的薄膜结构疏松多孔,厚度约6μm,经氢气还原与硒化处理后约2μm厚。用这种方法制备的CIGS薄膜电池玻璃衬底上的最高效率为13.6%(0.08cm2),柔性衬底Mo箔上的为13.0%[1],面积为65cm2的电池组件效率为8%[2,3]。其美国发明专利为US5985691。The coating method is to mix Cu-In-Ga-Se in a certain proportion to form nanoparticle coatings with different compositions, and then use different coating techniques to dry on the substrate to form a precursor film. VKKapur et al. of ISET Company in the United States dissolved the Cu, In, and Ga elements required for the final film according to the Cu/(In+Ga) ratio mixture of the CuIn 0.7 Ga 0.3 Se 2 stoichiometric formula in an acidic solution, and added an alkaline solution to neutralize the reaction. Form metal hydroxide, then rinse with water to remove by-products, dry to make metal oxide nanoparticles, mix with water and dispersant to form nano-coatings, and coat Mo/glass substrates with film-forming and Drying, and then reducing reaction in a mixed atmosphere of H2 and N2 at 500-550°C to obtain a dense Cu-In-Ga alloy film, and then selenized in a mixed atmosphere of H2Se and N2 at 420-450°C A CIGS thin film is formed. The thickness of the coated wet film is about 12 μm, and the film structure formed after drying is loose and porous, with a thickness of about 6 μm, and a thickness of about 2 μm after hydrogen reduction and selenization treatment. The highest efficiency of the CIGS thin film battery prepared by this method is 13.6% (0.08cm 2 ) on the glass substrate, 13.0% on the flexible substrate Mo foil [1] , and the efficiency of the battery module with an area of 65cm 2 is 8% [2, 3] . Its US invention patent is US5985691.
美国Nanosolar公司成立于2002年,2003年决定主要研究开发非真空法制备CIGS薄膜技术。他们利用不同的化学反应,采用有机金属化合物热分解法、喷雾共沉淀法、溶胶-凝胶法等方法制备出各种非氧化物的纳米粒子,如CuInSe2、CuGaSe、CuSe、In2Se3,通过控制反应过程的条件来控制纳米粒子的大小。以CuSe和In2Se3为核包裹纯硒后制成硒化物纳米粒子,并与水溶性溶剂调配成液相涂料,将其湿法涂覆(丝网印刷或滚涂印刷法)在已溅射沉积Mo薄膜的铝箔上干燥成膜,加热挥发掉有机溶剂后,前驱硒化物薄膜经过快速热处理(RTP)制备出PV(光伏)级薄膜材料,它利用了前驱硒化物薄膜中纯Se的180℃低温熔点和CuxSe的523℃中温熔点的液相特征,进行了多孔疏松硒化物前驱薄膜快速加热的致密化、二元硒化物合成反应和晶体的液相辅助生长等物理化学过程,制备出柱状致密的大晶粒CIS薄膜太阳电池吸收层,玻璃衬底的单体(0.470cm2)CIGS薄膜太阳电池的最高效率达到14.5%[4]。Nanosolar公司申请有美国专利50多项,与上述相关的专利为US20070092648(技术说明:CuSe代表富硒纳米微晶颗粒,CuxSe代表薄膜内各类硒化铜成份的总称,Cu2Se代表薄膜内真实的化学成份)。American Nanosolar company was established in 2002, and in 2003 decided to mainly research and develop CIGS thin film technology by non-vacuum method. They used different chemical reactions to prepare various non-oxide nanoparticles, such as CuInSe 2 , CuGaSe, CuSe, In 2 Se 3 , by controlling the conditions of the reaction process to control the size of the nanoparticles. CuSe and In 2 Se 3 were used as the core to wrap pure selenium to make selenide nanoparticles, and formulated with water-soluble solvent to form a liquid coating, which was wet-coated (screen printing or roll printing method) on the sputtered surface. The film is dried on the aluminum foil deposited by spraying Mo film, and the organic solvent is volatilized by heating. The precursor selenide film is subjected to rapid thermal treatment (RTP) to prepare a PV (photovoltaic) grade film material, which utilizes the 180% of pure Se in the precursor selenide film. ℃ low-temperature melting point and 523 ℃ medium-temperature melting point of Cu x Se, the liquid phase characteristics, carried out the physical and chemical processes of rapid heating densification of porous loose selenide precursor film, binary selenide synthesis reaction and liquid phase assisted growth of crystal, etc., prepared A columnar dense large-grain CIS thin-film solar cell absorber layer is produced, and the highest efficiency of a single (0.470cm 2 ) CIGS thin-film solar cell on a glass substrate reaches 14.5% [4] . Nanosolar has applied for more than 50 U.S. patents, and the patent related to the above is US20070092648 (technical description: CuSe represents selenium-rich nanocrystalline particles, CuxSe represents the general name of various copper selenide components in the film, and Cu 2 Se represents the real chemical composition).
在日本,T.Wada等人采用球磨法将单质Cu、In、Ga和Se的粉末混合物进行研磨,研磨过程中它们反应生成纳米Cu(In,Ga)Se2粉末,再与有机溶剂混合形成纳米颗粒涂料,被涂覆在Mo/玻璃衬底薄膜上,通过加热将有机溶剂除去;在下常大气压的惰性N2气体环境中加热处理,使玻璃衬底上该硒化物薄膜加热到550~570℃,多孔预置层硒化物薄膜烧结成致密的多晶薄膜,制备的电池转换效率为2.7%[5,6]。In Japan, T.Wada et al. used ball milling method to grind the powder mixture of elemental Cu, In, Ga and Se. During the grinding process, they reacted to form nano Cu(In, Ga)Se 2 powder, which was then mixed with organic solvent to form nano Particle coating, which is coated on Mo/glass substrate film, and the organic solvent is removed by heating; heat treatment in an inert N2 gas environment under normal atmospheric pressure, so that the selenide film on the glass substrate is heated to 550-570 °C , the porous pre-layer selenide film was sintered into a dense polycrystalline film, and the conversion efficiency of the prepared battery was 2.7% [5,6] .
韩国国家能源研究所的K.Yoon[7]所领导的研究小组将CuI、InI3和GaI3溶解在嘧啶中,Na2Se溶解在甲醇中,在低温氮气保护下混合反应生成约15nm的CIGS纳米粒子。用有机溶剂调和成涂料,涂覆在基片的Mo衬底上,在快速热处理炉中进行二段式加热硒化,制备的薄膜电池效率为1.11%。The research team led by K. Yoon [7] of the National Energy Research Institute of South Korea dissolved CuI, InI 3 and GaI 3 in pyrimidine, Na 2 Se in methanol, and mixed reaction under the protection of low-temperature nitrogen to form CIGS of about 15nm Nanoparticles. An organic solvent is used to make a coating, and the coating is coated on the Mo substrate of the substrate, and two-stage heating and selenization are carried out in a rapid heat treatment furnace, and the efficiency of the prepared thin film battery is 1.11%.
电沉积法制备CIGS前驱硒化物薄膜的工艺是在酸性水溶液中以Mo衬底作为阴极,直接电沉积各类CIGS硒化物前驱薄膜。美国国家可再生能源实验室(NREL)的Bhattacharya等人在氯化物溶液体系中,用一步法直接电沉积CIGS各元素而得到了富Cu硒化物前驱薄膜,在真空硒气氛环境下对它进行热处理,同时蒸发沉积约占薄膜总量中50%的In、Ga来调节薄膜化学成份的配比,使最终薄膜成份符合制备半导体器件的要求,制备的薄膜电池效率达到15.4%[8]。但是,这种电沉积溶液不太稳定,放置一天便有大量溶质沉淀析出;另外,电沉积该硒化物前驱薄膜中Ga的含量很低,Ga/(In+Ga)之比仅0.1。通过加入氨基磺酸和苯二甲酸氢钾pH缓冲溶液后,有效改善了电沉积溶液的稳定性,其在工艺实用性方面获得了突破[9],薄膜中Ga/(In+Ga)之比可达到0.3~0.7,硒化物前驱薄膜在真空硒气氛环境下热处理,同时蒸发沉积约占薄膜总量5~10%的In、Ga来调节薄膜成份接近化学计量比,制备薄膜电池的效率达到9.4%。如果电沉积CIGS前驱硒化物薄膜仅在H2Se气氛中进行热处理,然后用KCN溶液溶解掉薄膜中富Cu相的Cu2Se,不需要真空补充蒸发In、Ga与Se成份的薄膜太阳电池效率达到6.2%[10]。Bhattacharya等人在美国申请与获得多项发明专利,其中,在中国获得的发明专利号为:96199008.2;Bhattacharya现在美国Solopower公司专门从事电沉积硒化物前驱薄膜与热处理制备CIGS薄膜电池光伏组件生产技术的研究开发,Solopower公司获得风险投资3000万美元,建立了20MW的电沉积CIGS薄膜电池中试生产线。The process of preparing CIGS precursor selenide film by electrodeposition method is to directly electrodeposit various CIGS selenide precursor films in acidic aqueous solution with Mo substrate as cathode. Bhattacharya et al. of the National Renewable Energy Laboratory (NREL) obtained a Cu-rich selenide precursor film by direct electrodeposition of CIGS elements in a chloride solution system, and heat-treated it in a vacuum selenium atmosphere. , while evaporating and depositing In and Ga, which account for about 50% of the total film, to adjust the chemical composition ratio of the film, so that the final film composition meets the requirements for preparing semiconductor devices, and the efficiency of the prepared thin film battery reaches 15.4% [8] . However, this electrodeposition solution is not stable, and a large amount of solute precipitates out after one day; in addition, the Ga content in the electrodeposited selenide precursor film is very low, and the ratio of Ga/(In+Ga) is only 0.1. After adding sulfamic acid and potassium hydrogen phthalate pH buffer solution, the stability of the electrodeposition solution was effectively improved, and a breakthrough was made in terms of process practicability [9] , the ratio of Ga/(In+Ga) in the film It can reach 0.3-0.7. The selenide precursor film is heat-treated in a vacuum selenium atmosphere, and at the same time, evaporates and deposits In and Ga, which account for 5-10% of the total film, to adjust the film composition to be close to the stoichiometric ratio. The efficiency of preparing a thin-film battery reaches 9.4 %. If the electro-deposited CIGS precursor selenide film is only heat-treated in H 2 Se atmosphere, and then KCN solution is used to dissolve Cu 2 Se in the Cu-rich phase of the film, the efficiency of the thin-film solar cell that does not need vacuum supplementary evaporation of In, Ga and Se components reaches 6.2% [10] . Bhattacharya and others have applied for and obtained a number of invention patents in the United States. Among them, the invention patent number obtained in China is: 96199008.2; Bhattacharya is now a Solopower company in the United States specializing in the production technology of electrodeposition selenide precursor film and heat treatment to prepare CIGS thin film cell photovoltaic modules. For research and development, Solopower received a venture capital of 30 million US dollars and established a 20MW pilot production line for electrodeposited CIGS thin film batteries.
IRDEP(Energy Development and Research Institute光伏能源开发研究所)作为法国CNRS(国家科学研究中心)、法国电力公司(EDF)和法国巴黎国立高等化学大学的联合研究单位(UnitéMixte de Recherche)成立于2005年。IRDEP-光伏能源开发研究所采取的主要工艺路线是电沉积CuInSe2再对其表面进行硫化,形成CuIn(Se,S)2的结构;近期目标为:(1)小面积电池的效率大于12%;(2)30×30cm2组件效率大于8%。主要措施是在CIS中加入Ga或S[11,12]。他们采用硫酸盐体系进行电沉积富Cu相CuInSe2薄膜的研究,再在S气氛中进行硫化热处理,获得大晶粒致密的柱状结构薄膜材料,然后用KCN溶液去除富Cu相。制备的电池最好效率为11.5%,衬底面积为30×30cm2时,电沉积的预置层的质量均匀,电池效率可达7%以上。存在问题是:沉积的薄膜一般是富Cu薄膜,经过热处理后需要在KCN溶液中刻蚀或溶解掉薄膜中富Cu相的Cu2Se,它会影响薄膜表面的结构和电池pn结的质量。另外,热处理过程中Mo与Se反应易形成较厚的MoSe[13]。IRDEP( The Energy Development and Research Institute (Photovoltaic Energy Development Institute) was established in 2005 as a joint research unit (UnitéMixte de Recherche) of CNRS (National Center for Scientific Research), Electricity of France (EDF) and National Higher Chemistry University of Paris, France. The main process route adopted by IRDEP-Photovoltaic Energy Development Research Institute is to electrodeposit CuInSe 2 and then sulfide its surface to form a CuIn(Se,S) 2 structure; the short-term goal is: (1) The efficiency of small-area cells is greater than 12% ; (2) 30×30cm 2 module efficiency is greater than 8%. The main measure is to add Ga or S to the CIS [11, 12] . They used the sulfate system for electrodeposition of Cu-rich phase CuInSe 2 thin film research, and then carried out sulfidation heat treatment in S atmosphere to obtain a large-grain dense columnar structure thin film material, and then removed the Cu-rich phase with KCN solution. The best efficiency of the prepared battery is 11.5%. When the substrate area is 30×30cm 2 , the quality of the electrodeposited preset layer is uniform, and the battery efficiency can reach more than 7%. The problem is that the deposited film is generally Cu-rich film. After heat treatment, Cu 2 Se in the Cu-rich phase in the film needs to be etched or dissolved in KCN solution, which will affect the structure of the film surface and the quality of the pn junction of the battery. In addition, the reaction between Mo and Se during heat treatment tends to form thicker MoSe [13] .
德国的A.Kampmann等人采用硫酸盐体系,对电化学沉积进行了长期研究,并在CISSolartechnik公司建立了卷带式连续电沉积中试线。在带宽为100mm金属薄卷带上进行CIGS薄膜的制备,工艺过程:Mo、Cu、钢、不锈钢薄作为薄膜电池的衬底,沉积阻挡层、溅射沉积Mo层,按顺序电沉积Cu-In-Ga后再蒸发沉积Se,最后Se层上蒸发沉积Na的化合物,然后进行快速升温热处理,形成CIGS薄膜,其工艺过程与真空溅射后硒化法的技术相似。不锈钢薄带上CIGS电池效率为10.4%(面积为1.0cm2),面积为13.3cm2的效率为6.6%[14]。Germany's A. Kampmann et al. used the sulfate system to conduct long-term research on electrochemical deposition, and established a roll-to-roll continuous electrodeposition pilot line at CISSolartechnik. The CIGS thin film is prepared on a thin metal tape with a bandwidth of 100mm. The process: Mo, Cu, steel, and stainless steel are used as the substrate of the thin film battery, and the barrier layer is deposited, the Mo layer is deposited by sputtering, and Cu-In is electrodeposited in sequence. After -Ga, Se is evaporated and deposited, and finally Na compounds are evaporated and deposited on the Se layer, and then a rapid heating and heat treatment is performed to form a CIGS film. The process is similar to the technology of selenization after vacuum sputtering. The efficiency of CIGS cells on thin stainless steel strips is 10.4% (with an area of 1.0cm 2 ), and that with an area of 13.3cm 2 is 6.6% [14] .
从以上文献与专利说明书中我们可知,纳米涂料的涂覆过程决定其必须添加各种有机添加剂,以便使纳米粒子能够稳定、均匀地分散于溶剂中,并防止纳米粒子的絮凝,这些添加剂会在半导体薄膜中形成杂质缺陷,形成预置层的多孔、疏松结构。涂料涂覆与干燥形成薄膜后,纳米粒子之间仅是切线式点接触,接触面积相对很小,使加热形成大晶粒致密薄膜时,其反应动力学受到阻碍而使情况变得很复杂,因而其反应动力学在许多方面与粒子之间接触的表面积总数有关。氧化物纳米涂料需要两次加热步骤,一次是疏松结构的氧化物还原成致密的金属合金,然后再加热硒化或在H2Se有毒气体中进一步硒化,制备的光吸收层成份均匀、半导体带隙平整,硫化处理能够在表层形成梯度带隙和表层高阻的双性能p型半导体薄膜;但是,其高温氢还原时间长,能源消耗大,存在爆炸的危险,其技术诀窍借鉴了真空溅射金属预置层后硒化制备薄膜电池的技术;硒化物纳米粒子的制备需要在有机溶剂中反应制备,消耗大量的有机溶剂,易造成环境污染,相对成本较高;在非真空后处理的重熔结晶过程中,依赖于预置层中低熔点组份的液相辅助再结晶过程的薄膜致密化机理,它借鉴了多元共蒸发气相沉积薄膜时晶体的液相生长技术,最终获得了柱状致密的大晶粒薄膜;但薄膜孔隙中遗留的涂料添加剂与夹杂等缺陷很难完全消除,快速热处理制备的光吸收层成份均匀性较差,薄膜表层的结晶质量不高,杂质与晶界复合较多而影响电池pn结的品质,使薄膜电池的开路电压Voc较低。From the above documents and patent specifications, we know that the coating process of nano-coatings determines that various organic additives must be added so that the nanoparticles can be stably and uniformly dispersed in the solvent and prevent the flocculation of the nanoparticles. Impurity defects are formed in the semiconductor thin film, forming a porous and loose structure of the pre-set layer. After the paint is coated and dried to form a film, the nanoparticles are only in tangential point contact, and the contact area is relatively small. When heating to form a dense film with large grains, the reaction kinetics are hindered and the situation becomes very complicated. The reaction kinetics are thus in many ways related to the total amount of surface area in contact between the particles. Oxide nano-coatings require two heating steps, one is the reduction of loose structure oxides into dense metal alloys, and then heating for selenization or further selenization in H 2 Se poisonous gas, the prepared light-absorbing layer has uniform composition, semiconductor The band gap is flat, and the sulfuration treatment can form a dual-performance p-type semiconductor film with a gradient band gap and a high surface resistance on the surface; however, its high-temperature hydrogen reduction time is long, energy consumption is large, and there is a danger of explosion. Its technical know-how is borrowed from vacuum sputtering The technology of preparing thin-film batteries by selenization after irradiating metal pre-layers; the preparation of selenide nanoparticles needs to be prepared by reaction in organic solvents, which consumes a large amount of organic solvents, which is easy to cause environmental pollution and relatively high cost; non-vacuum post-processing In the process of remelting and crystallization, the film densification mechanism depends on the liquid phase assisted recrystallization process of the low melting point components in the preset layer. Dense large-grain film; however, it is difficult to completely eliminate defects such as coating additives and inclusions left in the pores of the film, and the composition uniformity of the light-absorbing layer prepared by rapid heat treatment is poor, the crystallization quality of the film surface is not high, and impurities and grain boundaries are recombined More will affect the quality of the pn junction of the battery, making the open circuit voltage Voc of the thin film battery lower.
电沉积制备硒化物薄膜的特点:可对被沉积材料进行自纯化作用,可使用较低纯度的原材料,可根据沉积电位来改变预置层薄膜中的成份,便于形成梯度带隙分布,与涂覆法相比其预置层薄膜较致密。存在的问题是:Mo衬底在沉积初期发生化学置换反应而腐蚀、溶液中溶质的溶解度小,电沉积半导体硒化薄膜的电流密度相对较小,电沉积与涂覆法相比薄膜的沉积速度偏低、薄膜中含有大量的氧、溶液的稳定性依然存在着问题等,只有在H2Se或类H2Se气体中的处理才能有效地除去氧化物,这对消除有毒气体的使用增添了困难。另一方面,过度地追求电沉积硒化物前驱薄膜的成份要求符合薄膜电池的化学计量比是不恰当的,电沉积硒化物前驱薄膜中过量的高熔点硒化物会阻碍薄膜进一步地致密化,薄膜中即使存在过量的CuSe(富铜结构),也不能在加热过程中产生明显的液相物聚集或凝聚、包裹其它颗粒而产生滑动、薄膜变形(致密化)或在薄膜表面析出;如果不沉积In、Ga来中和掉多余Cu2Se,就需要KCN溶液通过浸润、溶解掉薄膜中的Cu2Se。The characteristics of selenide film prepared by electrodeposition: it can self-purify the deposited material, use lower-purity raw materials, and change the composition of the pre-set film according to the deposition potential, which is convenient for forming a gradient band gap distribution. The coating method is denser than the pre-layer film. The existing problems are: the Mo substrate corrodes due to chemical replacement reaction at the initial stage of deposition, the solubility of solute in the solution is small, the current density of the electrodeposited semiconductor selenide film is relatively small, and the deposition rate of the film is slower than that of the electrodeposition method compared with the coating method. Low, the film contains a lot of oxygen, the stability of the solution still has problems, etc., only the treatment in H2Se or H2Se -like gas can effectively remove oxides, which adds difficulties to the elimination of toxic gases . On the other hand, it is inappropriate to excessively pursue the composition requirements of the electrodeposited selenide precursor film to meet the stoichiometric ratio of the thin film battery. The excessive high melting point selenide in the electrodeposited selenide precursor film will hinder the further densification of the film. Even if there is an excessive amount of CuSe (copper-rich structure), it cannot produce obvious liquid phase aggregation or agglomeration during the heating process, wrapping other particles to cause sliding, film deformation (densification) or precipitation on the film surface; if not deposited To neutralize excess Cu 2 Se with In and Ga, KCN solution is required to dissolve Cu 2 Se in the film through wetting.
发明内容 Contents of the invention
本发明是鉴于上述技术在工业化生产过程中实际存在的问题而构成的,它提供了一种低成本制备CIGS薄膜电池硒化物前驱膜与快速硒硫化热处理直接制备薄膜太阳电池的方法。可用于低成本纳米涂料印刷滚涂法或水浴电沉积前驱硒化物薄膜直接快速硒硫化处理,并连续化地进行薄膜电池后续工序的生产,制备出高效无镉CIGS薄膜太阳电池集成光伏组件。该薄膜太阳电池的光吸收层是通过真空快速热处理使疏松或多孔微晶前驱体薄膜熔融、颗粒间浸润、液相辅助晶体合成反应生长的同时,进行金属靶反应溅射In2Se3与/或In2S3,使薄膜整体成份由富铜转变为贫铜结构,微量过剩的In2S3在薄膜电池吸收层的表面生成高阻OVC(有序缺陷黄铜矿)结构的n-Cu(In,Ga)3(Se,S)5,构成了低成本制备薄膜电池的pn浅埋结和双性能光吸收层;由于硒化物前驱薄膜中Ga和S元素分别在Mo背电极处与薄膜表层均有较高含量或其中Ga呈V型分布,快速硒硫化热处理后,该薄膜的半导体带隙在薄膜厚度的纵深方向呈现V型分布,薄膜表面具有pn浅埋结。随着基片温度的降低,再在光吸收层上反应溅射沉积n型高阻本征i-In(OH,S)/ZnS(O,OH)/ZnO(S)透明缓冲层与i层。随后溅射沉积低阻透明n-ZnO:Al薄膜构成电池的n型导电层,就完成了此类低成本硒化物前驱薄膜制备CIGS薄膜电池较完整的pin构造,它与共蒸发最高效率(19.9%)的CIGS薄膜电池理论模型与实际结构呈现了较明显的一致性。The present invention is formed in view of the problems actually existing in the industrial production process of the above-mentioned technologies, and it provides a low-cost method for preparing selenide precursor films for CIGS thin-film cells and rapid selenium sulfidation heat treatment to directly prepare thin-film solar cells. It can be used for low-cost nano-coating printing roll coating method or water-bath electrodeposition precursor selenide thin film direct rapid selenium vulcanization treatment, and continuous production of thin-film battery follow-up process to prepare high-efficiency cadmium-free CIGS thin-film solar cell integrated photovoltaic modules. The light-absorbing layer of the thin-film solar cell is made of loose or porous microcrystalline precursor film melting, inter-particle infiltration, and liquid-phase assisted crystal synthesis reaction growth through rapid vacuum heat treatment, and metal target reactive sputtering of In 2 Se 3 and/or Or In 2 S 3 , so that the overall composition of the film changes from copper-rich to copper-poor structure, and a small amount of excess In 2 S 3 generates n-Cu with a high resistance OVC (ordered defect chalcopyrite) structure on the surface of the absorber layer of the thin film battery (In, Ga) 3 (Se, S) 5 constitutes the pn shallow buried junction and dual-performance light-absorbing layer for low-cost preparation of thin-film batteries; since the Ga and S elements in the selenide precursor film are respectively at the Mo back electrode and the film The surface layer has a relatively high content or the Ga in it has a V-shaped distribution. After rapid selenium sulfidation heat treatment, the semiconductor band gap of the film presents a V-shaped distribution in the depth direction of the film thickness, and the film surface has a pn shallow buried junction. As the temperature of the substrate decreases, the n-type high-resistance intrinsic i-In(OH,S)/ZnS(O,OH)/ZnO(S) transparent buffer layer and i-layer are deposited on the light absorbing layer by reactive sputtering. . Subsequent sputtering deposits a low-resistance transparent n-ZnO:Al thin film to form the n-type conductive layer of the battery, and this kind of low-cost selenide precursor film is completed to prepare a relatively complete pin structure for CIGS thin-film batteries, which has the highest efficiency with co-evaporation (19.9% ) CIGS thin film battery theoretical model and the actual structure showed a more obvious consistency.
本发明的另外目的是提供一种用于CIGS薄膜太阳电池的制造工艺,与过去的真空法相比,可大幅度降低前期制造设备的投入,大幅度提高薄膜太阳电池制造过程中稀散贵金属原材料的利用率,降低了制造过程的能源消耗,缩短与简化了制造工艺环节,揉合了共蒸发与溅射预置层后硒化制备薄膜电池的技术优势,提升了低成本制备方法生产薄膜电池的品质,从而降低CIGS类薄膜太阳电池的原材料与制造成本,促使太阳能电池获得更广泛地应用。Another object of the present invention is to provide a manufacturing process for CIGS thin-film solar cells, which can greatly reduce the investment in early stage manufacturing equipment and greatly improve the utilization of sparse precious metal raw materials in the thin-film solar cell manufacturing process compared with the vacuum method in the past The efficiency reduces the energy consumption in the manufacturing process, shortens and simplifies the manufacturing process, combines the technical advantages of co-evaporation and sputtering pre-layer selenization to prepare thin-film batteries, and improves the quality of thin-film batteries produced by low-cost preparation methods , thereby reducing the raw material and manufacturing costs of CIGS thin-film solar cells, and promoting the wider application of solar cells.
为解决上述课题,本发明提供了非真空低成本法制备薄膜电池的硒化物前驱薄膜与快速硒硫化热处理制备薄膜太阳电池的方法,其主要特征在于:(1)在刚性衬底基片的钼电极薄膜上顺序涂覆纳米硒化物涂料与干燥成膜,或顺序电镀(或电沉积)不同组份纳米微晶硒化物前驱薄膜,该硒化物前驱薄膜成份与构造分别是:(CuGaSe2+CuSe)、(Ga2Se3+CuSe)、In4Se3(或In2Se3+CuInSe2)、CuSe[或(CuSe+Ga2Se3)、(CuSe+CuGaSe2)]的顺序取舍式组合;(2)制备了该硒化物前驱薄膜的一摞刚性基板被放置于真空室内的气密空间中,通过从室温至290℃高真空加热、注入氢气,再抽至高真空与注入氢气的多次操作和最后注入氩气+氢气的第一氢化预处理工序;(3)第二硒化处理,将该摞基片由上而下或由下而上地平行移动,分别一片片地推入另一相对的气密空间,先启动基片底部的加热,并向第二气密空间导入类H2Se气体,在保持足够的硒气压(20~80kPa)时,对移动中的基片进行上下快速加热或上部扫描式加热与底部随基片移动的固定方式加热、升温,基片本身始终保持在350℃~580℃,基片表层由于高功率辐射热源的移动式扫描加热,前驱硒化物薄膜会快速升温到350℃~1100℃,促使硒化物前驱薄膜中CuxSe/与In4Se3相受热快速融化(523℃液化),辅助CIGS薄膜晶体液相反应生长和薄膜自身的致密化,大晶粒致密的CIGS薄膜生成后,其表层会渗出微量或吸附着多余液相CuxSe;(4)第三硒硫化处理,基片衬底在520℃~580℃适宜温度时,将基片运动转移至溅射位置,调节气密空间气压至0.3~25Pa,通过反应溅射In2Se3或In2S3中和反应掉基片表层多余的液相CuxSe,严格控制基片表面CIGS薄膜成份由富铜转变成贫铜结构过程中In2Se3或In2S3的溅射量;(5)第四硒化处理,反应溅射结束后,增大气密空间导入类H2Se气体量,使其环境硒气压达20~80kPa时,高功率辐射热源对基片进行更快速度的热扫描;(6)第五高温硫化处理,排空类H2Se气体后,重新注入反应溅射气体H2S+Ar,维持气压在0.3~25Pa,基片移动至溅射位置后进行反应溅射In2S3,它在薄膜表层生成n型Cu(In1-xGax)SSe或Cu(In1-yGay)3(Se1-xSx)5高阻层;在上述快速硒硫化热处理的操作过程中,第二气密空间交替充入类H2Se气体或H2S+Ar气体,中间进行过高真空排气,其气压有升有降;(7)将经过快速硒硫化热处理后的基片转移至第三气密冷却空间;这样,第一空间整摞基片在经过快速硒硫化热处理后归入第三冷却空间,该空间注入有Ar+H2S混合气体,保证基片衬底逐渐由580℃下降至110℃过程中,CIGS薄膜材料内硒硫元素不流失;(8)降温后的基片分别被推入第四气密空间,进行金属靶反应溅射沉积薄膜电池的高阻本征In(OH,S)/ZnS(O,OH)/ZnO(S)缓冲层与i层,二或三对纯金属溅射靶的材质与反应气体的搭配是:In/(Ar、H2S与H2O)、Zn/(Ar、H2S与H2O)和Zn/(Ar、H2S与O2或CO2),溅射过程中基片衬底的温度控制在110℃~350℃;溅射完成后气密空间被抽至高真空状态,启动高功率辐射热源快速扫描基片表面;(9)将反应溅射沉积了高阻缓冲层后的基片分别归入第五冷却空间;基片冷却后就可转入下一激光加工处理或机械划线的电池集成组件的电极串联连接工序,或沉积低阻透明导电ZnO:Al薄膜工序。In order to solve the above-mentioned problems, the present invention provides the method for preparing thin-film solar cells by non-vacuum low-cost method for preparing the selenide precursor thin film of thin-film battery and rapid selenium sulfidation heat treatment, and its main features are: (1) molybdenum on rigid substrate substrate Sequential coating of nano-selenide coatings on the electrode film and drying to form a film, or sequential electroplating (or electrodeposition) of different components of nano-microcrystalline selenide precursor films, the composition and structure of the selenide precursor films are: (CuGaSe 2 +CuSe ), (Ga 2 Se 3 +CuSe), In 4 Se 3 (or In 2 Se 3 +CuInSe 2 ), CuSe [or (CuSe+Ga 2 Se 3 ), (CuSe+CuGaSe 2 )] sequential combination ; (2) A stack of rigid substrates on which the selenide precursor film was prepared was placed in an airtight space in a vacuum chamber, heated in a high vacuum from room temperature to 290°C, injected with hydrogen, and then evacuated to a high vacuum and injected with hydrogen several times Operation and the first hydrogenation pretreatment process of injecting argon + hydrogen at last; (3) second selenization treatment, the stack of substrates is moved in parallel from top to bottom or bottom to top, and pushed into another stack of substrates one by one. In a relatively airtight space, start the heating of the bottom of the substrate first, and introduce H 2 Se-like gas into the second airtight space, while maintaining sufficient selenium pressure (20-80kPa), move the substrate up and down Rapid heating or upper scanning heating and fixed heating and heating at the bottom moving with the substrate. The substrate itself is always kept at 350 ° C ~ 580 ° C. The surface layer of the substrate is heated by the mobile scanning of the high-power radiation heat source. It will quickly heat up to 350°C~1100°C, which will promote the rapid melting of the Cu x Se/ and In 4 Se 3 phases in the selenide precursor film (liquefied at 523°C), assisting the liquid phase reaction growth of the CIGS film crystal and the densification of the film itself. After the large-grained and dense CIGS film is formed, a small amount of Cu x Se in the surface layer will ooze out or absorb excess liquid phase; (4) the third selenium sulfidation treatment, when the substrate is at a suitable temperature of 520 ° C to 580 ° C, the The movement of the substrate is transferred to the sputtering position, and the pressure in the airtight space is adjusted to 0.3-25Pa. The excess liquid phase Cu x Se on the surface of the substrate is neutralized and reacted by reactive sputtering of In 2 Se 3 or In 2 S 3 , and the substrate is strictly controlled. The sputtering amount of In 2 Se 3 or In 2 S 3 in the process of changing the composition of the CIGS film on the surface of the sheet from copper-rich to copper-poor structure; The amount of H 2 Se gas is so that when the ambient selenium pressure reaches 20-80kPa, the high-power radiation heat source performs faster thermal scanning on the substrate; (6) the fifth high-temperature sulfurization treatment, after the H 2 Se-like gas is evacuated, Re-inject the reactive sputtering gas H 2 S+Ar, maintain the pressure at 0.3-25Pa, move the substrate to the sputtering position and perform reactive sputtering of In 2 S 3 , which generates n-type Cu (In 1-x Ga x ) SSe or Cu(In 1-y Ga y ) 3 (Se 1-x S x ) 5 high-resistance layer; during the operation of the above-mentioned rapid selenium sulfidation heat treatment, the second airtight space is alternately filled with H 2 Se-like gas or H 2 S+Ar gas, high vacuum exhaust is carried out in the middle, and its pressure rises and falls; (7) the substrate after rapid selenium sulfide heat treatment is transferred to the third airtight cooling space; thus, the first Space The whole stack of substrates is put into the third cooling space after rapid selenium sulfidation heat treatment. This space is injected with Ar+H 2 S mixed gas to ensure that the substrate substrate gradually drops from 580°C to 110°C. CIGS thin film material The internal selenium and sulfur elements are not lost; (8) the cooled substrates are pushed into the fourth airtight space respectively, and the high resistance intrinsic In(OH,S)/ZnS(O, OH)/ZnO(S) buffer layer and i layer, two or three pairs of pure metal sputtering target materials and reaction gases are: In/(Ar, H 2 S and H 2 O), Zn/(Ar, H 2 S and H 2 O) and Zn/(Ar, H 2 S and O 2 or CO 2 ), the temperature of the substrate during the sputtering process is controlled at 110 ° C ~ 350 ° C; after the sputtering is completed, the airtight space After being pumped into a high vacuum state, a high-power radiation heat source is started to quickly scan the surface of the substrate; (9) the substrates deposited with a high-resistance buffer layer by reactive sputtering are respectively classified into the fifth cooling space; after the substrate is cooled, it can be transferred to The next laser processing or mechanical scribing of the electrode series connection process of the battery integrated assembly, or the process of depositing a low-resistance transparent conductive ZnO:Al film.
根据本发明可知,前驱硒化物薄膜是按一定顺序涂覆或滚涂纳米硒化物涂料与干燥成膜的,或顺序水浴电沉积制备纳米微晶硒化物前驱薄膜而获得的,这些硒化物前驱薄膜的成份分别是:CuGaSe2、Ga2Se3、CuInSe2、CuSe、In4Se3或In2Se3的排列组合,其中仅富硒CuSe和贫硒In4Se3是低熔点(523℃)的硒化物,它们是硒化物前驱薄膜中不可缺少或必备成份,决定着能否让疏松的硒化物薄膜经过快速硒硫化热处理后,直接制备出大晶粒致密的吸收层薄膜。也就是说,必须通过多种二元(含少量三元)硒化物微晶颗粒之间进行合成反应,才能使前驱硒化物薄膜最终生成四元柱状、大晶粒致密的PV(光伏)级薄膜,其中均要利用合成反应过程中较低熔点二元硒化物CuSe和/或In4Se3(523℃)的固液相晶体反应生长机制,并且不能让前驱硒化物薄膜中高熔点固相硒化物(Ga2Se3、CuInSe2、CuGaSe2、In2Se3)阻止薄膜中低熔点硒化物微晶颗粒熔化、浸润、液相包裹着高熔点颗粒所导致的细观滑动、微观孔洞被填平或堵塞等薄膜的塑性变形过程与密实化进程。According to the present invention, the precursor selenide thin film is obtained by coating or rolling nano-selenide coating and drying film in a certain order, or sequential water-bath electrodeposition to prepare nano-microcrystalline selenide precursor film. These selenide precursor films The components are: the arrangement and combination of CuGaSe 2 , Ga 2 Se 3 , CuInSe 2 , CuSe, In 4 Se 3 or In 2 Se 3 , of which only selenium-rich CuSe and selenium-poor In 4 Se 3 have a low melting point (523°C) Selenides, which are indispensable or essential components in the selenide precursor film, determine whether the loose selenide film can be directly prepared with a large grain and dense absorbing layer film after rapid selenium sulfurization heat treatment. That is to say, it is necessary to carry out a synthesis reaction between a variety of binary (including a small amount of ternary) selenide microcrystalline particles, so that the precursor selenide film can finally generate a quaternary columnar, large-grain dense PV (photovoltaic) film. , in which the solid-liquid phase crystal reaction growth mechanism of the lower melting point binary selenide CuSe and/or In 4 Se 3 (523°C) should be used during the synthesis reaction, and the high melting point solid phase selenide in the precursor selenide film should not be allowed to (Ga 2 Se 3 , CuInSe 2 , CuGaSe 2 , In 2 Se 3 ) prevent the microscopic sliding and filling of microscopic holes caused by the melting and infiltration of low melting point selenide microcrystalline particles in the film, and the liquid phase wrapping high melting point particles Plastic deformation process and densification process of films such as blockage or blockage.
在本发明中,纳米硒化物涂覆、滚涂的前驱薄膜中难免夹杂高分子有机物,水浴电沉积硒化物薄膜中夹杂着约15%以上的氧化物,它们均需要通过从室温至290℃高真空加热、注入氢气,抽至高真空与注入氢气的多次操作工序和最后注入氩气+氢气的第一氢化预处理工序;硒化物前驱薄膜在290℃温度以下时,其内部发生合成反应几率较小,有利于多孔薄膜的表面与内部微晶吸附气体被脱附、部分氧化物被还原,加热使夹杂的有机物挥发或脱附等工艺措施均是必须的,硒化物前驱薄膜材料在正式快速加热前被调制到电子级高纯态对后续薄膜的重结晶制备半导体器件是非常有益的。第二气密空间导入类H2Se气体前被抽至1×10-3Pa以上的高真空,在与第一气密空间气压平衡后,打开两室之间的闸板阀,将第一室内的一片基片推入快速硒硫化热处理室内的气密空间并关闭闸板阀,继续导入类H2Se气体至50~80kPa的气压后,就可进行第二硒硫化处理工序;类H2Se气体成份的组成为:30%~50%氩气、25%~35%氢气、15%~45%H2Se。在保持足够硒气氛的前提下,对移动中的基片先下后上或上下同时快速扫描式加热与升温,基片自身保持在350℃~580℃的温度范围,高功率辐射热源使基片表层的前驱硒化物薄膜快速升温到350℃~1100℃,促使硒化物前驱薄膜中间的微晶CuSe和/或In4Se3快速受热融化(523℃液化)辅助CIGS薄膜晶体的液相反应生长,薄膜自身经历着重熔与再结晶的致密化过程,快速加热促进了前驱硒化物薄膜内发生化学合成反应,最终生成高熔点、大晶粒致密的CIGS薄膜。由于制备硒化物前驱薄膜时对成份严格要求为富铜结构,表层有意识地安排较多的微晶CuSe,快速加热后表层会渗出微量液相CuxSe,此时衬底基片应该维持在520℃~580℃,基片底部加热器处于恒功率控制状态。当整个基片完全生成CIGS大晶粒致密薄膜时,其表面会吸附着多余的液相Cu2Se,降低环境中硒气压至0.3~15Pa,基片转移至反应溅射区域,进行反应溅射In2Se3或In2S3,严格监控基片表层多余液相Cu2Se被反应中和掉时或薄膜中铜含量降低到24.5%时,恒功率加热条件下基片薄膜表面的物理状态会出现非常明显的变化,即CIGS薄膜成份由富铜转变成贫铜结构的过程中溅射In2Se3或In2S3的量需要精确地监控。In the present invention, the precursor films coated with nano-selenide and roll-coated are inevitably mixed with polymeric organic matter, and the selenide film deposited by water bath electrodeposition contains more than 15% oxides. Vacuum heating, hydrogen injection, multiple operations of pumping to high vacuum and hydrogen injection, and finally the first hydrogenation pretreatment process of injecting argon + hydrogen; when the temperature of the selenide precursor film is below 290 ° C, the synthesis reaction inside it is relatively low. Small, it is beneficial for the surface and internal microcrystalline adsorption gas of the porous film to be desorbed, part of the oxides to be reduced, heating to volatilize or desorb the mixed organic matter and other technological measures are necessary. The selenide precursor film material is rapidly heated in the formal It is very beneficial for the subsequent recrystallization of thin films to prepare semiconductor devices after being modulated to an electronic-grade high-purity state. The second airtight space is evacuated to a high vacuum above 1×10 -3 Pa before introducing H 2 Se-like gas. After the air pressure in the first airtight space is balanced, the gate valve between the two chambers is opened, and the first Push a piece of substrate in the room into the airtight space of the rapid selenium sulfidation heat treatment chamber and close the gate valve, continue to introduce H 2 Se-like gas to a pressure of 50-80kPa, and then proceed to the second selenium sulfide treatment process; The composition of Se gas components is: 30%-50% argon, 25%-35% hydrogen, 15%-45% H 2 Se. On the premise of maintaining a sufficient selenium atmosphere, the moving substrate is first lowered and then upper or up and down at the same time. The substrate itself is kept at a temperature range of 350°C to 580°C, and the high-power radiation heat source makes the substrate The temperature of the precursor selenide film on the surface is rapidly raised to 350 ° C ~ 1100 ° C, which promotes the rapid melting of microcrystalline CuSe and/or In 4 Se 3 in the middle of the selenide precursor film (liquefied at 523 ° C) to assist the liquid phase reaction growth of CIGS thin film crystals, The film itself undergoes a densification process of remelting and recrystallization, and rapid heating promotes the chemical synthesis reaction in the precursor selenide film, and finally produces a CIGS film with a high melting point and large grain density. Since the composition of the selenide precursor film is strictly required to be a copper-rich structure, more microcrystalline CuSe is consciously arranged on the surface layer, and a small amount of liquid phase Cu x Se will seep out of the surface layer after rapid heating. At this time, the substrate should be maintained at 520 ℃ ~ 580 ℃, the heater at the bottom of the substrate is in a constant power control state. When the entire substrate is completely formed with a CIGS large-grain dense film, excess liquid phase Cu 2 Se will be adsorbed on its surface, the selenium pressure in the environment will be reduced to 0.3-15Pa, and the substrate will be transferred to the reactive sputtering area for reactive sputtering In 2 Se 3 or In 2 S 3 , strictly monitor the physical state of the substrate film surface under constant power heating conditions when the excess liquid phase Cu 2 Se on the substrate surface is neutralized by reaction or when the copper content in the film is reduced to 24.5%. There will be a very obvious change, that is, the amount of sputtered In 2 Se 3 or In 2 S 3 needs to be accurately monitored during the transition of the composition of the CIGS film from copper-rich to copper-poor structure.
由于硒化物前驱薄膜本身是疏松结构,其传导热的性能被限制;本发明优选先从底部加热与升温,硒化物前驱薄膜中接近钼薄膜的CuGaSe2+CuSe与Ga2Se3在380℃开始合成反应,薄膜中少量CuGaSe2作为高熔点硒化物的仔晶,诱导CuxSe与Ga2Se3在其周围反应生成宽带隙CuGaSe2大晶粒薄膜,致使基片的钼薄膜被大晶粒CuGaSe2相互连接成片而覆盖;另一方面,CuGaSe2中微量镓与钼容易反应生成金属化合物,极大地改善CIGS薄膜与背电极钼薄膜之间的接合力,阻止背电极钼元素继续与过量的硒反应生成MoSe。如果此时上部(或外部)的高功率辐射热源快速扫描硒化物前驱薄膜,其表面就会产生融熔、颗粒间浸润、塌陷或收缩等现象,高熔点Cu(In,Ga)Se2微晶会诱导低熔点液相CuxSe和In4Se3与Ga2Se3在其周围反应生长成CIGS大晶体薄膜,各大品粒间的晶界被消融,前驱薄膜底部与表层Ga与In元素相互扩散,在大晶粒薄膜深度方向自然形成平滑的成份梯度分布与半导体梯度带隙,多余或过量的液相Cu2Se吸附在大品粒CIGS薄膜的表层,被随后溅射的In2Se3或In2S3中和反应掉;加大注入类H2Se气体的量,使环境气压达20~80kPa时,再次启动高功率辐射热源快速扫描基片表面,基片表层的薄膜快速熔融削除了各大晶粒间的晶界,晶粒内Cu2Se、In2Se3等杂相物被溶解,填平了晶界之间低洼处与抹平了大晶粒表面的凸起部,使CIGS薄膜断面的晶体非常完整、薄膜的微观表面也很平滑,降低了薄膜电池中有效的晶界复合,提高了电池开路电压Voc;排空类H2Se气体后重新注入H2S气体,溅射沉积In2S3后的薄膜表层生成n型Cu(In1-xGax)SSe或Cu(In1-yGay)3(Se1-X,SX)5高阻层,其厚度大约20~40nm,形成薄膜电池同质浅埋结或双性能光吸收层,改善了薄膜电池结特性与抑制漏电流,提高了薄膜电池光电转换效率。同理,随着基片CIGS薄膜的自然冷却,启动溅射电池缓冲层的n型本征高阻In(OH,S)/ZnS(O,OH)/ZnO(S)薄膜后,第四气密空间抽至高真空后,启动高功率辐射热源快速扫描基片表面,使溅射沉积缓冲层材料中的气体脱附、薄膜晶粒间更密实和锌硫元素向p型CIGS薄膜表层扩散,改善了薄膜电池pn结内建电场区的品质。Since the selenide precursor film itself has a loose structure, its heat conduction performance is limited; in the present invention, it is preferable to heat and raise the temperature from the bottom first, and the CuGaSe 2 +CuSe and Ga 2 Se 3 close to the molybdenum film in the selenide precursor film start at 380°C In the synthesis reaction, a small amount of CuGaSe 2 in the film is used as the seed crystal of high melting point selenide, which induces Cu x Se and Ga 2 Se 3 to react around it to form a wide-bandgap CuGaSe 2 large-grain film, resulting in the molybdenum film on the substrate being covered by large grain CuGaSe 2 is interconnected into sheets to cover each other; on the other hand, the trace amount of gallium and molybdenum in CuGaSe 2 is easy to react to form a metal compound, which greatly improves the bonding force between the CIGS film and the molybdenum film of the back electrode, and prevents the molybdenum element of the back electrode from continuing to contact with excessive molybdenum. Selenium reacts to form MoSe. If the upper (or external) high-power radiation heat source quickly scans the selenide precursor film at this time, the surface will produce melting, intergranular infiltration, collapse or shrinkage, and the high melting point Cu(In, Ga)Se 2 microcrystal It will induce the low melting point liquid phase Cu x Se and In 4 Se 3 to react with Ga 2 Se 3 to grow into a CIGS large crystal film around it, the grain boundaries between the major grains are ablated, and the Ga and In elements at the bottom and surface of the precursor film Interdiffusion, naturally forming a smooth composition gradient distribution and semiconductor gradient band gap in the depth direction of the large-grained film. The excess or excess liquid phase Cu 2 Se is adsorbed on the surface of the large-grained CIGS film, and is subsequently sputtered by In 2 Se 3 or In 2 S 3 to neutralize and react; increase the amount of injected H 2 Se-like gas so that when the ambient pressure reaches 20-80kPa, start the high-power radiation heat source again to quickly scan the surface of the substrate, and the film on the surface of the substrate melts rapidly The grain boundaries between the large grains are cut off, Cu 2 Se, In 2 Se 3 and other impurity phases in the grains are dissolved, and the low-lying places between the grain boundaries and the raised parts on the surface of the large grains are smoothed , so that the crystal of the CIGS film section is very complete, and the microscopic surface of the film is also very smooth, which reduces the effective grain boundary recombination in the film battery and increases the open circuit voltage Voc of the battery; after the H 2 Se-like gas is evacuated, the H 2 S gas is re-injected , the surface layer of the film after sputtering deposition of In 2 S 3 generates an n-type Cu(In 1-x Ga x )SSe or Cu(In 1-y Ga y ) 3 (Se 1-X , S X ) 5 high resistance layer, Its thickness is about 20-40nm, forming a homogeneous shallow buried junction or dual-performance light-absorbing layer of thin-film batteries, improving the junction characteristics of thin-film batteries and suppressing leakage current, and improving the photoelectric conversion efficiency of thin-film batteries. Similarly, with the natural cooling of the CIGS film on the substrate, after the n-type intrinsically high resistance In(OH, S)/ZnS(O, OH)/ZnO(S) film of the sputtering battery buffer layer is started, the fourth gas After the dense space is evacuated to a high vacuum, a high-power radiation heat source is started to quickly scan the surface of the substrate to desorb the gas in the sputter-deposited buffer layer material, make the grains of the film more compact, and diffuse zinc and sulfur elements to the surface of the p-type CIGS film, improving The quality of the built-in electric field region of the pn junction of the thin film battery is guaranteed.
在本发明第一氢化预处理过程中,也可以加设遮断氢气供给,快速开启气密空间阀门的真空排气工序;通过该真空排气工序,气密空间暂时会成为高真空状态,加热与高真空使硒化物前驱薄膜中夹杂的有机物再次挥发或脱附,重新注入氢气使活性高的氢气与硒化物前驱膜中的氧化物反应,使硒化物前驱薄膜材料尽可能地被还原成电子级高纯态,彻底削除薄膜中有机物的夹杂,减少氧化物的存在。同理,第二、三、四气密空间的真空室内同样也设有真空排气机构,可以进行真空排气操作程序,它被用来调整薄膜中的某些状态。In the first hydrogenation pretreatment process of the present invention, it is also possible to add a vacuum exhaust process that cuts off the hydrogen supply and quickly opens the airtight space valve; through this vacuum exhaust process, the airtight space will temporarily become a high vacuum state, heating and The high vacuum makes the organic matter contained in the selenide precursor film volatilize or desorb again, and re-inject hydrogen to make the highly active hydrogen react with the oxides in the selenide precursor film, so that the selenide precursor film material can be reduced to electronic grade as much as possible High-purity state, completely remove the inclusion of organic matter in the film, and reduce the existence of oxides. Similarly, the vacuum chambers of the second, third, and fourth airtight spaces are also provided with a vacuum exhaust mechanism, which can perform vacuum exhaust operation procedures, and it is used to adjust certain states in the film.
因此,通过本发明制造的低成本硒化物前驱薄膜经过快速硒硫化热处理制备的CIGS薄膜太阳电池,能够可靠地获得黄铜矿型薄膜太阳电池特征性的光电转换效率,随着技术的不断完善,其性能将达到真空共蒸发制备薄膜电池的水平。Therefore, the CIGS thin-film solar cell prepared by rapid selenium sulfidation heat treatment through the low-cost selenide precursor film manufactured by the present invention can reliably obtain the characteristic photoelectric conversion efficiency of chalcopyrite-type thin-film solar cells. With the continuous improvement of technology, Its performance will reach the level of thin-film batteries prepared by vacuum co-evaporation.
本发明的其它目的、优点和新特征的部分将在下面的说明书中陈述,并且该部分对本领域的技术人员来说,通过对下面附图说明、具体实施方法和案例的研究是容易了解的。The other objectives, advantages and novel features of the present invention will be stated in the following description, and this part will be easily understood by those skilled in the art through the study of the following descriptions of drawings, specific implementation methods and cases.
附图说明 Description of drawings
图1所示是一般CIGS类薄膜太阳电池各层结构的简图;Figure 1 is a schematic diagram of the structure of each layer of a general CIGS thin-film solar cell;
图2是本发明低成本前驱硒化物薄膜与快速硒硫化处理制备的薄膜太阳电池结构简图;Fig. 2 is the thin-film solar cell structural diagram that the present invention's low-cost precursor selenide thin film and rapid selenium vulcanization treatment prepare;
图3所示是本发明的低成本硒化物前驱薄膜进行快速硒硫化热处理制备CIGS薄膜太阳电池的光吸收层的原理简图;Shown in Fig. 3 is that low-cost selenide precursor thin film of the present invention carries out fast selenium vulcanization heat treatment and prepares the schematic diagram of the principle of the light absorbing layer of CIGS thin film solar cell;
图4所示是本发明制备CIGS薄膜太阳电池光伏集成组件生产工序的主流程简图。其小,图4(a)反应溅射金属硅、钛靶制备SiO、TN与SiN等碱阻挡层;图4(b)溅射制备Mo电极层;图4(c)激光切割钼薄膜均分背电场制备各子电池的电极;图4(d)纳米涂料顺序滚涂制备或顺序电沉积制备硒化物前驱薄膜;图4(e)硒化物前驱薄膜氢化预处理;图4(f)硒化物前驱薄膜在硒气氛环境中重熔再结晶;图4(g)液相Cu2Se被反应溅射In2Se3或In2S3中和掉、高功率辐射热源快速扫描后重熔消除晶粒间晶界与抹平薄膜的高低凹凸表面,然后溅射In2S3生成高阻n型Cu(InGa)3(SeS)5;图4(h)反应溅射铟锌靶制备In(OH,S)/ZnS(O,OH)/ZnO(S)薄膜电池的缓冲层;图4(i)激光照射处理接触电极;图4(j)溅射透明导电ZnO:Al层;图4(k)激光照射反爆冲切割透明电极层;图4(l)CIGS薄膜电池光伏集成组件电极引线、封装。Fig. 4 is a schematic diagram of the main process of the production process of the CIGS thin film solar cell photovoltaic integrated module of the present invention. It is small, Figure 4(a) Reactive sputtering metal silicon, titanium target to prepare alkali barrier layers such as SiO, TN and SiN; Figure 4(b) Sputtering to prepare Mo electrode layer; Figure 4(c) Laser cutting molybdenum thin film The electrodes of each sub-battery were prepared in the back electric field; Fig. 4(d) nano-coating sequential roll coating or sequential electrodeposition to prepare selenide precursor film; Fig. 4(e) hydrogenation pretreatment of selenide precursor film; Fig. 4(f) selenide The precursor film is remelted and recrystallized in a selenium atmosphere; Fig. 4(g) liquid phase Cu 2 Se is neutralized by reactive sputtering In 2 Se 3 or In 2 S 3 , and remelted and decrystallized after a high-power radiation heat source is quickly scanned Intergranular grain boundaries and smoothing the uneven surface of the film, and then sputtering In 2 S 3 to generate high-resistance n-type Cu(InGa) 3 (SeS) 5 ; Figure 4(h) Reactive sputtering indium zinc target to prepare In(OH , S)/ZnS(O, OH)/ZnO(S) thin-film battery buffer layer; Figure 4(i) laser irradiation treatment of contact electrodes; Figure 4(j) sputtered transparent conductive ZnO:Al layer; Figure 4(k ) laser irradiating anti-explosion punching to cut the transparent electrode layer; Figure 4 (l) CIGS thin-film cell photovoltaic integrated module electrode leads and packaging.
图5(a)所示是纳米涂料印刷滚涂法或水浴电沉积法制备前驱硒化物薄膜快速硒硫化热处理制备薄膜电池光吸收层、缓冲层与i层装置的原理结构简图;图5(b)硒化物前驱薄膜通过(本发明方法制作的)直列式快速硒硫化热处理装置的原理简图;图5(c)薄膜电池光吸收层的表面连续地制备高阻缓冲层与本征i层;图5(b)、图5(c)分别是图5(a)大系统装置中32a和34a两个部件的放大图。Fig. 5 (a) shows that nano-coating printing roller coating method or water-bath electrodeposition method prepares the precursor selenide thin film rapid selenium vulcanization heat treatment and prepares the schematic structure diagram of thin-film battery light absorbing layer, buffer layer and i-layer device; Fig. 5 ( b) Schematic diagram of the principle of the in-line rapid selenium vulcanization heat treatment device for the selenide precursor thin film (made by the method of the present invention); Fig. 5 (c) The surface of the thin-film battery light-absorbing layer is continuously prepared with a high-resistance buffer layer and an intrinsic i layer ; Fig. 5 (b), Fig. 5 (c) are respectively enlarged views of two components of 32a and 34a in Fig. 5 (a) large system device.
具体实施方法Specific implementation method
本发明制造的低成本前驱硒化物薄膜太阳电池(图2所示)与传统黄铜矿型类CIGS薄膜太阳电池的基本结构(图1所示)是相同的,仅在制造途径或方法上存在一些差异,用非真空低成本方法先制备出硒化物前驱薄膜,再进行真空快速硒硫化热处理直接地制造出薄膜电池p型光吸收层(图3所示)、薄膜电池pn结区的缓冲层与i层,就可转入薄膜太阳电池集成组件的内联式电极串联连接的划线工序(电池底电极与面电极串联连接),或继续沉积n型低阻透明的窗口层ZnO:Al,制备出常规实验室检测用单体薄膜太阳电池。The basic structure (shown in Figure 1) of the low-cost precursor selenide thin-film solar cell (shown in Figure 2) made by the present invention is the same as that of the traditional chalcopyrite-type CIGS thin-film solar cell, and only exists in the manufacturing route or method There are some differences. The selenide precursor thin film is first prepared by a non-vacuum low-cost method, and then the vacuum rapid selenium sulfide heat treatment is used to directly manufacture the p-type light absorbing layer of the thin-film battery (as shown in Figure 3), and the buffer layer of the p-n junction region of the thin-film battery. With the i layer, it can be transferred to the scribing process of the inline electrode series connection of the thin film solar cell integrated module (the bottom electrode of the battery is connected in series with the surface electrode), or continue to deposit the n-type low-resistance transparent window layer ZnO:Al, A single thin-film solar cell for routine laboratory testing was prepared.
当使用质量均匀性较差的普通钠钙浮法玻璃或批次不同、质量参差不齐的玻璃时,玻璃表面碱成份是严重不均匀的,随着薄膜电池制备工艺的进行,会有其它杂质通过Mo薄膜电极层1c向光吸收层1d中扩散,影响光吸收层的品质和大面积结晶的均匀性;另外,电池工艺的实施会造成玻璃表面的碱爆,使Mo电极层薄膜与光吸收层之间的结合力减弱,导致薄膜电池吸收层与Mo薄膜的分离与脱落,影响薄膜电池的光电转换效率与填充因子FF。为了获得均质、优良的薄膜电池光伏集成组件,本发明优选在碱石灰玻璃(也称普通钠钙玻璃,英文缩写SLG)基片1a上顺序沉积碱阻挡层1b和Mo电极薄膜层1c,碱阻挡层由反应溅射金属硅或金属钛靶制备SiO、TiN、SiN等构成;另一原因是本发明硒化物前驱薄膜中含有CIGS薄膜光学吸收层在重熔再结晶过程中所需要的钠盐,SLG基片中钠通过Mo电极薄膜层扩散进入吸收层不是非常必需的。When using ordinary soda-lime float glass with poor quality uniformity or glass with different batches and uneven quality, the alkali composition on the surface of the glass is seriously uneven, and there will be other impurities as the thin-film battery manufacturing process proceeds Diffusion into the light-absorbing
图3表示本发明优选纳米涂料顺序滚涂或电化学逐层沉积硒化物前驱薄膜各层的构造,以及快速硒硫化热处理时,硒化物前驱薄膜受热重熔再结晶的原理简图,与图4(f)相关。Fig. 3 shows the structure of each layer of the preferred nano-coating sequential roll coating or electrochemical deposition of selenide precursor film layer by layer in the present invention, and during rapid selenium vulcanization heat treatment, the principle diagram of remelting recrystallization of the selenide precursor film, and Fig. 4 (f) Related.
图5(a)表示预制好硒化物前驱薄膜后的SLG基片放入快速硒硫化热处理装置内进行薄膜电池光吸收层与缓冲层与i层制备的装置原理简图,与图4(e)、图4(f)、图4(g)和图4(h)所示的前驱硒化物薄膜快速硒硫化热处理工序相对应,是经由闸板阀320、321、340、341将氢化预处理室31a、快速硒硫化热处理室32a、储片冷却室33a、溅射沉积室34a、取片室35a分别连通的直列式快速硒硫化热处理装置的原理性简图,在此装置上的各室31a、32a、33a、34a上分别连接着未图示的真空排气机构。如果再联接图4(i)、图4(j)和图4(k)的真空设备,就可以连续制备出薄膜电池的光伏集成组件。Figure 5(a) shows a schematic diagram of the device principle for preparing the thin-film cell light absorption layer, buffer layer and i-layer after the SLG substrate is placed into the rapid selenium sulfide heat treatment device after the prefabricated selenide precursor thin film, and Figure 4(e) , Fig. 4(f), Fig. 4(g) and Fig. 4(h) show that the rapid selenium vulcanization heat treatment process of the precursor selenide thin film is corresponding, is to pass the
图5(a)中的31a装置与图4(e)所示前驱硒化物薄膜氢化预处理工序相对应,在氢化预处理室31a的内部搭载着可收纳以批为单位的多个基片3a,基片3a放置在可上下升降、整体被搬运的支承机构上(未图示),支承架放置在气密空间312内,气密空间外侧有加热器311和热辐射屏蔽板310,以及基片推送机构313,在气密空间中还有氢气、氩气共用导入管和可控的排气阀门(未图示)。收纳在氢化预处理室内的一摞基片3a已进行了Mo电极薄膜层上的纳米硒化物前驱薄膜的顺序滚涂与烘干,或电化学顺序电沉积硒化物前驱薄膜,其中Mo底电极薄膜已被激光切割成被均分的薄膜单体;在以批为单位的基片3a中,经过加热氢化处理的基片3a保存于基片的可升降操作、水平搁置的搬运架上(未图示),它可由基片推送机构313与升降支承机构共同协作情况下,把基片3a一个个地经由闸板阀320推运至快速硒硫化热处理室32a的小车323上。The
图5(b)是本发明快速硒硫化热处理硒化物前驱薄膜制备薄膜电池吸收层装置的原理简图,它与图4(f)前驱硒化物薄膜在硒气氛环境中进行重熔再结晶工序和图4(g)反应溅射In2Se3或In2S3中和掉重熔再结晶吸收层表面的吸附CuxSe与溅射In2S3生成高阻n-Cu(In1-xGax)SSe或Cu(In1-yGay)3(Se1-xSx)5的工序相对应。在快速硒硫化热处理室32a中,可控制移动距离、速度的小车323上放置着基片3b,基片3b下均匀布置着电阻加热装置与基片3b接触的多对热电偶,可进行基片背部可控温度或恒功率方式的加热;可控制移动距离、速度和功率的高功率热辐射源324能对基片3b表面进行快速扫描式加热;在可移动小车323两侧安装有固定的H2Se或类H2Se气体导入管,在气体导入管靠近小车323的单侧壁上设有多个均匀布置的喷嘴孔,H2Se或类H2Se气体从喷嘴孔流向移动的基片3b的表面(未图示);在32a室中安装有一对金属铟反应溅射靶325,其上面分别安装有氩气和溅射反应气体导入管的两套气路;上述装置均被安置在气密空间326中,气密空间326上安装有可快速开启排气或调节气压的阀门和检测气体压力的真空裸规管(未图示)。打开闸板阀321,基片3b被储片冷却室33a内的取片机构331纳入可水平升降的基片承载机构333上(未图示)。Fig. 5 (b) is the schematic diagram of the present invention's rapid selenium vulcanization heat treatment selenide precursor film to prepare the absorbing layer device of thin film battery, and it carries out the remelting and recrystallization process and the remelting recrystallization process of it and Fig. 4 (f) precursor selenide film in selenium atmosphere environment Figure 4(g) Reactive sputtering of In 2 Se 3 or In 2 S 3 neutralizes the adsorbed Cu x Se on the surface of the remelted recrystallized absorber layer and sputters In 2 S 3 to form high resistance n-Cu (In 1-x The process corresponds to Ga x )SSe or Cu(In 1-y Ga y ) 3 (Se 1-x S x ) 5 . In the rapid selenium vulcanization
在储片冷却室33a中,基片3c上的硒化物前驱薄膜经过加热、溅射In2Se3/In2S3已成功转变成贫铜、大晶粒致密的光学吸收层,其基片3c的温度将由转入时的540℃~580℃逐渐降低至100℃,储片冷却室内始终充有0.5~30Pa的H2S+Ar气体,保证基片3c上光学吸收层在温度下降过程中不会挥发或逸失掉硒硫元素;随着基片3c逐渐增多,在闸板阀321关闭状态时,打开闸板阀340,利用基片推送机构332将基片3c推运至溅射沉积室34a的小车342上。In the
图5(c)是溅射沉积缓冲层与i层室34a装置的原理简图,它与图4(h)的CIGS薄膜电池吸收层上直接反应溅射金属铟锌靶制备In(OH,S)/ZnS(O,OH)/ZnO(S)缓冲层与i层的工序相对应。在溅射沉积室34a内,可控制移动距离、速度的小车343与快速硒硫化热处理室的小车323基本结构相同,放置基片3d的下面均匀布置着电阻加热装置和两对测温热电偶,由软编织导线将它与真空室外部的控制器相连接,对基片表面进行缓冲层与i层溅射时,基片温度被控制在80℃~350℃,优选100℃~180℃;在34a室中安装有二~三对中频交流或直流脉冲反应溅射金属靶343、345和346,它们分别是高纯铟和锌金属对靶,每对靶上分别安装有两套气路管线,供应工作所需的溅射与反应气体,溅射沉积区被多孔金属网罩住,单独与地线连接而不与机壳相连,其作用是屏蔽两靶之间的溅射离子,防止带电离子轰击基片3d而破坏薄膜电池pn结的构造;同样,在溅射室34a中安装有固定型高功率辐射热源344,它们也被安置在气密空间347中,气密空间347上安装有可快速开启排气或调节气压的可控阀门,以及检测气体压力的真空裸规管(未图示)。缓冲层与i层溅射完成后,进行高真空表层的快速热处理后的基片3d经由闸板阀341被取片室35a内的取片机构351收入基片承载机构(未图示)352的支架上,在取片室35a内搭载有与氢化预处理室31a的结构相同的基片可搬运的支承机构,可将相当于以批为单位的多个基片3e收纳在支承机构的水平架上,开启真空取片室35a的大门,就可用搬运叉车将整批基片3e的支承机构从真空取片室中直接运出,转入下道生产工序。Fig. 5 (c) is the schematic diagram of the principle of the sputtering deposition buffer layer and the i-
实施例1Example 1
当用纳米硒化物涂料制作CuInSe2-xSx薄膜太阳电池时,SLG基片表面分别溅射碱阻挡层和Mo背电极薄膜,在该基片表面分别实施滚涂硒化物涂料CuSe、In4Se3(或In2Se3)与CuSe各一次,本发明优选贫硒的In4Se3(熔点520℃)纳米涂料;每次滚涂涂料后立即烘干,硒化物前驱薄膜呈现CuSe/In4Se3(或In2Se3)/CuSe构造,薄膜总Cu/In>1.06,表面CuSe>底部CuSe,最佳比1.1~1.5,烘干后总厚度约4~7μm(要求最终快速硒硫化热处理后制备的吸收层厚度约0.9~1.8μm),三层硒化物薄膜的成份结构比约4∶10∶6.1,在前驱硒化物薄膜最后一次烘干前,需要均匀喷淋一定量的钠盐,它可在较低条件下辅助硒化物前驱薄膜快速硒硫化热处理时获得大晶粒致密薄膜。将烘干后的前驱硒化物薄膜的基片3a按规定片数装入到图5(a)所示的氢化预处理室内水平承载机构的支架上,关闭真空室的门。When making CuInSe 2-x S x thin-film solar cells with nano-selenide coatings, the surface of the SLG substrate is sputtered with an alkali barrier layer and a Mo back electrode film, and roll-coating CuSe and In 4 selenide coatings on the surface of the substrate. Se 3 (or In 2 Se 3 ) and CuSe each once, the present invention is preferably selenium-poor In 4 Se 3 (melting point 520°C) nano-coating; each time the coating is dried immediately after coating, the selenide precursor film presents CuSe/In 4 Se 3 (or In 2 Se 3 )/CuSe structure, total Cu/In film > 1.06, CuSe on the surface > CuSe on the bottom, the optimum ratio is 1.1-1.5, and the total thickness after drying is about 4-7 μm (requires final rapid selenium vulcanization The thickness of the absorbing layer prepared after heat treatment is about 0.9-1.8 μm), and the composition structure ratio of the three-layer selenide film is about 4:10:6.1. Before the precursor selenide film is dried for the last time, a certain amount of sodium salt needs to be evenly sprayed , it can assist the rapid selenium sulfidation heat treatment of selenide precursor film under lower conditions to obtain large-grain dense film. Put the dried precursor
本发明的前驱硒化物薄膜快速硒硫化热处理标准工艺程序为:开启氢化预处理室31a真空排气装置与其内气密空间312的阀门,同时,加热器311将气密空间内部温度从室温升至290℃,纳米前驱硒化物或电沉积前驱硒化物的优选温度范围分别是:30℃~180℃和30℃~290℃,抽至高真空1×10-3Pa以上后,关闭气密空间的阀门,注入氢气使气密空间的气压维持在30~60kPa之间,保持3~5分钟后排空,抽至高真空后重新注入氢气,循环3~5次,使纳米硒化物涂料中有机添加剂彻底脱附与挥发或氢化分解(电沉积前驱硒化物薄膜中15%~18%的氧化物被部分还原),硒化物前驱薄膜中的材料呈纯净的电子纯级,最后一次排空后注入Ar+H2气体(分别是:50~70%和30~50%),降底气密空间的气压至0.3~20Pa,并与32a室的气压平衡后打开闸板阀320,将基片3a推送至快速硒硫化热处理室32a的小车323上,关闭闸板阀320。The standard process procedure of the rapid selenium vulcanization heat treatment of the precursor selenide film of the present invention is: open the valve of the vacuum exhaust device of the hydrogenation pretreatment chamber 31a and the inner airtight space 312, and simultaneously, the heater 311 raises the internal temperature of the airtight space from room temperature To 290°C, the preferred temperature ranges of nanometer precursor selenide or electrodeposition precursor selenide are: 30°C ~ 180°C and 30°C ~ 290°C, after pumping to a high vacuum of 1×10 -3 Pa, close the airtight space Valve, inject hydrogen to maintain the air pressure in the airtight space between 30-60kPa, keep it for 3-5 minutes, then evacuate it, pump it to a high vacuum and re-inject hydrogen, cycle 3-5 times, so that the organic additives in the nano-selenide coating Desorption and volatilization or hydrogenation decomposition (15% to 18% of the oxides in the electrodeposition precursor selenide film are partially reduced), the material in the selenide precursor film is pure electronic grade, and Ar+ is injected after the last evacuation H 2 gas (respectively: 50~70% and 30~50%), lower the air pressure of the airtight space at the bottom to 0.3~20Pa, and open the gate valve 320 after the air pressure in the 32a chamber is balanced, and the substrate 3a is pushed to the On the dolly 323 of the rapid selenium sulfide heat treatment chamber 32a, close the gate valve 320.
经过氢化预处理的基片3a放置于小车323上后就改称为3b,启动小车基片3b背部加热装置,升温至350~550℃(或450~580℃为含Ga硒化物的优选),同时开启小车两侧气路的阀门,注入类H2Se气体,气密空间326内硒气氛维持在30~80kPa的气压下,小车移动后启动高功率辐射热源对基片3b进行扫描式快速硒化热处理,玻璃基片的温度控制在530~580℃,基片表面的硒化物被快速加热到550℃~1100℃,硒化物前驱薄膜被充分反应生成大晶粒致密的CIS(或CIGS)薄膜,由于硒化物前驱薄膜自身是富铜结构,快速硒化热处理后表面会吸附着多余的液相Cu2Se,关闭类H2Se气体管路阀门,打开气密空间的排气阀门,降低环境硒气压至0.5~25Pa,小车323移动至反应溅射靶的位置,小车323上的基片3b底部加热器处于恒功率控制状态。当基片3b上进行反应溅射In2Se3或In2S3中和反应掉液相Cu2Se时,监测小车323上基片3b底部多对热电偶差值的变化,由它决定反应溅射In2Se3或In2S3的单位功率或单位面积上的沉积量,以及精确控制小车323的移动速度;严格控制基片3b表面硒化物薄膜由于反应溅射沉积In2Se3或In2S3,薄膜整体成份由富铜转变成贫铜结构过程中此薄膜物理状态(测试温度)的突变,也就是铜占薄膜成份比≤24.5%时的关键变化点。小车基片3b始终维持恰当的移动速度和溅射In2Se3或In2S3合适的沉积量,就完成了整个基片3b表面均匀、完全地转变成CIGS薄膜电池的吸收层,关闭溅射电源、溅射氩气和反应气体H2Se或H2S,关闭小车323的加热器,并将它移动、退回高功率辐射热源处,开启小车两侧气路的阀门,注入类H2Se气体至30~80kPa,重新开启高功率辐射热源对基片3b表面进行更快速地扫描,小车323与高功率辐射热源装置324同时进行着相对运动,基片3b表面大晶粒CIS或CIGS的晶界与晶粒表面凸起部被重熔,降低了薄膜电池的有效晶界复合和溶解了晶体中的杂相,达到薄膜电池开路电压Voc被提高的目的。基片移动至溅射位置附近,降低气密空间的气压至0.5~25Pa,并更换溅射反应气体为H2S,启动小车加热电源、移动机构和反应溅射电源,反应溅射In2S3至基片3b表层均匀地沉积,基片3b表面生成高阻n-CuInS2或n-CuIn3(Se1-x,Sx)5,厚度大约20~40nm,此时基片3b的温度大约为480℃~550℃。开启闸板阀321,将已硒硫化处理完毕的基片3b送入储片冷却室33a的承载支架上,在0.5~30Pa的Ar+H2S气氛保护下自然冷却。After the hydrogenation pretreated
冷却到100℃以下的基片3c被输送至溅射沉积室34a的小车342上,开启小车342上的加热器与密闭空间347的排气阀门,基片3c被加热到80℃~350℃,优选100℃~180℃,气密空间被抽至高真空1×10-3Pa以上,开启各反应溅射靶上的反应气体与溅射氩气的阀门,维持气密空间在0.2~25Pa的气压,调节各靶上反应与溅射气体为恰当配比与流量,第一溅射靶位的靶材是纯金属铟,反应气体H2S+H2O,溅射产物是In(OH,S),其中包含少量的In2O3;第二、三溅射靶位的材料均是金属纯锌,反应气体分别是H2S+H2O与H2S+O2或CO2,溅射产物分别是ZnS(O,OH)与ZnO(S),二、三靶位上的反应气体H2S的流量是不同的,溅射功率也不相同;缓冲层溅射顺序为:In(OH,S)/ZnS(O,OH)/ZnO(S),它们不能被颠倒或产生其它的组合。小车基片3c接近各溅射靶位前开启溅射电源,顺序溅射薄膜电池的缓冲层与i层薄膜,其厚度分别是:15~25nm、20~30nm和50~75nm,合计约90~130nm;基片表面全部沉积完各层薄膜后,关闭小车342上的加热电源,完全打开气密空间347上的气压控制阀,抽至高真空1×10-3Pa后,开启小车的运动装置和高功率辐射热源344,对基片表面的CIS薄膜、缓冲层与i层进行闪速热处理,其热影响的区域仅占薄膜表层厚度的1~2μm,促使溅射薄膜内的吸附气体脱附、品粒间更密实和锌硫元素向CIS薄膜的表层扩散。打开闸板阀341,基片3c被取片室35a内的取片机构351收入基片承载机构352的支架上,直至基片达到一定数量后,整个承载架被取出真空室,基片转入下一操作工序。The
实施例1可以制备出两种类型薄膜太阳电池,用In2S3中和液相CuxSe的CuInSeS薄膜电池的开路电压Voc和光电转换效率相对较高。In Example 1, two types of thin film solar cells can be prepared, and the open circuit voltage Voc and photoelectric conversion efficiency of the CuInSeS thin film cell in which the liquid phase Cu x Se is neutralized with In 2 S 3 are relatively high.
实施例2Example 2
当用纳米硒化物涂料制作CuIn0.7Ga0.3Se2-xSx薄膜太阳电池时,需要四种纳米硒化物涂料,它们分别是:(CuSe+CuGaSe2)、Ga2Se3、In4Se3(或In2Se3+CuInSe2)、CuSe,分别调制它们到恰当的粘度,连续性地在基片Mo薄膜上实施滚涂与烘干,四种硒化物涂料可连续地一次性成膜,其前驱硒化物薄膜构造为:(CuSe+CuGaSe2)/Ga2Se3/In4Se3(或In2Se3+CuInSe2)/CuSe,薄膜总Cu/(In+Ga)>1.06,四层薄膜成份的原子结构比为:(4+4)∶1∶3.5∶12.1,前驱硒化物薄膜厚度约4~7μm,其中薄膜中各元素成份比Ga/(In+Ga)≥0.3、Se/M<I,表面CuSe>底部CuSe。该种CIGS薄膜电池的特点是硒化物前驱薄膜中镓元素集中在底层,贫硒的铟硒化合物相在镓硒化合物相之上,快速硒硫化热处理工艺与实施例1基本相同;基片底部预先加热后再启动高功率辐射热源,由于硒化物前驱薄膜的热传导特性和铟镓元素扩散系数的差异,底层优先生成高镓的CGS半导体薄膜,再进行铟镓元素之间的互扩散,最终CIGS薄膜中铟镓元素在厚度方向不是均匀分布,自然形成镓元素的梯度分布与薄膜电池的背电场,背电场的形成改善了薄膜电池载流子的收集与电池转换效率,再加上表层掺杂硫元素所形成的浅埋结,CIGS薄膜电池的吸收层半导体带隙呈V型分布,制造的薄膜电池与实施例1相比,大幅度提高了其性价比。When making CuIn 0.7 Ga 0.3 Se 2-x S x thin film solar cells with nano-selenide coatings, four nano-selenide coatings are required, which are: (CuSe+CuGaSe 2 ), Ga 2 Se 3 , In 4 Se 3 (or In 2 Se 3 +CuInSe 2 ), CuSe, adjust them to the appropriate viscosity respectively, roll coating and drying on the substrate Mo thin film continuously, the four kinds of selenide coatings can be continuously filmed at one time, The structure of its precursor selenide film is: (CuSe+CuGaSe 2 )/Ga 2 Se 3 /In 4 Se 3 (or In 2 Se 3 +CuInSe 2 )/CuSe, the total Cu/(In+Ga) of the film>1.06, four The atomic structure ratio of the film composition of the layer is: (4+4):1:3.5:12.1, the thickness of the precursor selenide film is about 4-7 μm, and the ratio of the elements in the film is Ga/(In+Ga)≥0.3, Se/ M<I, surface CuSe>bottom CuSe. The feature of this CIGS thin film battery is that the gallium element in the selenide precursor film is concentrated on the bottom layer, the selenium-poor indium selenide compound phase is on the gallium selenide compound phase, and the rapid selenium sulfide heat treatment process is basically the same as that of
实施例3Example 3
电化学沉积硒化物前驱薄膜制备CuInSe2-xSx薄膜太阳电池。其电沉积溶液成份的配比为:2.6mMol·L-1CuCl2·2H2O,9.6mMol·L-1InCl3和5.5mM ol·L-1H2SeO3,LiCl0.236Mol·L-1;并添加邻苯二甲酸氢钾和氨基磺酸组成的ph=3缓冲剂,测得电镀溶液的PH~2.6,采用三电极的恒电位体系,参比电极为饱和甘汞电极(SCE)。将溅射沉积了碱阻挡层与Mo背电极薄膜的SLG基片放入上述电镀溶液中,在-0.5V预先处理基片Mo背电极薄膜1分钟,基片取出后用去离子水冲洗与高纯氮气吹干,搁置一定时间后,再次放入电镀溶液中进行电沉积,先-0.2V预沉积5~8分钟Cu2-xSe,在-0.5V沉积15分钟,在-0.6V沉积45分钟,再在-0.2V沉积5~8分钟;取出的基片冲洗干净后用高纯氮气吹干,硒化物前驱物薄膜的表面呈银灰色,具有光滑、致密的外观,厚度约1.8~2.4μm,薄膜成份结构为:Cu2-xSe/CuInSe2/Cu2-xSe,Cu/In>1.06,薄膜中氧含量约15%,表层Cu2-xSe>底部Cu2-xSe,将基片放入图5的快速硒硫化热处理装置的氢化预处理室31a前喷淋一定量的钠盐,按照实施例1标准工艺程序进行,得到的基片经过集成电池的电极串联连接操作-激光划线热处理制备接触电极、溅射ZnO:Al低阻透明窗口层和激光反爆冲压分割面电极等工艺程序,就基本算得到CIS薄膜电池的集成组件,清理大面积薄膜电池的周边与焊接电极引线,就可以进行大面积组件光电转换效率的测试,进行光伏组件的封装工艺操作。Preparation of CuInSe 2-x S x thin film solar cells by electrochemical deposition of selenide precursor film. The ratio of the electrodeposition solution components is: 2.6mMol L -1 CuCl 2 2H 2 O, 9.6mMol L -1 InCl 3 and 5.5mM ol L -1 H 2 SeO 3 , LiCl0.236Mol L - 1 ; and add the ph=3 buffering agent that potassium hydrogen phthalate and sulfamic acid are formed, record the pH~2.6 of electroplating solution, adopt the constant potential system of three electrodes, reference electrode is saturated calomel electrode (SCE) . Put the SLG substrate with the alkali barrier layer and the Mo back electrode film deposited by sputtering into the above-mentioned electroplating solution, pre-treat the Mo back electrode film of the substrate at -0.5V for 1 minute, and rinse the substrate with deionized water after taking it out. Blow dry with pure nitrogen, put it into the electroplating solution again after a certain period of time for electrodeposition, first deposit Cu 2-x Se at -0.2V for 5 to 8 minutes, deposit at -0.5V for 15 minutes, deposit at -0.6V for 45 Minutes, and then deposited at -0.2V for 5 to 8 minutes; the removed substrate was rinsed and dried with high-purity nitrogen, the surface of the selenide precursor film was silver gray, with a smooth and dense appearance, and the thickness was about 1.8 to 2.4 μm, the composition structure of the film is: Cu 2-x Se/CuInSe 2 /Cu 2-x Se, Cu/In>1.06, the oxygen content in the film is about 15%, Cu 2-x Se on the surface>Cu 2-x Se on the bottom, Spray a certain amount of sodium salt before putting the substrate into the hydrogenation pretreatment chamber 31a of the rapid selenium sulfidation heat treatment device in Figure 5, and proceed according to the standard process procedure of Example 1, and the obtained substrate is connected in series through the electrodes of the integrated battery- Laser scribing heat treatment to prepare contact electrodes, sputtering ZnO:Al low-resistance transparent window layer, and laser anti-explosion stamping split surface electrodes and other processes can basically be calculated as integrated components of CIS thin-film batteries, cleaning the periphery and welding of large-area thin-film batteries Electrode leads can be used to test the photoelectric conversion efficiency of large-area modules and perform packaging process operations of photovoltaic modules.
实施例4Example 4
电化学沉积硒化物前驱薄膜制备CuInGaSe2-xSx薄膜太阳电池,其中前驱硒化物薄膜仅是依赖于沉积电位控制薄膜中的成份与半导体带隙呈V型,薄膜是一步法获得富Cu硒化物前驱薄膜。其电沉积溶液成份的配比为:2.0mMol·L-1CuCl2,10.0mMol·L-1InCl3、15.0mM ol·L-1GaCl3和5.0mM ol·L-1H2SeO3,0.236Mol·L-1LiCl,添加邻苯二甲酸氢钾和氨基磺酸ph=3缓冲剂,测得电解槽中溶液的PH~2.6,采用三电极的恒电位体系,参比电极为饱和甘汞电极(SCE)。将基片先浸入专用预处理电解槽液中,在-0.5V预先处理基片上背电极Mo薄膜1分钟,Mo与溶液中CuxSe发生化学置换反应,并沉积较薄一层CuxSe,取出后用去离子水冲洗与高纯氮气吹干,搁置一定时间后,再次放入专用电解槽液中进行电沉积;先-0.2V电位预沉积5~8分钟(Cu2-xSe+CuGaSe2),在-0.75V电位沉积25分钟获得高镓[Cu2-xSe+Cu(In0.5,Ga0.5)Se2],在-0.5V电位沉积35分钟,再在-0.2V电位沉积5分钟和-0.8V电位沉积3分钟,硒化物前驱薄膜在底层和表面均为高镓含量,由于含镓硒化物均是高熔点固相物,薄膜内Ga元素的扩散相对较困难,决定了它在硒化物前驱薄膜的重熔再结晶过程中起着框架作用;控制沉积电位的一次性电沉积基片取出后冲洗干净,用高纯氮气吹干并放置烘箱中烘干,该电沉积薄膜表面呈现光滑、致密的银灰色外观,厚度约1.8~2.4μm,薄膜成份的层状结构分布为:(Cu2-xSe+CuGaSe2)/[Cu(In0.5,Ga0.5)Se2]/Cu(In0.8Ga0.2)Se2/(Cu2-xSe+CuGaSe2)/CuIn0.4Ga0.6Se,薄膜中Cu/(In+Ga)>1.06,Se/M<1,总成份CuSe+CuIn0.7Ga0.3Se2,其中表层CuSe>底部CuSe,表面层Ga元素<底部Ga元素,薄膜中氧含量约15~17%;按照实施例1的标准工艺程序进行,就可得到致密大晶粒、带隙呈V型分布的优质CIGS薄膜太阳电池。Electrochemical deposition of selenide precursor film to prepare CuInGaSe 2-x S x thin film solar cells, in which the precursor selenide film is only dependent on the deposition potential to control the composition of the film and the semiconductor band gap is V-shaped, and the film is a one-step method to obtain Cu-Se rich selenium compound precursor film. The composition ratio of the electrodeposition solution is: 2.0mMol·L -1 CuCl 2 , 10.0mMol·L -1 InCl 3 , 15.0mM ol·L -1 GaCl 3 and 5.0mM ol·L -1 H 2 SeO 3 , 0.236Mol L -1 LiCl, adding potassium hydrogen phthalate and sulfamic acid ph = 3 buffer, the pH of the solution in the electrolytic cell was measured to be 2.6, using a three-electrode constant potential system, and the reference electrode was saturated glycerin Mercury electrode (SCE). The substrate is first immersed in the special pretreatment electrolytic bath, and the Mo film on the back electrode on the substrate is pretreated at -0.5V for 1 minute. The chemical replacement reaction between Mo and Cux Se in the solution occurs, and a thin layer of Cux Se is deposited. After taking it out, rinse it with deionized water and blow it dry with high-purity nitrogen gas. After standing for a certain period of time, put it into the special electrolytic bath again for electrodeposition; 2 ) Deposit at -0.75V potential for 25 minutes to obtain high gallium [Cu 2-x Se+Cu(In 0.5 , Ga 0.5 )Se 2 ], deposit at -0.5V potential for 35 minutes, and then deposit 5 at -0.2V potential Minutes and -0.8V potential deposition for 3 minutes, the selenide precursor film has high gallium content on the bottom layer and the surface, because gallium selenide is a high melting point solid phase, the diffusion of Ga element in the film is relatively difficult, which determines its It plays a framework role in the remelting and recrystallization process of the selenide precursor film; the disposable electrodeposition substrate that controls the deposition potential is taken out, rinsed, blown dry with high-purity nitrogen and placed in an oven to dry, the surface of the electrodeposition film It presents a smooth and dense silver-gray appearance, with a thickness of about 1.8-2.4 μm. The layered structure distribution of the film composition is: (Cu 2-x Se+CuGaSe 2 )/[Cu(In 0.5 , Ga 0.5 )Se 2 ]/Cu (In 0.8 Ga 0.2 )Se 2 /(Cu 2-x Se+CuGaSe 2 )/CuIn 0.4 Ga 0.6 Se, Cu/(In+Ga)>1.06 in the film, Se/M<1, total composition CuSe+CuIn 0.7 Ga 0.3 Se 2 , where surface layer CuSe>bottom CuSe, surface layer Ga element<bottom Ga element, the oxygen content in the film is about 15-17%; according to the standard process procedure of Example 1, dense large grains, banded High-quality CIGS thin-film solar cells with V-shaped gap distribution.
实施例5Example 5
电化学沉积硒化物前驱薄膜制备双面可透光型CuInGaSe2-xSx薄膜太阳电池。选用商用ITO玻璃衬底进行硒化物前驱薄膜的电沉积。沉积前ITO玻璃在异丙醇中超声清洗10min和进行激光划线分割透明导电膜的操作,选用硫酸盐电化学沉积体系,参比电极为饱和硫酸汞电极(MSE相对标准氢电极的电位为+650mV),在80℃、无搅拌、高纯氮气除氧的水溶液中恒电位电沉积Ga2Se3和CuIn0.7Ga0.3Se2。先在ITO上电沉积0.2~0.3μm厚的Ga2Se3,沉积电位为-1.1V(相对于饱和甘汞电极MSE),溶液组成为:1mM的SeO2,1mM的Ga2(SO4)3和0.3MK2SO4,pH值用硫酸调到2.4。再沉积CIGS,沉积工艺:溶液配比:0.3MK2SO4(pH2.4,H2SO4调节),1.0mMCuSO4,3.0mMIn2(SO4)3、3.0mMGa2(SO4)3和1.7mMSeO2;沉积电位为-0.9V,薄膜厚度约1.8~2.4,薄膜中Cu/(In+Ga)>1.06,Se/M<1,表层Cu2-xSe>底部Cu2-xSe,表层Ga元素<底部Ga元素。按照实施例1标准快速硒硫化热处理工艺程序进行,得到的基片经过集成电池的电极连接操作-激光划线热处理制备接触电极、溅射ZnO:Al低阻透明窗口层、激光反爆冲压分割电极和电极引线与封装等工艺操作程序,就得到了特殊用途CIS薄膜电池集成组件的玻璃发电幕墙部件,其正面透射阳光发电,反面接受散射的红外光,可叠加双面吸收的光能发电。Double-sided transparent CuInGaSe 2-x S x thin film solar cells prepared by electrochemical deposition of selenide precursor film. A commercial ITO glass substrate was chosen for the electrodeposition of the selenide precursor thin film. Before deposition, the ITO glass was ultrasonically cleaned in isopropanol for 10 minutes and laser scribing was performed to divide the transparent conductive film. The sulfate electrochemical deposition system was selected, and the reference electrode was a saturated mercury sulfate electrode (the potential of MSE relative to the standard hydrogen electrode was + 650mV), constant potential electrodeposition of Ga 2 Se 3 and CuIn 0.7 Ga 0.3 Se 2 in an aqueous solution of high-purity nitrogen deoxygenated at 80°C without stirring. Electrodeposit 0.2-0.3μm thick Ga 2 Se 3 on ITO first, the deposition potential is -1.1V (relative to saturated calomel electrode MSE), the solution composition is: 1mM SeO 2 , 1mM Ga 2 (SO 4 ) 3 and 0.3M K 2 SO 4 , the pH was adjusted to 2.4 with sulfuric acid. Re-deposition CIGS, deposition process: solution ratio: 0.3MK 2 SO 4 (pH2.4, adjusted by H 2 SO 4 ), 1.0mMCuSO 4 , 3.0mMIn 2 (SO 4 ) 3 , 3.0mMGa 2 (SO 4 ) 3 and 1.7mMSeO 2 ; deposition potential is -0.9V, film thickness is about 1.8-2.4, Cu/(In+Ga)>1.06 in the film, Se/M<1, Cu 2-x Se on the surface>Cu 2-x Se on the bottom, Surface layer Ga element < bottom Ga element. According to the standard rapid selenium sulfide heat treatment process procedure of Example 1, the obtained substrate undergoes the electrode connection operation of the integrated battery-laser scribing heat treatment to prepare contact electrodes, sputtering ZnO:Al low-resistance transparent window layer, laser detonation stamping split electrodes And electrode lead wire and encapsulation and other process operation procedures, the glass power generation curtain wall component of the special-purpose CIS thin film battery integrated module is obtained. The front side transmits sunlight to generate power, and the back side receives scattered infrared light, which can superimpose the light energy absorbed on both sides to generate power.
实施例6Example 6
本实施例是纳米硒化物涂料制作CuIn0.7Ga0.3Se2-xSx薄膜太阳电池中的优选方案。它与实施例2的方法基本相同,也需要四种纳米硒化物涂料,在基片Mo电极薄膜上实施滚涂与烘干,可分步连续性地一次性成膜,四种硒化物涂料分别是:CuSe+CuGaSe2、Ga2Se3、In4Se3(或In2Se3+CuInSe2)、(CuSe+CuGaSe2);其前驱薄膜构造为:(CuSe+CuGaSe2)/Ga2Se3/In4Se3/(CuSe+CuGaSe2),薄膜总的Cu/(In+Ga)>1.06,四层薄膜成份中原子结构比为:(4+3)∶1∶3.5∶(12.1+1),前驱硒化物薄膜厚度约4~7μm,其中薄膜中各主要元素成份比Ga/(In+Ga)≥0.3、Se/M<1,表层CuSe>底部CuSe,表层Ga元素<底部Ga元素。其快速硒硫化热处理工艺与实施例2相同,薄膜电池的开路电压Voc比实施例2的少高,薄膜电池的半导体带隙呈V型分布。This example is a preferred scheme for making CuIn 0.7 Ga 0.3 Se 2-x S x thin film solar cells with nano-selenide coating. It is basically the same as the method of Example 2, and four kinds of nano-selenide coatings are also needed. Roll coating and drying are implemented on the substrate Mo electrode film, which can be film-formed step by step and continuously. The four kinds of selenide coatings are respectively It is: CuSe+CuGaSe 2 , Ga 2 Se 3 , In 4 Se 3 (or In 2 Se 3 +CuInSe 2 ), (CuSe+CuGaSe 2 ); the precursor film structure is: (CuSe+CuGaSe 2 )/Ga 2 Se 3 /In 4 Se 3 /(CuSe+CuGaSe 2 ), the total Cu/(In+Ga) of the film>1.06, the atomic structure ratio in the four-layer film composition is: (4+3):1:3.5:(12.1+ 1), the thickness of the precursor selenide film is about 4-7 μm, in which the ratio of the main elements in the film is Ga/(In+Ga)≥0.3, Se/M<1, surface layer CuSe>bottom CuSe, surface layer Ga element<bottom Ga element . The rapid selenium sulfidation heat treatment process is the same as that of Example 2, the open circuit voltage Voc of the thin film battery is slightly higher than that of Example 2, and the semiconductor band gap of the thin film battery is in a V-shaped distribution.
实施例7Example 7
三步电沉积(Cu2-xSe+CuGaSe2)/In4Se3/Cu2-xSe硒化物前驱薄膜制备CuInGaSe2-xSx薄膜太阳电池,电沉积采用标准的三电极体系,阳电极用石墨纤维布、参比电极用Ag/AgCl电极,采用可循环流动电解槽结构,电解液使用循环泵供给并形成环流。第一步沉积的溶液配比:0.3MK2SO4,1.0mMCuSO4,5.0mMGa2(SO4)3和1.7mMSeO2,H2SO4调节pH=2.2±0.2;沉积由恒电位过程控制,相对于Ag/AgCl电极的沉积电位为-0.75~-1.0V,可调节[Cu]/[Ga]的比例为富Cu或贫Cu;第二步沉积的溶液配比:1mM的SeO2,1mM的In2(SO4)3、0.3MK2SO4和适当有机添加剂,pH值用硫酸调到2.2,沉积贫硒的In4Se3依赖于溶液中ppm量的添加剂来控制;第三步更换电沉积溶液,进行Cu2-xSe的电沉积。硒化物前驱薄膜Cu/(In+Ga)>1.06,Se/M≤1,Ga/(Ga+In)=0.3~0.36,表层Cu2-xSe>底部Cu2-xSe,表层Ga元素<底部Ga元素,薄膜中氧含量约15%以上。按照实施例1标准工艺程序进行硒化物前驱薄膜的快速硒硫化热处理,再进行后续其它沉积工艺与操作,就可得到与实施例2相似的CIGS薄膜太阳电池,如果第三步电沉积过程添加Ga2(SO4)3,就可得到实施例6的薄膜电池。Three-step electrodeposition (Cu 2-x Se+CuGaSe 2 )/In 4 Se 3 /Cu 2-x Se selenide precursor film to prepare CuInGaSe 2-x S x thin film solar cell, electrodeposition adopts standard three-electrode system, anode Graphite fiber cloth is used for the electrode, and Ag/AgCl electrode is used for the reference electrode. The structure of the electrolytic cell can be circulated. The electrolyte is supplied by a circulation pump and forms a circulation. The solution ratio of the first step of deposition: 0.3MK 2 SO 4 , 1.0mMCuSO 4 , 5.0mMGa 2 (SO 4 ) 3 and 1.7mMSeO 2 , H 2 SO 4 to adjust the pH=2.2±0.2; the deposition is controlled by the constant potential process, The deposition potential relative to the Ag/AgCl electrode is -0.75~-1.0V, and the ratio of [Cu]/[Ga] can be adjusted to be Cu-rich or Cu-poor; the solution ratio of the second deposition step: 1mM SeO 2 , 1mM In 2 (SO 4 ) 3 , 0.3MK 2 SO 4 and appropriate organic additives, the pH value is adjusted to 2.2 with sulfuric acid, and the deposition of selenium-poor In 4 Se 3 is controlled by the additive in the ppm amount in the solution; the third step is to replace Electrodeposition solution for electrodeposition of Cu 2-x Se. Selenide precursor thin film Cu/(In+Ga)>1.06, Se/M≤1, Ga/(Ga+In)=0.3~0.36, surface layer Cu 2-x Se>bottom Cu 2-x Se, surface layer Ga element< The Ga element at the bottom, the oxygen content in the film is about 15% or more. Carry out the rapid selenium sulfide heat treatment of the selenide precursor thin film according to the standard process procedure of
实施例8Example 8
前面所述前驱硒化物薄膜的电池基片均是水平放置进行快速硒硫化热处理与溅射沉积等相关操作的,依据本发明核心技术的范围,也可以设计与制作立式放置基片的设备,分别将图4光伏组件生产工序主流程与图5直列式快速硒硫化热处理装置中基片直立操作,其它设备做出与此相对应的调整,它并没有超出本发明核心技术的范围。The battery substrates of the aforementioned precursor selenide thin films are all placed horizontally for rapid selenium sulfide heat treatment and sputtering deposition. According to the scope of the core technology of the present invention, it is also possible to design and manufacture equipment for vertical placement of substrates. The main flow of the photovoltaic module production process in Figure 4 and the upright operation of the substrate in the in-line rapid selenium vulcanization heat treatment device in Figure 5 are respectively adjusted, and other equipment is adjusted accordingly, which does not exceed the scope of the core technology of the present invention.
这样,第一氢化预处理室内的基片均呈直立式放置,氢化预处理室每次可推入二片硒化物前驱薄膜基片进入第二快速硒硫化处理室,第二室小车上的基片架也呈直立式放置,基片架的中间安置加热器,可烘烤外部两侧的基片,并布置多对热电偶,同时可测量两侧基片上多点的温度值,比水平放置的工作效率更高和节省能源;基片架小车的两侧分别对称安置两个可移动的高功率辐射热源,它们可同时开启与移动;可移动辐射热源旁安置两个对称放置的高纯金属铟反应溅射对靶装置,它们按照面向小车基片架的对称位置立式安装;与此相对应各室的闸板阀开启的门将更宽,一次有两片基片同时进出,取、送片机构要对两张基片进行着同时操作。同理,第三基片冷却室、第四溅射室和第五取片室全部与第一、第二室作相应的变动,内部从水平工作状态变更为垂直状态;其中,第四溅射室中需添置近一倍装置,共有四至六对金属反应溅射对靶,它们呈现对称与竖向安置,一对高功率辐射热源也呈对称与垂直状态,对基片呈现横向移动式扫描。其操作程序与工艺与实施例1的硒化物前驱薄膜快速硒硫化热处理标准工艺基本相同,其工作效率比水平放置基片装置的作业方式高一倍,更适合于大基片或超大基片薄膜电池光伏组件的制造。Like this, the substrates in the first hydrogenation pretreatment chamber are placed upright, and the hydrogenation pretreatment chamber can push two selenide precursor film substrates into the second fast selenium sulfide treatment chamber at a time, and the substrates on the trolley in the second chamber The film rack is also placed vertically, and a heater is placed in the middle of the substrate rack, which can bake the substrates on both sides of the outside, and arrange multiple pairs of thermocouples. At the same time, it can measure the temperature values of multiple points on the substrates on both sides. The work efficiency is higher and energy saving; two movable high-power radiation heat sources are symmetrically placed on both sides of the substrate rack trolley, and they can be turned on and moved at the same time; two symmetrically placed high-purity metal heat sources are placed next to the movable radiation heat source Indium reactive sputtering target device, they are vertically installed in a symmetrical position facing the trolley substrate rack; correspondingly, the gate valves of each chamber will open wider, and two substrates can enter and exit at the same time, taking and sending The chip mechanism is to operate the two substrates simultaneously. Similarly, the third substrate cooling chamber, the fourth sputtering chamber and the fifth taking-up chamber are all changed correspondingly to the first and second chambers, and the interior is changed from a horizontal working state to a vertical state; wherein, the fourth sputtering chamber Nearly double the device needs to be installed in the chamber, and there are four to six pairs of metal reactive sputtering targets, which are arranged symmetrically and vertically, and a pair of high-power radiation heat sources are also symmetrically and vertically positioned to scan the substrate in a lateral movement manner. Its operating procedures and processes are basically the same as the standard process for rapid selenium vulcanization heat treatment of selenide precursor films in Example 1, and its work efficiency is twice as high as that of the horizontally placed substrate device, and is more suitable for large substrates or super large substrate films Manufacture of cell photovoltaic modules.
工业上的可利用性Industrial availability
本发明适用于由纳米硒化物涂料滚涂或水浴电化学沉积制备硒化物前驱薄膜,通过对硒化物前驱薄膜的快速硒硫化热处理,可以直接、连续化地制备CIGS薄膜电池光学吸收层、缓冲层与i层,再通过后续的单体电池电极串联连接的方式(内联式集成组件),就可作为光电转换效率高的大面积光伏组件而被利用,用于光伏电站或建筑一体化的并网发电。The invention is applicable to the preparation of selenide precursor films by rolling coating of nano-selenide coatings or water bath electrochemical deposition, and can directly and continuously prepare the optical absorption layer and buffer layer of CIGS thin film batteries through the rapid selenium vulcanization heat treatment of the selenide precursor films It can be used as a large-area photovoltaic module with high photoelectric conversion efficiency by connecting the subsequent single cell electrodes in series (inline integrated module), which is used for photovoltaic power plants or building integration. grid power generation.
尽管本发明参照优选实施方案和说明书附图以及实施例进行了详细地说明,对本领域的技术人员来说,本发明的各种用途和变形可以不偏离本发明的实质与范围而完成。因此,可以认为在此详细的说明书和附图不是对本发明范围的限定,它可以从前面的权利要求书中推导出来,并且它们在法律上是等效的。Although the present invention has been described in detail with reference to the preferred embodiment and the accompanying drawings and examples, those skilled in the art can make various uses and modifications of the present invention without departing from the spirit and scope of the present invention. Accordingly, it should be considered that the detailed description and drawings herein are not limitations on the scope of the invention, which can be derived from the preceding claims, which are legally equivalent.
附图标记说明Explanation of reference signs
参考文献references
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