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TW201132499A - Highly adhesive polyester film for solar sell - Google Patents

Highly adhesive polyester film for solar sell Download PDF

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Publication number
TW201132499A
TW201132499A TW099141617A TW99141617A TW201132499A TW 201132499 A TW201132499 A TW 201132499A TW 099141617 A TW099141617 A TW 099141617A TW 99141617 A TW99141617 A TW 99141617A TW 201132499 A TW201132499 A TW 201132499A
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TW
Taiwan
Prior art keywords
mass
polyester film
film
solar cell
coating layer
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Application number
TW099141617A
Other languages
Chinese (zh)
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TWI409171B (en
Inventor
Koji Itoh
Hiroko Yabuki
Kenichi Mori
Original Assignee
Toyo Boseki
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Publication of TW201132499A publication Critical patent/TW201132499A/en
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Publication of TWI409171B publication Critical patent/TWI409171B/en

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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J7/00Chemical treatment or coating of shaped articles made of macromolecular substances
    • C08J7/04Coating
    • C08J7/043Improving the adhesiveness of the coatings per se, e.g. forming primers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40High-molecular-weight compounds
    • C08G18/42Polycondensates having carboxylic or carbonic ester groups in the main chain
    • C08G18/44Polycarbonates
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/36Layered products comprising a layer of synthetic resin comprising polyesters
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J7/00Chemical treatment or coating of shaped articles made of macromolecular substances
    • C08J7/04Coating
    • C08J7/0427Coating with only one layer of a composition containing a polymer binder
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J7/00Chemical treatment or coating of shaped articles made of macromolecular substances
    • C08J7/04Coating
    • C08J7/048Forming gas barrier coatings
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D175/00Coating compositions based on polyureas or polyurethanes; Coating compositions based on derivatives of such polymers
    • C09D175/04Polyurethanes
    • C09D175/06Polyurethanes from polyesters
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J7/00Adhesives in the form of films or foils
    • C09J7/20Adhesives in the form of films or foils characterised by their carriers
    • C09J7/22Plastics; Metallised plastics
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J7/00Adhesives in the form of films or foils
    • C09J7/20Adhesives in the form of films or foils characterised by their carriers
    • C09J7/22Plastics; Metallised plastics
    • C09J7/25Plastics; Metallised plastics based on macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds
    • C09J7/255Polyesters
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J7/00Adhesives in the form of films or foils
    • C09J7/20Adhesives in the form of films or foils characterised by their carriers
    • C09J7/29Laminated material
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J7/00Adhesives in the form of films or foils
    • C09J7/30Adhesives in the form of films or foils characterised by the adhesive composition
    • C09J7/35Heat-activated
    • HELECTRICITY
    • H02GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
    • H02SGENERATION OF ELECTRIC POWER BY CONVERSION OF INFRARED RADIATION, VISIBLE LIGHT OR ULTRAVIOLET LIGHT, e.g. USING PHOTOVOLTAIC [PV] MODULES
    • H02S10/00PV power plants; Combinations of PV energy systems with other systems for the generation of electric power
    • H02S10/30Thermophotovoltaic systems
    • HELECTRICITY
    • H10SEMICONDUCTOR DEVICES; ELECTRIC SOLID-STATE DEVICES NOT OTHERWISE PROVIDED FOR
    • H10FINORGANIC SEMICONDUCTOR DEVICES SENSITIVE TO INFRARED RADIATION, LIGHT, ELECTROMAGNETIC RADIATION OF SHORTER WAVELENGTH OR CORPUSCULAR RADIATION
    • H10F19/00Integrated devices, or assemblies of multiple devices, comprising at least one photovoltaic cell covered by group H10F10/00, e.g. photovoltaic modules
    • H10F19/80Encapsulations or containers for integrated devices, or assemblies of multiple devices, having photovoltaic cells
    • H10F19/85Protective back sheets
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2367/00Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2475/00Characterised by the use of polyureas or polyurethanes; Derivatives of such polymers
    • C08J2475/04Polyurethanes
    • C08J2475/08Polyurethanes from polyethers
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J2203/00Applications of adhesives in processes or use of adhesives in the form of films or foils
    • C09J2203/322Applications of adhesives in processes or use of adhesives in the form of films or foils for the production of solar panels
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J2467/00Presence of polyester
    • C09J2467/006Presence of polyester in the substrate
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J2475/00Presence of polyurethane
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E10/00Energy generation through renewable energy sources
    • Y02E10/50Photovoltaic [PV] energy

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Wood Science & Technology (AREA)
  • Laminated Bodies (AREA)
  • Photovoltaic Devices (AREA)

Abstract

The present invention provides a highly adhesive polyester film for solar cell with excellent adhesive and a back sheet using the same. A polyester film with a substrate thickness of 20 to 500 μ m having a coating layer on at least one surface is provided with a coating layer having a main component of urethane resin consisted of aliphatic polycarbonate polyol; in which an absorbance ratio (an absorbance closed to 1460 cm<SP>-1</SP> from aliphatic polycarbonate component/ an absorbance closed to 1530 cm<SP>-1</SP> from urethane component) measured by infrared spectroscopy is 0.70 to 1.60.

Description

201132499 六、發明說明: 【發明所屬之技術領域】 本發明是關於一種太陽能電池用易接著性聚酯薄膜。 更詳而言,一種即使在高溫高濕下與封止劑之接著爲優異 之聚酯薄膜。 【先前技術】 近年來,太陽能電池是作爲可取代造成地球溫暖化之 原因的石油能源之能量方法而受到注目。太陽能電池是一 種可將太陽光之能量直接加以轉換成電之太陽光發電系統 。太陽能電池元件是使用單晶矽、多晶矽、非晶矽等之半 導體、或化合物系、或有機物系色素等。一般而言,太陽 能電池元件是將數片至數十片配線成串聯 '並聯,且爲長 期(約20年以上)保護元件而採取各種構裝措施。組配於 該構裝之單元是稱爲「太陽能電池模組」。 一般而言’太陽能電池模組是製成以玻璃覆蓋將曝露 於太陽光之面、以封止材塡埋太陽能電池元件、且將背面 用被稱爲背板的由耐熱、耐候性塑膠材料等之許多層結構 所構成之保護片加以保護而成之構成。用於塡充太陽能電 池元件之封止材是使用乙烯•醋酸乙烯酯共聚物樹脂(在 下文中,則稱爲「EVA」)或聚乙烯醇縮丁醛樹脂(在下 文中,則稱爲「PVB」)等之烯烴系樹脂。藉由以上述玻 璃基板/封止材/太陽能電池元件/封止材/背板之構成重疊 起來而以真空積層機等加以熱壓接合,即可製得模組。封 201132499 止材是具有可將太陽能電池元件加以接著固 來自外部的濕氣侵入,以保護太陽能電池元 太陽能電池用背板是已有提案揭示從太 側(封止材側)依序爲聚酯薄膜/接著劑/聚 )/金屬、或金屬氧化物系薄膜層(防濕層) 膜(防污層)等之_層構成。背板是具有避 濕氣或污染而可長期保護太陽能電池元件之 與封止材直接接觸的太陽能電池元件側之聚 材間之接著性是重要。然而,未經施加表面 膜是無法獲得充分的接著性,因此一直被要 提案一種設置含有樹脂或交聯劑之接著層作 膜的接著性之方法(專利文獻1至4 )。 先前技術文獻 發明專利文獻 專利文獻1 日本特開第2006-152013號公 專利文獻2 日本特開第2006-332091號公 專利文獻3 曰本特開第2007-48944號公幸丨 專利文獻4 日本特開第2007-136911號公 【發明內容】 〔所欲解決之技術問題〕 在屋外嚴格環境條件下使用之太陽能電 待能獲得2 0年以上之長耐用期限化。因此, 件的封止材易接著薄膜方面,不僅只是初期 定,同時防止 ί牛之作用。 陽能電池元件 醋薄膜(著色 /接著劑/氟薄 免來自外部之 作用。因此, 酯薄膜與封止 處理之聚酯薄 求改善。已有 爲改善聚酯薄 報 報 y 報 池模組是被期 在被用作爲構 接著性,也需 -4- 201132499 要在高溫高濕下之長期間保持接著性。然而,如揭示於上 述發明專利文獻般之太陽能電池用易接著性聚酯薄膜,其 接著性卻不充分,特別是在高溫高濕下之長期使用中的接 著強度之降低則一向是無法避免者。 再者,從提高生產性或防止劣化的觀點,則對封止材 已演進到被使用含有交聯劑、紫外線吸收劑等添加劑之各 種組成物種。因此,對各種封止材也要求可顯現同等程度 的接著性之高泛用性易接著性薄膜。 本發明是有鑑於上述技術問題,提供一種具有在嚴格 的環境下也能耐受的強度之接著性、且幾乎不致於導致先 前被認爲無法避免的在高溫高濕下接著性降低、對各種封 止材也具有良好的接著性之太陽能電池用易接著性聚酯薄 膜。 〔解決問題之技術方法〕 本發明之發明人等爲解決上述技術問題而經專心硏討 結果發現:至少在單面具有塗布層之聚酯薄膜,且在塗布 層是含有以脂肪族系聚碳酸酯多元醇作爲構成成分之胺基 甲酸酯樹脂,特別是以脂肪族系聚碳酸酯多元醇作爲構成 成分之胺基甲酸酯樹脂爲主成分時,在紅外線光譜法光譜 中’源於脂肪族系聚碳酸酯成分之1 460 cm·1附近之吸光度 (A146Q)與源於胺基甲酸酯成分之1 5 3 0 附近之吸光 度(A153())的比率(A146〇/A153〇)爲0.70至1.60之塗布層 ’藉此則可顯現在嚴格的環境下也能耐受的強度之接著性201132499 VI. Description of the Invention: [Technical Field] The present invention relates to an easily adhesive polyester film for a solar cell. More specifically, it is a polyester film which is excellent in adhesion to a sealing agent even under high temperature and high humidity. [Prior Art] In recent years, solar cells have attracted attention as an energy method that can replace petroleum energy that causes global warming. A solar cell is a solar power system that converts the energy of sunlight directly into electricity. The solar cell element is a semiconductor such as a single crystal germanium, a polycrystalline germanium or an amorphous germanium, or a compound system or an organic dye. In general, solar cell components are manufactured by connecting several to several tens of wires in series 'parallel, and for long-term (about 20 years or more) protection components. The unit assembled in this configuration is called a "solar battery module". In general, a solar cell module is made of a glass-covered surface that is exposed to sunlight, a solar cell element is embedded in a sealing material, and a back surface is made of a heat-resistant and weather-resistant plastic material. A protective sheet composed of a plurality of layer structures is protected by a protective sheet. The sealing material for charging the solar cell element is an ethylene vinyl acetate copolymer resin (hereinafter referred to as "EVA") or a polyvinyl butyral resin (hereinafter, referred to as "PVB"). Or an olefin resin. The module can be obtained by laminating the above-mentioned glass substrate/sealing material/solar cell element/sealing material/backing plate with a vacuum laminator or the like by thermocompression bonding. Seal 201132499 is a polyester with a solar cell element that can be subsequently solidified from the outside to protect the solar cell. The solar cell backsheet has been proposed to be polyester from the side (sealing material side). Film/adhesive/poly)/metal, or metal oxide-based film layer (moisture-proof layer) film (anti-fouling layer) or the like. It is important that the back sheet is a laminate between the materials on the side of the solar cell element which is in direct contact with the sealing material to protect the solar cell element from moisture or contamination. However, since sufficient adhesion cannot be obtained without applying a surface film, a method of providing an adhesive layer containing a resin or a crosslinking agent as a film has been proposed (Patent Documents 1 to 4). PRIOR ART DOCUMENT PATENT DOCUMENT PATENT DOCUMENT PATENT DOCUMENT PATENT DOCUMENT PATENT DOCUMENT PATENT DOCUMENT PATENT DOCUMENT PATENT DOCUMENT PATENT DOCUMENT PATENT DOCUMENT PATENT DOCUMENT PRIOR ART [2007] No. 2007-136911 [Content of the invention] [Technical problems to be solved] The solar power equipment used under strict environmental conditions outside the house can be obtained for a long period of durability of more than 20 years. Therefore, the sealing material of the piece is easy to follow the film, not only the initial setting, but also the role of the 牛. The vinegar film of the solar cell component (coloring/adhesive/fluorine thin is free from the external effect. Therefore, the polyester film and the sealing treatment of the polyester are thinner and improved. There has been an improvement of the polyester thin report. In order to be used as a build-up property, it is necessary to maintain the adhesion during the long period of high temperature and high humidity. However, as disclosed in the above-mentioned invention patent document, the easy-adhesive polyester film for solar cells, The adhesiveness is not sufficient, especially in the long-term use under high temperature and high humidity, the decrease in the strength of the adhesive is always unavoidable. Furthermore, from the viewpoint of improving productivity or preventing deterioration, the sealing material has evolved. Various types of constituents containing an additive such as a crosslinking agent or an ultraviolet absorber are used. Therefore, a highly versatile easy-adhesive film which exhibits an equivalent degree of adhesion to various sealing materials is also required. The technical problem is to provide a bond with strength that can withstand in a strict environment, and hardly cause it to be previously considered to be unavoidable under high temperature and high humidity. [Easy method for solving the problem] The invention of the present invention has been found to solve the above-mentioned technical problems and has been found to be focused on the problem. : a polyester film having a coating layer on at least one side, and the coating layer is a urethane resin containing an aliphatic polycarbonate polyol as a constituent component, particularly an aliphatic polycarbonate polyol When the urethane resin as a constituent component is a main component, the absorbance (A146Q) derived from the aliphatic polycarbonate component in the vicinity of 1 460 cm·1 in the infrared spectroscopy spectrum is derived from the urethane. The ratio of the absorbance (A153()) in the vicinity of 1 5 3 0 of the ester component (A146〇/A153〇) is a coating layer of 0.70 to 1.60, whereby the strength which can be tolerated under a strict environment can be exhibited. Sex

S.S -5- 201132499 ,且在高溫高濕下也可顯現優異的接著性而終於達成 明。 此外,若塗布層是以脂肪族系聚碳酸酯多元醇作 成成分之胺基甲酸酯樹脂與交聯劑爲主成分時,在紅 光譜法光譜中,源於脂肪族系聚碳酸酯成分之1460 附近之吸光度(A146Q )與源於胺基甲酸酯成分之1530 附近之吸光度(A153Q )的比率(A146Q/A153Q )爲0.50至 ,藉此則也可對各種封止材顯現在高溫高濕下爲優異 著性而終於達成本發明。 前述技術問題是可藉由下列解決方法而獲得解決 (1) 一種太陽能電.池用易接著性聚酯薄膜,其係 在單面具有塗布層之基材厚度爲20至500 jam之聚酯 ,且該塗布層是含有以脂肪族系聚碳酸酯多元醇作爲 成分之胺基甲酸酯樹脂。 (2 )如前述之太陽能電池用易接著性聚酯薄膜, 該塗布層是以脂肪族系聚碳酸酯多元醇作爲構成成分 基甲酸酯樹脂爲主成分,且在該塗布層之紅外線光譜 譜中,源於脂肪族系聚碳酸酯成分之1 460 cnT1附近之 度(A1460)與源於胺基甲酸酯成分之1530 cm — 1附近 光度(Ai53G)的比率(Αι46〇/Αι53。)爲 0_70 至 1.60。 (3)如前述之太陽能電池用易接著性聚酯薄膜, 該塗布層是以脂肪族系聚碳酸酯多元醇作爲構成成分 基甲酸酯樹脂與交聯劑爲主成分,且在該塗布層之紅 本發 爲構 外線 cm'1 cm'1 1.55 的接 〇 至少 薄膜 構成 其中 之胺 法光 吸光 之吸 其中 之胺 外線 201132499 光譜法光譜中,源於脂肪族系聚碳酸酯成分之1460 附近之吸光度(A146Q)與源於胺基甲酸酯成分之153〇 附近之吸光度(Ai53G)的比率(Ai46〇/Ai53G)爲〇.50至 〇 (4) 如前述之太陽能電池用易接著性聚酯薄膜, 該交聯劑是選自三聚氰胺系交聯劑、異氰酸酯系交聯 碳化二亞胺系交聯劑、曙唑啉系交聯劑中之至少一種 劑。 (5) 如前述之太陽能電池用易接著性聚酯薄膜, 在該塗布層中之該交聯劑的含量相對於胺基甲酸酯樹 5質量%以上且90質量%以下。 (6) 如前述之太陽能電池用易接著性聚酯薄膜, 該聚酯薄膜爲白色聚酯薄膜。 (7) —種太陽能電池用背板,其係積層前述之太 電池用易接著性聚酯薄膜而成。 〔發明之功效〕 本發明之太陽能電池用易接著性聚酯薄膜是顯現 的接著性,特別是在高溫高濕下之接著性(耐濕熱性 優異。因此,較佳的實施形態是在上述高溫、高濕環 之接著性可維持與最初同等之接著性。此外,本發明 佳的實施形態是將本發明之太陽能電池用易接著性聚 膜用作爲背板之構件時,則與封止材之接著性爲良好 cm cm·1 1.55 其中 劑、 交聯 其中 脂爲 其中 陽能 強固 )爲 境下 之較 酯薄 201132499 【實施方式】 〔實施發明之形態〕 (聚酯薄膜) 在本發明用於構成基材之聚酯樹脂是可使用:聚對苯 二甲酸乙二醇酯、聚對苯二甲酸丁二醇酯、聚2,6-萘二甲 酸乙二醇酯、聚對苯二甲酸亞甲酯,及將例如二甘醇、新 戊二醇、聚伸烷基二醇等之二醇成分,或己二酸、癸二酸 、鄰苯二甲酸、間苯二甲酸、2,6-萘二甲酸等之二羧酸成 分等作爲共聚合成分而加以共聚合而成之聚酯樹脂等。 在本發明適合使用之聚酯樹脂是主要以將聚對苯二甲 酸乙二醇酯、聚對苯二甲酸丙二醇酯、聚對苯二甲酸丁二 醇酯、聚萘二甲酸乙二醇酯中至少一種作爲構成成分。在 此等聚酯樹脂中,從物性與成本之均衡的觀點,則最佳爲 聚對苯二甲酸乙二醇酯。此外,此等聚酯薄膜經加以雙軸 向延伸即可提高耐藥品性、耐熱性、機械性強度等。 此外,本發明之聚酯薄膜可爲單層之聚酯薄膜,也可 爲具有最外層與中心層之至少由三層所構成之聚酯薄膜。 在本發明中,若係製成三層構成時,可在最外層(在 上述兩種三層時,則爲A層)含有粒子,在中心層(在上 述兩種三層時,則爲B層)則可實質地未含有粒子。以在 A層含有粒子爲較佳的理由是因將本發明之聚酯薄膜用作 爲太陽能電池用之構件時,則可提高在進行積層金屬、或 金屬氧化物系薄膜層或塗布層等之防濕功能層、防污功能 201132499 層等後續加工步驟中的操作使用性。若將粒子添加在最外 層時,則可獲得適合於加工性之充分的操作使用性。 此外,以在B層實質地未含有粒子爲較佳的理由是可 減少滑劑粒子,特別是無機粒子之凝集體而引起的突起之 形成機率。此外,藉由採取此構成,則可獲得高透明性之 薄膜,對於透光型(see-through type)太陽能電池等要求 透明性的領域也是適合。 另外,所謂的「實質地未含有惰性粒子」是意謂例如 在無機粒子的情況,藉由螢光X-射線分析將源於粒子的元 素加以定量分析時,則可獲得少於50 ppm,較佳爲少於1 〇 PPm,最佳爲偵測限界以下之含量。其係因爲即使未積極地 添加粒子,但是有可能由於源於外來異物之污染成分、或 原料樹脂或在薄膜製造步驟中所附著於生產線或裝置之污 垢剝離而混入於薄膜中的情況。 對此等各層因應需要可在聚酯中含有各種添加劑。添 加劑是包括:例如抗氧化劑、耐光劑、抗凝膠化劑、有機 濕潤劑、抗靜電劑、紫外線吸收劑、界面活性劑等。 包含在最外層的粒子之種類及含量是並無特殊限制, 可爲無機粒子或有機粒子。例如可例示二氧化矽、二氧化 駄、滑石、高嶺石等之金屬氧化物、碳酸鈣、磷酸鈣、硫 酸鋇等之對聚酯爲惰性之無機粒子。此等惰性無機粒子是 可任一種單獨使用或兩種以上併用。 201132499 前述粒子之平均粒徑較佳爲o.l至3.5&quot;m。該平均粒 徑之下限較佳爲0.5^m,更佳爲〇.8/zm,進一步更佳爲 1.0/zm。此外’該平均粒子之上限更佳爲3〇/zm,進一步 更佳爲2.8Mm。若平均粒徑爲小於〇.1/irn時,則無法獲 得充分的操作使用性。若超過3.5/zm時,則容易形成粗大 突起。 此外’此等之粒子較佳爲多孔質粒子,特別是較佳爲 多孔質二氧化矽。多孔質粒子由於在薄膜製膜步驟進行延 伸時容易變型成扁平型,且透明性之降低爲小,因此爲較 佳。 最外層之無機粒子的含量相對於構成最外層的聚酯較 佳爲〇.〇1至0_20質量%。該濃度之下限更佳爲0·02質量% ,進一步更佳爲0.03質量%。並且,該濃度之上限更佳爲 0,15質量%,進一步更佳爲〇.1〇質量%。若少於0.01質量 %時,則無法獲得充分的操作使用性。若超過〇·2質量%時 ,則透明性降低,因此爲不佳。 前述粒子的平均粒徑之測定是可以下列方法測定。 以電子顯微鏡或光學顯微鏡攝影粒子之照片’以最小 的粒子一個之大小成爲2至5 mm之倍率來測定300至500 個粒子之最大徑(若爲多孔質二氧化矽的情況’則爲凝集 體之粒徑),以其平均値作爲平均粒徑。此外’如欲測定 積層薄膜的被覆層中之粒子平均粒徑時’則使用透射型電 子顯微鏡(TEM ),以12萬倍之倍率攝影積層薄膜之截面 ,即可測定粒子之最大徑。 -10- 201132499 對聚酯混合上述粒子之方法是可採用習知的方法。例 如可在製造聚酯之任意階段進行添加,但是較佳爲在酯化 階段,或在酯交換反應結束後、聚縮合反應開始前之階段 作成爲分散於乙二醇等之漿體而添加來進行聚縮合反應。 此外,也可使用配備有排氣孔之捏合擠壓機來摻合經分散 於乙二醇或水等而成的粒子之漿體與聚酯原料之方法、或 使用捏合擠壓機來摻合經乾燥的粒子與聚酯原料之方法等 而進行。 從提高太陽能電池之光電轉換效率的觀點,本發明之 薄膜較佳爲使用白色聚酯薄膜作爲聚酯薄膜,以使其也可 利用反射光。爲有效地顯現光反射性,則白色聚酯薄膜之 L値較佳爲85.0至100、a値爲-10.0至+10.0、b値爲-10.0 至+1〇.〇。若爲該範圍時,則可提高光之反射率,因此爲較 佳。 從如上述之對基材之聚酯薄膜賦予白色性或隱蔽性、 提高光反射性的觀點,則較佳爲在基材含有白色顏料及/或 無機粒子。 在白色聚酯薄膜所使用的白色顏料是可使用氧化鈦、 硫酸鋇、氧化鋅、硫化鋅、碳酸鈣等。此外,爲提高分散 性等之目的,則可對該白色顏料施加各種有機、無機表面 處理。特別是在白色顔料中,由於氧化鈦具有高折射率, 以少量即可顯現高白色性,因此爲較佳。若進一步倂用螢 光增白劑時,則可更進一步提高白色性而爲較佳。 -11 - 201132499 在白色聚酯薄膜中之白色顔料的含量,從光反射性的 觀點,則下限較佳爲5質量%,特佳爲8質量%。此外,該 白色顏料之含量’從製膜穩定性的觀點,則上限較佳爲3〇 質量°/β ’更佳爲2 5質量%,特佳爲2 〇質量%。 此外’爲更進一步提高白色度,在基材中除了白色顏 料以外而倂用螢光增白劑時’若白色顔料爲超過3〇質量% 時’由於白色顔料之紫外線吸收量增加,螢光增白劑爲發 揮功效所必要的紫外線則減少而會顯著地阻礙螢光增白功 效,使得白色度降低,因此爲不佳。 此外,爲對白色聚酯薄膜賦予其他功能,因應需要而 可在基材中含有平均粒徑爲小於白色顏料的無機粒子、耐 熱性有機粒子、抗氧化劑、交聯劑、紫外線吸收劑、塑化 劑等。 此外,使得白色聚酯薄膜含有白色顏料與平均粒徑大 於該白色顏料的至少一種無機粒子也爲較佳。無機粒子是 包括:氧化鈦、硫酸鋇、氧化鋅、硫化鋅、碳酸鈣等之白 色顏料,或爲如二氧化矽等之與聚酯的折射率差爲小的無 機粒子。此外,在使用兩種平均粒徑不同的白色顏料時, 則該白色顏料可爲同種或不同種。總結而言,從光反射性 與操作使用性的觀點,則較佳的模式是使用平均粒徑不同 的兩種無機粒子,且平均粒徑小的無機粒子爲白色顏料。 從成本或操作使用性的觀點,則平均粒徑大的無機粒子較 佳爲二氧化砂。 -12- 201132499 重要的是從在後加工之外觀性的觀點,則在白 薄膜中所含有的無機粒子之平均粒徑的上限値爲5. 較佳爲3.〇vm,特佳爲2.〇Mm。此外,從薄膜製造 在後加工步驟中之滑性的觀點,則在該基材薄膜中 的無機粒子之平均粒徑的下限値較佳爲0.5 m,特ΐ μ. m。 白色聚酯薄膜是可爲單層或多層。例如,假設 述白色顏料及/或無機粒子之層爲A層、其他層爲I 層時,則可選擇 A/B/A、 A/B/C、 C/A/B/A、 C/A/B/A/C 等之層構成。特別是具有B/A/B層之兩種三層構成 可使B層未含有粒子,或爲更進一步提高光反射性 A層相同的方式含有白色顏料、無機粒子或耐熱性 子等。此外,爲更進一步提高白色性,則也可在不 礙本發明之功效範圍使B層含有螢光增白劑。 而且,白色聚酯薄膜較佳爲經使其含有對聚酯 非相溶於該聚酯樹脂之熱塑性樹脂作爲空洞形成劑 至少朝一方向加以延伸而形成空洞所獲得含有空洞 〇 本發明之作爲基材的聚酯薄膜之厚度爲20至 ,更佳爲25至450//m,進一步更佳爲30至300( 基材厚度爲薄時,則熱收縮之影響爲大,有可能會 高溫高濕處理後之接著性降低的情況。若爲厚時, 加以捲取成爲捲筒。 色聚酯 0仁m, 步驟及 所含有 I 爲 0.7 含有上 ;層、C ' C/A/B 時,則 而以與 有機粒 致於阻 樹脂與 ,其次 之薄膜 5 0 0 // m 么m 0若 導致經 則無法 -13- 201132499 (塗布層) 本發明之太陽能電池用易接著性聚酯薄膜的特徵爲含 有以脂肪族系聚碳酸酯多元醇作爲構成成分之胺基甲酸酯 樹脂。 特別是在塗布層是以脂肪族系聚碳酸酯多元醇作爲構 成成分之胺基甲酸酯樹脂爲主成分時,重要的是在使用紅 外線光譜法之測定中,源於脂肪族系聚碳酸酯成分之146〇 cm·1附近之吸光度(A146())與源於胺基甲酸酯成分之1530 cm·1附近之吸光度(Ai5SQ)的比率(Ai46〇/Ai53Q)爲〇·7〇 至1.60。此外,在塗布層是以脂肪族系聚碳酸酯多元醇作 爲構成成分之胺基甲酸酯樹脂與交聯劑爲主成分時’重要 的是在紅外線光譜法光譜中’源於脂肪族系聚碳酸酯成分 之1460 cm·1附近之吸光度(A146C)與源於胺基甲酸酯成 分之1530 〇111-1附近之吸光度(八153。)的比率(八146()/人1530 )爲0.50至1.55。在此所謂「主成分」是意謂在塗布層中 所包含的總固體成份中含有50質量%以上’更佳爲70質 量%以上。 如在上述專利文獻1至4中所揭示,根據先前的技術 常識一直認爲從提高塗布層之耐久性的觀點’較佳爲在形 成塗布層時積極地導入交聯結構以製成剛性且強硬的塗布 層。然而,本發明卻發現經將以脂肪族系聚碳酸酯多元醇 作爲構成成分之聚胺基甲酸酯樹脂加以控制爲使用紅外線 光譜法的吸光度爲一定範圍,即可顯現強固的接著性、且 -14- 201132499 提高在高溫高濕熱下之接著性之顯著功效而終於達成本發 明。何以藉由如此之構成即可提高接著性之機制並不清楚 ,但是本發明之發明者的觀點如下。 例如,進行模組之構裝時,則在以經積層具有玻璃基 板/封止材/塗布層之聚酯薄膜(塗布層)之構成下,在高 溫下進行熱壓接合。此時,由於高溫接著時之聚酯薄膜的 熱收縮而會在聚酯薄膜(塗布層)與封止材之間產生應力 。特別是此等應力之產生也會由於各種封止材之種類•接 著條件而變化。其結果,一直被認爲該應力是無法完全加 以緩和而導致與封止材之接著性降低。並且,將如此的積 層體放置在高溫高濕下時,則塗布層會由於發生水解而劣 化。其結果,一直認爲無法完全耐受該應力而使得封止材 剝離,以致在高溫高濕下之接著性降低。因此,爲高度地 保持與封止材之強固的密著性或在高溫高濕下之接著性, 並非僅藉由將塗布層強固地加以交聯而賦予耐久性,而較 佳爲應以保持耐熱、耐水解性之成分且具備能耐受該應力 之柔軟性來對應。然而,只具有柔軟性時,則在塗膜強度 上會有問題。因此,最佳爲使得此等相反特性兩者並存。 在本發明中,塗布層是以脂肪族系聚碳酸酯多元醇作 爲構成成分之胺基甲酸酯樹脂爲主成分,且藉由設定以紅 外線光譜法所測得源於脂肪族系聚碳酸酯成分之1 460 cnT1附近之吸光度(A146Q )與源於胺基甲酸酯成分之1530 CO! 1附近之吸光度(Ai53Q)的比率(Ai46〇/Ai53Q)爲〇·70S.S -5-201132499, and excellent adhesion under high temperature and high humidity, finally arrived. In addition, when the coating layer is a urethane resin containing a fatty polycarbonate polyol as a component and a crosslinking agent as a main component, in the red spectrum spectrum, it is derived from an aliphatic polycarbonate component. The ratio of the absorbance (A146Q) in the vicinity of 1460 to the absorbance (A153Q) near the 1530 derived from the urethane component (A146Q/A153Q) is 0.50, whereby various sealing materials can be exhibited in high temperature and high humidity. The present invention has finally been achieved with excellent performance. The foregoing technical problem can be solved by the following solutions. (1) An easy-to-adherent polyester film for solar energy, which is a polyester having a coating layer having a coating thickness of 20 to 500 mm on one side. Further, the coating layer is a urethane resin containing an aliphatic polycarbonate polyol as a component. (2) The above-mentioned easy-adhesive polyester film for a solar cell, which is characterized in that an aliphatic polycarbonate polyol is used as a constituent component of a urethane resin as a main component, and an infrared spectrum spectrum of the coating layer is used. The ratio of the vicinity of 1 460 cnT1 (A1460) derived from the aliphatic polycarbonate component to the luminosity (Ai53G) derived from the urethane component of 1530 cm -1 (Αι46〇/Αι53.) is 0_70 to 1.60. (3) The above-mentioned easy-adhesive polyester film for a solar cell, wherein the coating layer is based on an aliphatic polycarbonate polyol as a constituent component of a urethane resin and a crosslinking agent, and is in the coating layer The red hair is made of the outer line cm'1 cm'1 1.55. At least the film constitutes the amine-based light-absorbing light. The amine outside line 201132499 is obtained from the spectral spectrum of the aliphatic polycarbonate component. The ratio of the absorbance (A146Q) to the absorbance (Ai53G) near the 153〇 derived from the urethane component (Ai46〇/Ai53G) is 〇.50 to 〇(4). The ester film is at least one selected from the group consisting of a melamine-based crosslinking agent, an isocyanate-based crosslinked carbodiimide-based crosslinking agent, and an oxazoline-based crosslinking agent. (5) The content of the crosslinking agent in the coating layer in the coating layer is 5 mass% or more and 90 mass% or less with respect to the urethane tree. (6) The above-mentioned easy-adhesive polyester film for a solar cell, which is a white polyester film. (7) A back sheet for a solar cell, which is formed by laminating an easy-contact polyester film for a battery as described above. [Effects of the Invention] The easy-adhesive polyester film for a solar cell of the present invention exhibits adhesion, particularly in high-temperature and high-humidity (excellent heat and humidity resistance). Therefore, a preferred embodiment is at the above-mentioned high temperature. In addition, in the preferred embodiment of the present invention, when the easy-adhesive poly film for a solar cell of the present invention is used as a member of a back sheet, the sealing material is used as a backing material. The adhesiveness is good, cm cm·1 1.55, and the cross-linking grease is a relatively thin ester in which the yang energy is strong. 201132499 [Embodiment] [Form of the invention] (Polyester film) Used in the present invention The polyester resin constituting the substrate can be used: polyethylene terephthalate, polybutylene terephthalate, polyethylene-2,6-naphthalate, polyterephthalic acid Methylene ester, and a diol component such as diethylene glycol, neopentyl glycol, polyalkylene glycol, or adipic acid, sebacic acid, phthalic acid, isophthalic acid, 2,6 Copolymerization of a dicarboxylic acid component such as naphthalene dicarboxylic acid A polyester resin or the like which is obtained by copolymerization. The polyester resin suitable for use in the present invention is mainly composed of polyethylene terephthalate, polytrimethylene terephthalate, polybutylene terephthalate, polyethylene naphthalate. At least one is a constituent. Among these polyester resins, polyethylene terephthalate is preferred from the viewpoint of balance between physical properties and cost. Further, these polyester films can be subjected to biaxial stretching to improve chemical resistance, heat resistance, mechanical strength and the like. Further, the polyester film of the present invention may be a single layer of a polyester film or a polyester film having at least three layers of an outermost layer and a center layer. In the present invention, when the three-layer structure is used, particles may be contained in the outermost layer (in the case of the above two layers, the layer A), and in the center layer (in the case of the above two layers, B) The layer) may be substantially free of particles. In the case where the polyester film of the present invention is used as a member for a solar cell, it is preferable to prevent the deposition of a laminated metal, a metal oxide film layer or a coating layer. Operational use in subsequent processing steps such as wet functional layer and antifouling function 201132499. When particles are added to the outermost layer, sufficient workability suitable for workability can be obtained. Further, the reason why the particles are substantially not contained in the layer B is preferable because the formation of protrusions due to the agglomeration of the lubricant particles, particularly the inorganic particles, can be reduced. Further, by adopting such a configuration, a film having high transparency can be obtained, and it is also suitable for a field requiring transparency such as a see-through type solar cell. In addition, the phrase "substantially does not contain inert particles" means that, for example, in the case of inorganic particles, when the elements derived from the particles are quantitatively analyzed by fluorescent X-ray analysis, less than 50 ppm can be obtained. Preferably, it is less than 1 〇 PPm, and the best is below the detection limit. This is because even if the particles are not actively added, there is a possibility that the contaminated component derived from the foreign matter or the raw material resin or the stain adhered to the production line or the device in the film production step is peeled off and mixed into the film. These layers may contain various additives in the polyester as needed. The additive includes, for example, an antioxidant, a light stabilizer, an antigelling agent, an organic wetting agent, an antistatic agent, an ultraviolet absorber, a surfactant, and the like. The type and content of the particles contained in the outermost layer are not particularly limited, and may be inorganic particles or organic particles. For example, metal oxides such as cerium oxide, cerium oxide, talc, and kaolinite, inorganic particles such as calcium carbonate, calcium phosphate, and barium sulfate which are inert to the polyester can be exemplified. These inert inorganic particles may be used singly or in combination of two or more. 201132499 The average particle diameter of the aforementioned particles is preferably from 0.1 to 3.5 &quot; m. The lower limit of the average particle diameter is preferably 0.5 μm, more preferably 〇.8/zm, still more preferably 1.0/zm. Further, the upper limit of the average particle is more preferably 3 Å/zm, still more preferably 2.8 Mm. If the average particle diameter is less than 〇.1/irn, sufficient workability cannot be obtained. When it exceeds 3.5/zm, it is easy to form coarse protrusions. Further, such particles are preferably porous particles, and particularly preferably porous ceria. The porous particles are preferably deformed into a flat type when stretched in the film forming step, and the transparency is reduced to be small, which is preferable. The content of the outermost inorganic particles is preferably from 〇1 to 0_20% by mass based on the polyester constituting the outermost layer. The lower limit of the concentration is more preferably 0. 02% by mass, still more preferably 0.03% by mass. Further, the upper limit of the concentration is more preferably 0,15% by mass, still more preferably 〇.1% by mass. If it is less than 0.01% by mass, sufficient workability cannot be obtained. When it exceeds 〇·2 mass%, transparency will fall, and it is unpreferable. The measurement of the average particle diameter of the above particles can be measured by the following method. Photographing particles by electron microscopy or optical microscopy to determine the maximum diameter of 300 to 500 particles in the case of a minimum particle size of 2 to 5 mm (in the case of porous ceria) The particle size) is based on the average enthalpy as the average particle diameter. Further, when the average particle diameter of the particles in the coating layer of the laminated film is to be measured, the maximum diameter of the particles can be measured by using a transmission electron microscope (TEM) to photograph the cross section of the laminated film at a magnification of 120,000 times. -10- 201132499 A method of mixing the above particles with polyester can be carried out by a conventional method. For example, it may be added at any stage of the production of the polyester, but it is preferably added in the esterification stage or after the end of the transesterification reaction or before the start of the polycondensation reaction to be dispersed in a slurry of ethylene glycol or the like. A polycondensation reaction is carried out. Further, a kneading extruder equipped with a vent hole may be used to blend a slurry of particles dispersed in ethylene glycol or water with a polyester raw material, or a kneading extruder may be used for blending. The dried particles and the method of the polyester raw material are carried out. From the viewpoint of improving the photoelectric conversion efficiency of the solar cell, the film of the present invention preferably uses a white polyester film as the polyester film so that it can also utilize reflected light. In order to effectively exhibit light reflectivity, the white polyester film preferably has an L値 of 85.0 to 100, a値 of -10.0 to +10.0, and b値 of -10.0 to +1 〇. If it is in this range, the reflectance of light can be increased, so that it is preferable. From the viewpoint of imparting whiteness or concealability to the polyester film of the substrate as described above and improving light reflectivity, it is preferred to contain a white pigment and/or inorganic particles on the substrate. As the white pigment used for the white polyester film, titanium oxide, barium sulfate, zinc oxide, zinc sulfide, calcium carbonate or the like can be used. Further, various organic and inorganic surface treatments can be applied to the white pigment for the purpose of improving dispersibility and the like. In particular, in the white pigment, since titanium oxide has a high refractive index and high whiteness in a small amount, it is preferable. When the fluorescent whitening agent is further used, whiteness can be further improved, which is preferable. -11 - 201132499 The content of the white pigment in the white polyester film is preferably from 5% by mass, particularly preferably from 8% by mass, from the viewpoint of light reflectivity. Further, from the viewpoint of film formation stability, the upper limit of the content of the white pigment is preferably 3 〇 mass ° / β ', more preferably 25 mass%, and particularly preferably 2 mass%. In addition, in order to further improve the whiteness, when the fluorescent whitening agent is used in addition to the white pigment in the substrate, 'if the white pigment is more than 3% by mass, the amount of ultraviolet light absorbed by the white pigment increases, and the fluorescence increases. The ultraviolet light which is necessary for the whitening agent to be effective is reduced, and the fluorescent whitening effect is remarkably hindered, so that the whiteness is lowered, and thus it is not preferable. In addition, in order to impart other functions to the white polyester film, inorganic particles having an average particle diameter smaller than that of the white pigment, heat-resistant organic particles, an antioxidant, a crosslinking agent, an ultraviolet absorber, and plasticization may be contained in the substrate as needed. Agents, etc. Further, it is also preferred that the white polyester film contains a white pigment and at least one inorganic particle having an average particle diameter larger than the white pigment. The inorganic particles are white pigments including titanium oxide, barium sulfate, zinc oxide, zinc sulfide, calcium carbonate, or the like, or inorganic particles having a small refractive index difference from polyester such as cerium oxide. Further, when two white pigments having different average particle diameters are used, the white pigments may be the same or different species. In summary, from the viewpoint of light reflectivity and workability, a preferred mode is to use two kinds of inorganic particles having different average particle diameters, and the inorganic particles having a small average particle diameter are white pigments. From the viewpoint of cost or workability, the inorganic particles having a large average particle diameter are preferably sand dioxide. -12- 201132499 It is important that the upper limit 平均 of the average particle diameter of the inorganic particles contained in the white film is 5. From the viewpoint of the appearance of the post-processing, it is preferably 3. 〇vm, particularly preferably 2. 〇Mm. Further, from the viewpoint of the slipperiness of the film production in the post-processing step, the lower limit 平均 of the average particle diameter of the inorganic particles in the base film is preferably 0.5 m, particularly μ.m. The white polyester film can be a single layer or a plurality of layers. For example, if the layer of white pigment and/or inorganic particles is layer A and the other layer is layer I, then A/B/A, A/B/C, C/A/B/A, C/A can be selected. /B/A/C and other layers. In particular, the three-layered structure having the B/A/B layer can be such that the layer B does not contain particles or further enhances light reflectivity. The layer A contains white pigments, inorganic particles, heat-resistant members, and the like. Further, in order to further improve the whiteness, the layer B may contain a fluorescent whitening agent without impairing the efficacy of the present invention. Further, the white polyester film is preferably obtained by containing a thermoplastic resin which is incompatible with the polyester resin as a void forming agent and extending at least in one direction to form voids. The polyester film has a thickness of 20 to more preferably 25 to 450 / / m, and more preferably 30 to 300 (when the thickness of the substrate is thin, the effect of heat shrinkage is large, and high temperature and high humidity treatment may be possible. When the thickness is reduced, it is wound into a roll. The color polyester 0 is m, the step and the contained I are 0.7, and the layer, C ' C/A/B, then The resin is compatible with the organic particles, and the film 5 0 0 // m m 0 is not able to pass through -13 - 201132499 (coating layer) The easy-adhesive polyester film for solar cells of the present invention is characterized by A urethane resin containing an aliphatic polycarbonate polyol as a constituent component. In particular, when the coating layer is a urethane resin containing an aliphatic polycarbonate polyol as a constituent component as a main component It is important to use infrared light In the measurement of the method, the ratio of the absorbance (A146()) in the vicinity of 146 〇cm·1 derived from the aliphatic polycarbonate component to the absorbance (Ai5SQ) in the vicinity of 1530 cm·1 derived from the urethane component (Ai46〇/Ai53Q) is 〇·7〇 to 1.60. In addition, when the coating layer is a urethane resin containing a fatty polycarbonate polyol as a constituent component and a crosslinking agent as a main component, it is important. In the infrared spectroscopy spectrum, the absorbance (A146C) from the vicinity of 1460 cm·1 of the aliphatic polycarbonate component and the absorbance near the 1530 〇111-1 derived from the urethane component (eight 153). The ratio (eight 146 () / person 1530) is from 0.50 to 1.55. The term "principal component" as used herein means that the total solid content contained in the coating layer is 50% by mass or more and more preferably 70% by mass. As disclosed in the above-mentioned Patent Documents 1 to 4, it has been considered from the prior art that it is preferable to positively introduce a crosslinked structure to form rigidity when forming a coating layer from the viewpoint of improving the durability of the coating layer. And a tough coating layer. However, the present invention finds that The aliphatic polycarbonate polyol as a constituent component of the polyurethane resin is controlled so that the absorbance by infrared spectroscopy is within a certain range, and the strong adhesion can be exhibited, and the high temperature and high heat of the heat can be improved. The present invention has finally been achieved with the remarkable effect of the following. The mechanism by which the adhesion can be improved by such a configuration is not clear, but the inventors of the present invention have the following points. For example, when the module is assembled, Then, thermocompression bonding is performed at a high temperature under a configuration in which a polyester film (coating layer) having a glass substrate/sealing material/coating layer is laminated. At this time, stress is generated between the polyester film (coating layer) and the sealing material due to heat shrinkage of the polyester film at the time of high temperature. In particular, the generation of such stresses may also vary depending on the type of sealing material and the conditions of the various sealing materials. As a result, it has been considered that the stress cannot be completely alleviated and the adhesion to the sealing material is lowered. Further, when such a laminate is placed under high temperature and high humidity, the coating layer is deteriorated by hydrolysis. As a result, it has been considered that the stress cannot be completely withstood and the sealing material is peeled off, so that the adhesion under high temperature and high humidity is lowered. Therefore, in order to maintain the strong adhesion to the sealing material or the adhesion under high temperature and high humidity, the durability is not merely imparted by strongly crosslinking the coating layer, but it is preferable to maintain A component that is resistant to heat and hydrolysis, and has a softness that can withstand the stress. However, when it is only flexible, there is a problem in the strength of the coating film. Therefore, it is optimal to make both of these opposite characteristics coexist. In the present invention, the coating layer is mainly composed of a urethane resin having an aliphatic polycarbonate polyol as a constituent component, and is derived from an aliphatic polycarbonate as measured by infrared spectroscopy. The ratio of the absorbance (A146Q) near the composition of 460 cnT1 to the absorbance (Ai53Q) near the 1530 CO! 1 of the urethane component (Ai46〇/Ai53Q) is 〇·70

S -15- 201132499 至1.60,藉此則可使得上述特性兩者並存。亦即,以特定 的比例使得具有耐水解性之脂肪族聚碳酸酯成分、與可顯 現強硬性之胺基甲酸酯成分共存而圖謀上述特性兩者並存 。藉此,由於可緩和在高溫下進行熱接著時聚酯薄膜之熱 收縮所產生的應力,而可獲得與封止材之強固的接著性, 且由於在其後之高溫高濕環境下也可保持耐熱、耐水解性 ,因此可防止塗布層劣化。 其中,1460 cnT1附近之吸光度(A146D)是源於在脂肪 族系聚碳酸酯成分中所含有的亞甲基之C-H鍵特有之變形 振動(deformation vibration)。因此,1460 cm·1 附近之 吸光度(A146Q )大小是依存於塗布層之用於構成胺基甲酸 酯樹脂之脂肪族系聚碳酸酯多元醇成分之數量。在另一方 面,1530 (^1^1附近之吸光度(A153{))是源於在胺基甲酸酯 成分中所含有的N-H鍵特有之變形振動。因此,1530 cm·1 附近之吸光度(A153C&gt;)大小是依存於塗布層之用於構成胺 基甲酸酯樹脂的胺基甲酸酯成分之數量。因此,此等之吸 光度比率(A146Q/A153Q)是表示將各自具有不同特性之兩 成分以特定的比例而共存者。在本發明中,如前所述比率 (Ai46〇/A153。)爲 0.70 至 1.60,但是該比率(Ai46〇/Ai530 )之下限較佳爲0.75,更佳爲0.80。此外,該比率(A146〇/A15 30 )之上限較佳爲1.50,更佳爲1.45,進一步更佳爲1.40。 若該比率(Ai46〇/Ai530)爲少於〇.7〇時,則強硬的胺基甲 酸酯成分變得太多而使得塗布層之應力緩和降低,因此耐 -16- 55 201132499 濕熱性會降低。此外,若該比率(A146()/AI53Q)爲超過1· 時,則柔軟的脂肪族系聚碳酸酯之脂肪族成分增加過多 使得塗布層之強度降低,因此塗膜強度或耐濕熱性會降 〇 本發明是藉由如上所述模式,即可顯現與封止材之 烈的接著性,因此可提高在高溫高濕下之接著性(耐濕 性)。在下文中,將詳細地說明本發明之構成。 更進一步,若塗布層是以脂肪族系聚碳酸酯多元醇 爲構成成分之胺基甲酸酯樹脂與交聯劑爲主成分時,則 由設定在紅外線光譜法光譜中源於脂肪族系聚碳酸酯成 之1 460 cnT1附近之吸光度(A146Q)與源於胺基甲酸酯 分之1530 (^_1附近之吸光度(八153〇)的比率(人146()/八1 )爲0.50至1.55,藉此則可使得上述特性兩者並存,再 ,也可達成對於各種封止材可廣泛適用的泛用性。 在封止材方面,從提高生產性或防止劣化的觀點, 前已演進到使用含有交聯劑、紫外線吸收劑等添加劑之 種組成物種。例如,在屬於標準固化型之封止材是採用 熱壓接合(例如在90至13CTC歷時5至10分鐘)之暫 壓接後進行熱處理(例如在140至160 °C歷時30至50 鐘),以使得封止材緩慢地硬化之接著條件。在另一方 ,在屬於快速固化型封止材則採用以短時間進行熱壓接 (例如在1 4 0至1 6 0 °C歷時1 5至2 0分鐘)以使得封止 快速地硬化之接著條件。因此,不僅是要求對各種封止 而 低 強 熱 作 藉 分 成 5 3 0 者 巨 各 經 時 分 面 合 材 材 -17- 201132499 也會顯現同等程度之接著性的泛用性,也要求對各種接著 條件也能對應的高泛用性之易接著性薄膜。在另一方面, 在進行熱壓接合時,伴隨薄膜之熱收縮所產生的應力也會 由於各種封止材之種類•接著條件而變化。特別是對需要 長時間的高溫度之標準固化型而言,伴隨熱收縮所產生的 應力變化將會增大。其結果,在適用各種封止材時,則有 由於該應力無法完全加以緩和而導致與封止材之接著性降 低的情況。特別是在如快速固化型般以短時間進行高溫熱 壓接合時,局部性地熔融於塗布層之封止材將會侵蝕,特 別是會使得與經高溫高濕處理後的薄膜基材之接著性降低 。因此,較佳爲以交聯劑使得塗布層之交聯結構更強固, 同時使得此等相反的特性兩者並存。 在本發明中,塗布層是以脂肪族系聚碳酸酯多元醇作 爲構成成分之胺基甲酸酯樹脂與交聯劑爲主成分,且藉由 設定以紅外線光譜法所測得源於脂肪族系聚碳酸酯成分之 1 460 cnT1附近之吸光度(A146Q)與源於胺基甲酸酯成分之 1 5 3 0 CHT1附近之吸光度(A153Q)的比率(A146Q/A153Q)爲 0.50至1.55,藉此則可使得上述特性兩者並存。雖然該比 率(Ai46〇/A_i53Q)爲 〇·50 至 1.55’ 但是該比率(Ai46〇/Ai530 )之下限較佳爲0.60,更佳爲0.70。此外,該比率(Ai46〇/A153〇 )之上限較佳爲1.45,更佳爲1.35,進一步更佳爲1.25。 藉此,由於可將在高溫進行熱接著時,由於薄膜之熱收縮 所產生的應力可加以緩和,即使爲各種封止材•接著條件 -18- 201132499 也可獲得強固的接著性,且在其後之高溫高濕環境下 保持耐熱、耐水解性,因此其可防止塗布層之劣化。 該較佳的比率範圍會由於交聯劑而改變的理由是由於 劑的交聯點增加所導致。 (胺基甲酸酯樹脂) 本發明之胺基甲酸酯樹脂是至少含有多元醇成分 異氰酸酯成分作爲構成成分,並且因應需要而可含有 增長劑。本發明之胺基甲酸酯樹脂是此等構成成分主 胺基甲酸酯鍵所共聚合而成之高分子化合物。在本發 以具有脂肪族系聚碳酸酯多元醇作爲胺基甲酸酯樹脂 成成分爲其特徵。經將以脂肪族系聚碳酸酯多元醇作 成成分之胺基甲酸酯樹脂包含在本發明之塗布層,即 高耐濕熱性。另外,此等胺基甲酸酯樹脂之構成成分 由核磁共振分析等即可加以確認。 在本發明之作爲胺基甲酸酯樹脂之構成成分之二 分是需要使其含有耐熱、耐水解性優異之脂肪族系聚 酯多元醇。從本發明之防止由於太陽光而造成黃變的 ,則較佳爲使用脂肪族系聚碳酸醋多元醇。 「脂肪族系聚碳酸酯多元醇」是包括:脂肪族系 酸酯二醇、脂肪族系聚碳酸酯三醇等,但是適合使用 族系聚碳酸酯二醇。本發明之作爲胺基甲酸酯樹脂之 成分的脂肪族系聚碳酸酯二醇是包括:例如藉由使乙 '丙二醇 ' 1,3-丙二醇、1,4-丁 二醇、1,5-戊二醇、3- 也可 何以 交聯 、聚 鏈段 要以 明是 之構 爲構 可提 是藉 醇成 碳酸 觀點 聚碳 脂肪 構成 二醇 甲基 -19- 201132499 -1,5-戊二醇、1,6-己二醇、1,9-壬二醇、1,8-壬二醇、新戊 二醇、二甘醇、二丙二醇、I,4·環己烷二醇、1,4-環己烷二 甲醇等二醇類之一種或兩種以上,與例如碳酸二甲酯、碳 酸二苯酯、碳酸伸乙酯、光氣等之碳酸酯類進行反應所獲 得脂肪族系聚碳酸酯二醇等。脂肪族系聚碳酸酯二醇之數 量平均分子量較佳爲1500至4000,更佳爲2000至3000 。若脂肪族系聚碳酸酯二醇之數量平均分子量爲小時,則 用於構成胺基甲酸酯樹脂之脂肪族系聚碳酸酯成分的比率 相對變小。因此,爲控制前述比率(A t 4 6 Q / A t 5 3 〇 )爲在前 述範圍’則較佳爲控制脂肪族系聚碳酸酯二醇之數量平均 分子量爲在上述範圍。若脂肪族系聚碳酸酯二醇之數量平 均分子量爲大時,由於源於脂肪族系聚碳酸酯成分之1460 cm·1附近之吸光度(Al46G)增加,脂肪族成分增加,則有 可能會導致接著性或經高溫高濕處理後之強度降低的情況 。若脂肪族系聚碳酸酯二醇之數量平均分子量爲小時,由 於強硬的胺基甲酸酯成分增加,有可能會導致無法緩和由 於基材之熱收縮所產生的應力,而使得接著性降低的情況 0 作爲本發明之胺基甲酸酯樹脂之構成成分的聚異氰酸 醋是包括:例如伸茬基二異氰酸酯等之芳香族二異氰酸酯 類;異佛酮二異氰酸酯及4,4-二環己基甲烷二異氰酸酯、 L 3 -雙(異氰酸甲酯)環己烷等之脂環式二異氰酸酯類; 六亞甲基二異氰酸酯、及2,2,4_三甲基六亞甲基二異氰酸 -20- 201132499 醋等之脂肪族二異氰酸酯類;將此等化合物預先以單獨或 與Η胃甲基丙烷等進行加成所獲得聚異氰酸酯類。若 使用芳香族異氰酸酯時,則有可能由於黃變之問題而爲不 佳的情況。此外,與脂肪族系相比較,將成爲強硬的塗膜 ’有可能會導致無法緩和由於基材之熱收縮所產生的應力 而使得接著性降低的情況。 「鏈段增長劑」是包括··例如乙二醇、二甘醇、1,4-丁二醇、新戊二醇及1,6-己二醇等之二醇類;甘油、三羥 甲基丙烷、及新戊四醇等之多元醇類;伸乙基二胺、六亞 甲基二胺、及哌阱等之二胺類;一乙醇胺及二乙醇胺等之 胺基醇類;硫二乙二醇等之硫二甘醇類:或水。但是,若 使用主鏈爲短的鏈段增長劑時,則有可能會導致源於胺基 甲酸酯成分之1530 cm·1附近之吸光度(Α153〇)增加、塗 布層之柔軟性降低的情況。因此鏈段增長劑較佳爲主鏈爲 長者。此外,就賦予塗布層之柔軟性的觀點,較佳爲屬於 脂肪族系且主鏈之碳數爲4至10之長度的二醇或二胺之鏈 段增長劑。從此等的觀點,使用於本發明之鏈段增長劑較 佳爲1,4-丁二醇、1,6-己二醇、六亞甲基二胺等。亦即,爲 防止源於胺基甲酸酯成分之1 5 3 0 cnT1附近之吸光度降低 、且賦予柔軟性,則較佳爲使用1,4-丁二醇、1,6-己二醇、 六亞甲基二胺等之直鏈且分子量爲大者。 本發明之塗布層之塗布方法是並無特殊限制,可採用 各種在生產線外塗布法或在生產線上塗布法。但是,從生 -21 - 201132499 產性或環境保護的觀點,則較佳爲本發明之塗布層是使用 水系之塗布液,且以後述之在生產線上塗布法而設置。此 時,本發明之胺基甲酸酯樹脂較佳爲水溶性。另外,上述 「水溶性」是意謂可溶解於水、或含有少於5 0質量%的水 溶性之有機溶劑的水溶液。 爲對胺基甲酸酯樹脂賦予水溶性,則可在胺基甲酸酯 分子骨架中導入(共聚合)磺酸(鹽)基或羧酸(鹽)基 。由於磺酸(鹽)基爲強酸性,且有因其吸濕性能而難以 維持耐濕性的情況,因此較佳爲導入弱酸性的羧酸(鹽) 基。此外,也可導入聚氧化烯基等之非離子性基。 爲對胺基甲酸酯樹脂導入羧酸(鹽)基,例如作爲多 元醇成分而將二羥甲基丙酸、二羥甲基丁酸等具有羧酸基 之多元醇化合物導入作爲共聚合成分,並以鹽形成劑加以 中和。「鹽形成劑」之具體實例是包括:氨、三甲基胺、 三乙基胺、三異丙基胺、三-正丙基胺、三-正丁基胺等之 三烷基胺類;N-甲基嗎啉、N-乙基嗎啉等之N-烷基嗎啉類 ;N•二甲基乙醇胺、N-二乙基乙醇胺等之N-二烷基烷醇胺 類。此等是可單獨使用或兩種以上倂用。 在爲賦予水溶性而使用具有羧酸(鹽)基之多元醇化 合物作爲共聚合成分的情況,假設胺基甲酸酯樹脂之總聚 異氰酸酯成分爲1 00莫耳%時,則胺基甲酸酯樹脂中之具 有殘酸(鹽)基之多元醇化合物的組成莫耳比較佳爲3至 ό〇莫耳%,更佳爲5至40莫耳%。若該組成莫耳比爲小於 -22- 201132499 3莫耳%時,則有可能會導致水分散性變得困難的情況。此 外,若該組成莫耳比爲超過6 0莫耳%時,則有可能由於耐 水性降低而導致耐濕熱性降‘低的情況。 本發明之胺基甲酸酯樹脂之玻璃轉移點溫度較佳爲低 於0°C,更佳爲低於-5°c。若玻璃轉移點溫度爲低於0°c時 ,則黏度接近於在進行加壓接著時所局部性地熔融的EVA 或PVB等之烯烴樹脂,對由於局部性地混合而獲得提高強 固接著性上則有貢獻,且從塗布層之應力緩和的觀點,則 容易獲得適合之柔軟性,因此爲較佳。 在本發明之胺基甲酸酯樹脂也可爲提高在高溫高濕下 之接著性而在樹脂本身導入交聯基。從塗液之經時穩定性 或交聯密度提高功效,則較佳爲矽烷醇基。 也可爲提高接著性而含有除了本發明之胺基甲酸酯樹 脂以外之樹脂。其係包括:例如聚醚、或將聚酯作爲構成 成分之胺基甲酸酯樹脂、丙烯酸酯樹脂、聚酯樹脂等。 (添加劑) 在本發明中,塗布層是可同時將前述胺基甲酸酯樹脂 與交聯劑作爲主成分。藉由含有交聯劑,則可更進一步提 高在高溫高濕下之接著性。此外,在以短時間進行高溫熱 壓接合的情況,則可防止由於EVA之侵蝕而導致基材密著 性降低。因此,可達成在各種接著條件也可對應的高泛用 性之易接著性。交聯劑是由於在高溫高濕處理也不易劣化 ,故以可與羧酸基、羥基、胺基等進行反應而形成醯胺鍵 -23- 201132499 、胺基甲酸酯鍵、尿素鍵者爲較佳。與此相反’若伴隨酯 鍵、醚鍵時,則有具有水解性的情況,因此爲不佳。在本 發明適合使用之交聯劑是包括:三聚氰胺系、異氰酸酯系 、碳化二亞胺系、噚唑啉系等。在此等中,從塗液之經時 穩定性、在高溫高濕處理下之接著性提高功效的觀點,則 較佳爲異氰酸酯系、碳化二亞胺系。更進一步,從.塗布層 可獲得適度的柔軟性、適當地賦予塗布層之應力緩和作用 的觀點,則特佳爲使用異氰酸酯系交聯劑。此外,爲促進 交聯反應,因應需要也可適當地使用觸媒等。 交聯劑之含量,相對於胺基甲酸酯樹脂,則較佳爲5 質量%以上且90質量%以下,更佳爲10質量%以上且50 質量%以下。若爲少時,則有塗布層在高溫高濕下之強度 降低、接著性降低的情況,若爲多時,則有塗布層之樹脂 柔軟性降低,在常溫、高溫高濕下之接著性降低的情況。 在本發明中,爲提高塗膜強度也可摻合兩種交聯劑。 此外,爲促進交聯反應,因應需要也可適當地使用觸媒等 〇 在本發明中,也可在塗布層中含有粒子。該粒子是包 括:(1)二氧化矽、高嶺石、滑石、輕質碳酸鈣、重質碳 酸鈣、沸石、氧化鋁、硫酸鋇、碳黑、氧化鋅、硫酸鋅、 碳酸鋅、二氧化鈦、緞光白、矽酸鋁、矽藻土、矽酸鈣、 氫氧化鋁、水化埃洛石、碳酸鎂、氫氧化鎂等之無機粒子 ;(2)丙烯酸酯或甲基丙烯酸酯系、氯乙烯系、醋酸乙烯 -24- 201132499 酯系、尼龍、苯乙烯/丙烯酸系、苯乙烯/ 丁二烯系、聚苯 乙稀/丙烯酸系、聚苯乙烯/異戊二烯系、聚苯乙烯/異戊二 嫌系、甲基丙烯酸甲酯/甲基丙烯酸丁酯系、三聚氰胺系、 聚碳酸酯系、尿素系、環氧系、胺基甲酸酯系、酚系、鄰 苯二甲酸二烯丙酯系、聚酯系等之有機粒子。 前述粒子較佳爲平均粒徑爲1至50〇11111者。平均粒徑 是並無特殊限制,從維持薄膜之透明性的觀點,則較佳爲 1 至 1 0 0 n m 〇 前述粒子是可含有兩種以上平均粒徑不同之粒子。 另外,上述之平均粒徑是使用透射型電子顯微鏡(TEM )’以12萬倍倍率攝影積層薄膜之截面來測定存在於塗布 層之截面10處以上的粒子之最大徑,即可作爲其等之平均 値而求得。 粒子之含量較佳爲0.5質量。/〇以上且20質量%以下。 若爲少時,則無法獲得充分的抗黏連性。此外,也會導致 耐刮傷性惡化。若爲多時,塗膜強度則降低。 塗布層也可以提高塗布時之調平性、塗布液之脫泡爲 目的而含有界面活性劑。界面活性劑是可爲陽離子系、陰 離子系、非離子系等中任一者,較佳爲矽系 '乙炔二醇系 或氟系界面活性劑。此等界面活性劑也可在不致於損及與 封止材之接著性程度之範圍,在塗布液中含有例如〇. 00 5 至0.5質量%之範圍。 -25- 201132499 爲對塗布層賦予其他功能性,也可在不致於損及與封 止材之接著性程度之範圍而含有各種添加劑。該添加劑是 包括:例如螢光染料、螢光增白劑、塑化劑、紫外線吸收 劑、顏料分散劑、抑泡劑、消泡劑、防腐劑、抗靜電劑等 0 在本發明中,在聚酯薄膜上設置塗布層之方法是包括 將含有溶劑、粒子、樹脂之塗布液在聚酯薄膜上塗布、乾 燥之方法。溶劑是包括:甲苯等之有機溶劑、水或水與水 溶性有機溶劑之混合系,從環境問題的觀點,則較佳爲水 單獨或經在水混合水溶性有機溶劑而成者。 (太陽能電池用易接著性聚酯薄膜之製造) 關於本發明之光學用易接著性聚酯薄膜之製造方法, 以聚對苯二甲酸乙二醇酯(在下文中,則簡稱爲「PET」) 薄膜爲例說明如下,當然並不受限於此等者。 將PET樹脂加以充分真空乾燥後,供應至擠壓機,由 T-模將約2 8 0°C之熔融PET樹脂以薄片狀熔融擠出於旋轉 冷卻輥,並以靜電流延法(electrostatic application method) 使其冷卻固化而獲得未延伸PET薄片。該未延伸PET薄片 是可爲單層構成或爲使用共擠出法的複層構成。 將所獲得未延伸PET薄片以經加熱至80至120°C之輥 朝長度方向加以延伸2.5至5.0倍,以獲得單軸向延伸PET 薄膜。並且.,以夾具把持薄膜端部而導入於經加熱至70至 140°C之熱風區,並朝寬度方向加以延伸2.5至5.0倍。接 -26- 201132499 著,導入於160至240°C之熱處理區而進行1至60 熱處理以使結晶配向完成。 在此薄膜製造步驟中之任意階段,在PET薄膜 單面塗布塗布液而形成如前所述之塗布層。塗布層 於PET薄膜之兩面也並無特別的問題。塗布液中之 成物的固體成份濃度較佳爲2至3 5重量%,特佳爲 重量°/p 用於將此塗布液塗布於PET薄膜之方法是可使 的任意方法。例如,逆向輥式塗布法、凹版輪轉式 、吻合式塗布法、模具式塗布機法、輥刷法、噴霧 法、風刀式塗布法、線棒式塗布法、管狀刮刀(Pipe] 法、浸透式塗布法、幕簾式塗布法等。將此等方法 或組合塗佈。 在本發明中,塗布層是在未延伸或單軸向延 PET薄膜塗布前述塗布液,經乾燥後至少朝單軸方 延伸,接著進行熱處理而形成。在進行薄膜之製膜 由在生產線上塗佈法形成塗布層,即可更進一步提 層與聚酯薄膜基材之密著性,因此從可提高在高溫 之封止材與密著性的觀點,則爲較佳。 在本發明中,最終所獲得塗布層之厚度較佳爲 3000 nm,更佳爲10至1000 nm,進一步更佳爲10至 ,特佳·爲10至400 nm。此外,塗布層經乾燥後之 較佳爲0.01至3 g/m2,更佳爲〇.〇1至1 g/m2,進一 秒鐘之 之至少 是形成 樹脂組 4至1 5 用習知 塗布法 式塗布 Doctor) 以單獨 伸後之 向加以 時,藉 高塗布 高濕下 10至 5 0 0 nm 塗布量 步更佳 -27- 201132499 爲0.01至0.5g/m2,特佳爲0.01至0.4g/m2。若塗布層之 塗布量爲少於〇.〇1 g/m2時,則對接著性之功效幾乎消失。 在另一方面,若塗布量爲超過3 g/m2時,則抗黏連性降低 〇 (太陽能電池用背板) 本發明之太陽能電池用背板是以具有前述塗布層之聚 酯薄膜作爲構成構件。特別是較佳爲使用於與封止材直接 接觸的最表層。藉由如此的構成,則本發明之太陽能電池 用背板可達成與封止材之強固的密著性,即使在長期嚴格 的環境下也可達成良好的密著性。因此,有助於太陽能電 池元件之保持防濕性或提高阻障性。 本發明之太陽能電池用背板之形態是可例示:例如具 有前述塗布層之聚酯薄膜/接著劑/具有金屬箔或金屬系薄 膜層之薄膜/接著劑/聚氟乙烯薄膜或聚酯系高耐久防濕薄 膜之構成。此外,本發明之聚酯薄膜也可爲在兩面具有該 塗布層之構成。本發明之塗布層也可與除了封止材以外之 構成而達成良好的接著性。在此,具有金屬箔或金屬系薄 膜層之薄膜可適合使用具有水蒸氣阻障性者。 前述金屬之種類是包括:鋁、錫、鎂、銀、不銹鋼等 ’其中,特別是鋁、銀由於具有較高的反射率且可容易地 以工業方式取得而爲較佳。金屬層是可製成金屬箔來使用 ’也可製成薄膜而積層在聚酯薄膜等。將此等金屬製成薄 膜而積層之方法是可使用真空蒸鍍法、濺鍍法、離子電鍍 法、電漿化學氣相沉積法(CVD )等。 -28- 201132499 在本發明中,可利用:將具有前述塗布層之聚酯薄膜 、具有金屬箔或金屬系薄膜層之薄膜、聚氟乙烯薄膜或聚 酯系高耐久防濕薄膜之各層間,以真空吸引等加以一體化 而進行熱壓接合的積層法等之一般成形法,將上述各層作 成爲一體成形體而加以熱壓接合成形以製造太陽能電池用 背板。此時,爲提高各薄膜間之接著性等,較佳爲透過接 著劑來積層。接著劑是包括:例如(甲基)丙烯酸系樹脂 、烯烴系樹脂、乙烯基系樹脂、其他等之以樹脂作爲媒介 物的主成分之加熱熔融型接著劑、溶劑型接著劑、光硬化 型接著劑等。 在此所謂的「高耐久防濕薄膜」是以提高耐候性爲目 的所積層者,高耐久防濕薄膜是包括:例如聚四氟乙烯( PTFE)、四氟乙烯-全氯烷氧基共聚物(PFA)、四氟乙烯 •六氟丙烯共聚物(FEP)、乙烯-四氟乙烯共聚物(ETFE )、聚氯三氟乙烯(PCTFE)、聚偏二氟乙烯(PVDF)、 或聚氟乙烯(PVF)等之氟樹脂薄膜、或由經在聚碳酸酯 、聚甲基丙烯酸甲酯、聚丙烯酸酯、聚對苯二甲酸乙二醇 酯(PET)、聚萘二甲酸乙二醇酯(PEN )、丙烯酸酯等之 樹脂中捏合紫外線吸收劑而成之樹脂組成物所構成之薄膜 〇 (太陽能電池模組) 太陽能電池模組是例如使用玻璃基板、經配設配線的 作爲光起電力元件的太陽能電池元件、以挾住太陽能電池 -29- 201132499 元件之狀態而插入的封止材、以及本發明之太陽能電池背 板所構成。封止劑是適合使用乙烯·醋酸乙烯酯共聚物或 聚乙烯醇縮丁醛樹脂等之烯烴樹脂。特別是由於本發明之 塗布層具有如上所述之柔軟性,可與例如乙烯•醋酸乙烯 酯共聚物或聚乙烯醇縮丁醛樹脂之封止材達成良好的接著 性。 封止材是可分類成:經由積層步驟的熱壓接合後,以 設置於另外生產線的烘箱之固化步驟來進行硬化反應之標 準固化型;及在積層步驟之積層機內部進行硬化反應之快 速固化型,但是任一者皆可適用。封止材之主成分是使用 乙烯•醋酸乙烯酯共聚物或聚乙烯醇縮丁醛樹脂等之烯烴 樹脂。另外,在此所謂「主成分」是意謂在封止劑中含有 50質量%以上,更佳爲70質量%以上者。因此,例如可爲 進行交聯反應而添加交聯劑或反應引發劑等。例如,在進 行熱交聯時,可使用:2,5-二甲基己烷-2,5-二羥基過氧化 物、2,5-二甲基-2,5-二(三級丁基過氧基)己炔-3、二-三 級丁基過氧化物、三級丁基異丙苯基過氧化物、2,5 -二甲 基-2,5-二(三級丁基過氧基)己烷等之有機過氧化物。此 外,在進行光硬化時,則可使用二苯甲酮、鄰苯甲醯基苯 甲酸甲酯或苯偶姻醚等之光增感劑。進一步也可考慮與玻 璃基板之接著而摻合矽烷偶合劑。也有以促進接著性及硬 化之目的而摻合的情況,含有環氧基之化合物是可使用: 參(2-羥基乙基)異三聚氰酸三縮水甘油酯、新戊二醇二 -30- 201132499 縮水甘油基醚、1,6 -己二醇二縮水甘油基醚、丙烯基縮水 甘油基醚、2 -乙基己基縮水甘油基醚等之含有環氧基之化 合物。 《實施例》 其次,使用實施例及比較例詳細地說明本發明,但是 本發明並不受限於以下之實施例者。此外,在本發明使用 之評估方法如下所述。 (1 )固有黏度 根據JIS K 73 67-5準則,且溶劑是使用苯酚(60質量 %)與1,1,2,2-四氯乙烷(40質量%)之混合溶劑,在30 °C進行測定。 (2 )薄膜之視密度 將薄膜切成4片5公分見方之正方形作爲試料。將此 疊合4片,將其厚度使用測微計變化位置而以4位有效數 字進行測定任意1 0處,並計算出疊合厚度之平均値。將該 平均値除以4且拾整成有效數字3位數來作爲每一片之平 均厚度(t: β m )。使用自動上皿天秤以4位有效數字測 定該試料4片之質量(w:克),並以下式計算出視密度。 另外,視密度是求到有效數字3位數: 視密度(g/cm3) = (wxi〇4) /(5.〇〇X5.〇〇x4xt)。 〈PD 1 1 07 1 8 7 008 5〉S -15- 201132499 to 1.60, by which both of the above characteristics can coexist. In other words, the aliphatic polycarbonate component having hydrolysis resistance and the urethane component which exhibits toughness are coexisted in a specific ratio, and both of the above characteristics are exhibited. Thereby, since the stress generated by the heat shrinkage of the polyester film when the heat is subsequently performed at a high temperature can be alleviated, the strong adhesion to the sealing material can be obtained, and it can also be used in the high-temperature and high-humidity environment thereafter. Since heat resistance and hydrolysis resistance are maintained, deterioration of the coating layer can be prevented. Among them, the absorbance (A146D) in the vicinity of 1460 cnT1 is derived from the deformation vibration characteristic of the C-H bond of the methylene group contained in the aliphatic polycarbonate component. Therefore, the absorbance (A146Q) in the vicinity of 1460 cm·1 is the amount of the aliphatic polycarbonate polyol component constituting the urethane resin depending on the coating layer. On the other hand, the absorbance (A153{) in the vicinity of 1530 (^1^1) is derived from the deformation vibration unique to the N-H bond contained in the urethane component. Therefore, the absorbance (A153C&gt;) in the vicinity of 1530 cm·1 is the amount of the urethane component constituting the urethane resin depending on the coating layer. Therefore, these absorbance ratios (A146Q/A153Q) are those in which two components each having different characteristics coexist in a specific ratio. In the present invention, the ratio (Ai46〇/A153.) is 0.70 to 1.60 as described above, but the lower limit of the ratio (Ai46〇/Ai530) is preferably 0.75, more preferably 0.80. Further, the upper limit of the ratio (A146〇/A15 30 ) is preferably 1.50, more preferably 1.45, still more preferably 1.40. If the ratio (Ai46〇/Ai530) is less than 〇.7〇, the tough urethane component becomes too much and the stress of the coating layer is moderately lowered, so that the heat resistance of the coating layer is resistant to -16-55 201132499 reduce. Further, when the ratio (A146()/AI53Q) is more than 1·, the aliphatic component of the soft aliphatic polycarbonate is excessively increased to lower the strength of the coating layer, so that the film strength or the moist heat resistance is lowered. According to the present invention, the adhesion to the sealing material can be exhibited by the above-described mode, so that the adhesion (moisture resistance) under high temperature and high humidity can be improved. Hereinafter, the constitution of the present invention will be described in detail. Further, when the coating layer is a urethane resin containing a fatty polycarbonate polyol as a constituent component and a crosslinking agent as a main component, it is derived from an aliphatic condensing spectrum set in an infrared spectroscopy spectrum. The ratio of the absorbance of the carbonate to 1 460 cnT1 (A146Q) to the absorbance of the urethane 1530 (the absorbance near the ^_1 (eight 153 〇) (human 146 () / 八 1) is 0.50 to 1.55 In this way, both of the above characteristics can be coexisted, and versatility which can be widely applied to various sealing materials can be achieved. In terms of sealing materials, from the viewpoint of improving productivity or preventing deterioration, it has been advanced. The species is composed of a compound containing a crosslinking agent, an ultraviolet absorber, etc. For example, the sealing material belonging to the standard curing type is subjected to thermocompression bonding (for example, after 90 to 13 CTC for 5 to 10 minutes). Heat treatment (for example, at 140 to 160 ° C for 30 to 50 minutes) to cause the sealing material to slowly harden. On the other side, in the case of a fast curing type sealing material, hot pressing is performed in a short time ( For example, at 1 40 to 1 60 °C 1 5 to 20 minutes) in order to make the sealing fast harden the subsequent conditions. Therefore, it is not only required to be used for various sealing and low-strength heat is divided into 5 3 0. 201132499 will also show the versatility of the same degree of adhesion, and also requires a highly versatile easy-adhesive film that can be used for various subsequent conditions. On the other hand, in the case of thermocompression bonding, the heat accompanying the film The stress generated by the shrinkage also varies depending on the type of the various sealing materials and the subsequent conditions. Especially for the standard curing type which requires a long time of high temperature, the stress change caused by the heat shrinkage will increase. As a result, when various sealing materials are applied, there is a case where the stress cannot be completely alleviated, and the adhesion to the sealing material is lowered. Particularly, when high-temperature thermocompression bonding is performed in a short time as in the rapid curing type, The sealing material partially melted on the coating layer will be eroded, in particular, the adhesion to the film substrate after the high temperature and high humidity treatment is lowered. Therefore, it is preferred to use a crosslinking agent. The crosslinked structure of the coating layer is stronger, and at the same time, the opposite characteristics are both coexisted. In the present invention, the coating layer is crosslinked with a urethane resin having an aliphatic polycarbonate polyol as a constituent component. The agent is a main component, and the absorbance (A146Q) near the 1 460 cnT1 derived from the aliphatic polycarbonate component and the 1 5 3 0 CHT1 derived from the urethane component are determined by infrared spectroscopy. The ratio of the nearby absorbance (A153Q) (A146Q/A153Q) is 0.50 to 1.55, whereby both of the above characteristics can coexist. Although the ratio (Ai46〇/A_i53Q) is 〇·50 to 1.55', the ratio (Ai46) The lower limit of 〇/Ai530 ) is preferably 0.60, more preferably 0.70. Further, the upper limit of the ratio (Ai46〇/A153〇) is preferably 1.45, more preferably 1.35, still more preferably 1.25. Thereby, since the heat can be thermally cured at a high temperature, the stress generated by the heat shrinkage of the film can be alleviated, even for various sealing materials, and then the condition -18-201132499 can obtain strong adhesion, and In the high temperature and high humidity environment, the heat resistance and hydrolysis resistance are maintained, so that the deterioration of the coating layer can be prevented. The reason why the preferred ratio range is changed by the crosslinking agent is due to an increase in the crosslinking point of the agent. (urethane resin) The urethane resin of the present invention contains at least a polyol component, an isocyanate component as a constituent component, and may contain a growth agent if necessary. The urethane resin of the present invention is a polymer compound obtained by copolymerizing a main urethane bond of these constituent components. In the present invention, an aliphatic polycarbonate polyol is used as a component of a urethane resin. A urethane resin containing an aliphatic polycarbonate polyol as a component is contained in the coating layer of the present invention, i.e., has high heat and humidity resistance. Further, the constituent components of these urethane resins can be confirmed by nuclear magnetic resonance analysis or the like. The component which is a constituent component of the urethane resin of the present invention is required to contain an aliphatic polyester polyol which is excellent in heat resistance and hydrolysis resistance. From the prevention of yellowing due to sunlight by the present invention, it is preferred to use an aliphatic polycarbonate polyol. The "aliphatic polycarbonate polyol" includes, for example, an aliphatic acid ester diol or an aliphatic polycarbonate triol, but a family of polycarbonate diols is suitably used. The aliphatic polycarbonate diol of the present invention as a component of the urethane resin includes, for example, by making ethylene propylene glycol 1,3-propanediol, 1,4-butanediol, 1,5- The pentanediol, 3- can also be cross-linked, and the poly-chain segment should be structured as a structure. It can be formed from the viewpoint of carbonation to form a carbon-fat to form a diol methyl-19-201132499-1,5-penta Alcohol, 1,6-hexanediol, 1,9-nonanediol, 1,8-nonanediol, neopentyl glycol, diethylene glycol, dipropylene glycol, I,4·cyclohexanediol, 1, An aliphatic polycondensation obtained by reacting one or two or more kinds of glycols such as 4-cyclohexanedimethanol with a carbonate such as dimethyl carbonate, diphenyl carbonate, ethyl carbonate, phosgene or the like Carbonate diol and the like. The number average molecular weight of the aliphatic polycarbonate diol is preferably from 1,500 to 4,000, more preferably from 2,000 to 3,000. When the number average molecular weight of the aliphatic polycarbonate diol is small, the ratio of the aliphatic polycarbonate component constituting the urethane resin is relatively small. Therefore, in order to control the ratio (A t 4 6 Q / A t 5 3 〇 ) to be in the above range, it is preferred to control the number average molecular weight of the aliphatic polycarbonate diol to be in the above range. When the number average molecular weight of the aliphatic polycarbonate diol is large, since the absorbance (Al46G) in the vicinity of 1460 cm·1 originating from the aliphatic polycarbonate component increases, the aliphatic component increases, which may result in Subsequent or reduced strength after high temperature and high humidity treatment. If the number average molecular weight of the aliphatic polycarbonate diol is small, since the tough urethane component is increased, there is a possibility that the stress due to the heat shrinkage of the substrate cannot be alleviated, and the adhesion is lowered. Case 0 Polyisocyanate as a constituent component of the urethane resin of the present invention is an aromatic diisocyanate including, for example, a decyl diisocyanate; isophorone diisocyanate and 4,4-bicyclo An alicyclic diisocyanate such as hexylmethane diisocyanate or L 3 -bis(isocyanatomethyl)cyclohexane; hexamethylene diisocyanate; and 2,2,4-trimethylhexamethylene Isocyanic acid-20-201132499 An aliphatic diisocyanate such as vinegar; a polyisocyanate obtained by adding these compounds in advance or separately with methyl propylpropane or the like. If an aromatic isocyanate is used, it may be unfavorable due to the problem of yellowing. Further, as compared with the aliphatic system, it becomes a tough coating film, which may cause a decrease in the adhesion due to the heat shrinkage of the substrate. "Segment growth agent" is a glycol including, for example, ethylene glycol, diethylene glycol, 1,4-butanediol, neopentyl glycol, and 1,6-hexanediol; glycerin, trishydroxyl Polyols such as propane and neopentyl alcohol; diamines such as ethyl diamine, hexamethylene diamine, and pipe trap; amine alcohols such as monoethanolamine and diethanolamine; sulfur Sulphur diethylene glycol such as ethylene glycol: or water. However, when a chain extender having a short main chain is used, there is a possibility that the absorbance (Α153〇) in the vicinity of 1530 cm·1 from the urethane component is increased, and the flexibility of the coating layer is lowered. . Therefore, the segment growth agent is preferably the main chain for the elderly. Further, from the viewpoint of imparting flexibility to the coating layer, a chain extender of a diol or a diamine which is aliphatic and has a carbon number of 4 to 10 in the main chain is preferable. From such a viewpoint, the segment growth agent used in the present invention is preferably 1,4-butanediol, 1,6-hexanediol, hexamethylenediamine or the like. In other words, in order to prevent the absorbance from the vicinity of 1 530 cnT1 derived from the urethane component from being lowered and imparting flexibility, it is preferred to use 1,4-butanediol or 1,6-hexanediol. A straight chain of hexamethylenediamine or the like has a large molecular weight. The coating method of the coating layer of the present invention is not particularly limited, and various coating methods in the production line or in the production line can be employed. However, from the viewpoint of productivity or environmental protection, it is preferred that the coating layer of the present invention is a coating liquid using a water system, and is provided in a production line coating method to be described later. At this time, the urethane resin of the present invention is preferably water-soluble. Further, the above "water-soluble" means an aqueous solution which is soluble in water or contains less than 50% by mass of a water-soluble organic solvent. In order to impart water solubility to the urethane resin, a sulfonic acid (salt) group or a carboxylic acid (salt) group may be introduced (copolymerized) into the urethane molecular skeleton. Since the sulfonic acid (salt) group is strongly acidic and it is difficult to maintain moisture resistance due to its hygroscopic property, it is preferred to introduce a weakly acidic carboxylic acid (salt) group. Further, a nonionic group such as a polyoxyalkylene group may be introduced. In order to introduce a carboxylic acid (salt) group into a urethane resin, for example, as a polyol component, a polyol compound having a carboxylic acid group such as dimethylolpropionic acid or dimethylolbutyric acid is introduced as a copolymer component. And neutralized with a salt forming agent. Specific examples of the "salt forming agent" include trialkylamines such as ammonia, trimethylamine, triethylamine, triisopropylamine, tri-n-propylamine, and tri-n-butylamine; N-alkylmorpholine such as N-methylmorpholine or N-ethylmorpholine; N-dialkylalkanolamines such as N•dimethylethanolamine and N-diethylethanolamine. These can be used alone or in combination of two or more. In the case where a polyol compound having a carboxylic acid (salt) group is used as a copolymerization component for imparting water solubility, assuming that the total polyisocyanate component of the urethane resin is 100% by mole, the aminocarboxylic acid is used. The composition of the polyol compound having a residual acid (salt) group in the ester resin is preferably from 3 to ό〇 mol%, more preferably from 5 to 40 mol%. If the composition molar ratio is less than -22 - 201132499 3 mole %, there is a possibility that water dispersibility becomes difficult. Further, when the composition molar ratio is more than 60% by mole, there is a possibility that the wet heat resistance is lowered to be low due to a decrease in water resistance. The glass transition point temperature of the urethane resin of the present invention is preferably lower than 0 ° C, more preferably lower than -5 ° C. When the glass transition point temperature is lower than 0 ° C, the viscosity is close to that of the olefin resin such as EVA or PVB which is locally melted at the time of pressurization, and the strong adhesion is obtained by local mixing. There is a contribution, and from the viewpoint of stress relaxation of the coating layer, it is easy to obtain suitable flexibility, and therefore it is preferable. The urethane resin of the present invention may also introduce a crosslinking group into the resin itself in order to improve the adhesion under high temperature and high humidity. The stanol group is preferred from the viewpoint of the stability over time of the coating liquid or the crosslinking density. A resin other than the urethane resin of the present invention may be contained for the purpose of improving the adhesion. The system includes, for example, a polyether or a urethane resin having a polyester as a constituent component, an acrylate resin, a polyester resin or the like. (Additive) In the present invention, the coating layer can simultaneously contain the aforementioned urethane resin and a crosslinking agent as main components. By containing a crosslinking agent, the adhesion under high temperature and high humidity can be further improved. Further, in the case where the high-temperature thermocompression bonding is performed in a short time, it is possible to prevent the substrate adhesion from being lowered due to the erosion of the EVA. Therefore, it is possible to achieve easy adhesion of high versatility which can be matched in various subsequent conditions. Since the crosslinking agent is not easily deteriorated by high-temperature and high-humidity treatment, it can be reacted with a carboxylic acid group, a hydroxyl group, an amine group or the like to form a guanamine bond-23-201132499, a urethane bond, and a urea bond. Preferably. On the other hand, when it is accompanied by an ester bond or an ether bond, it may be hydrolyzable, which is not preferable. The crosslinking agent suitable for use in the present invention includes melamine-based, isocyanate-based, carbodiimide-based, oxazoline-based, and the like. Among these, an isocyanate-based or carbodiimide-based system is preferred from the viewpoints of the stability of the coating liquid and the effect of improving the adhesion under high-temperature and high-humidity treatment. Further, from the viewpoint of obtaining moderate flexibility from the coating layer and appropriately imparting a stress relieving action to the coating layer, it is particularly preferable to use an isocyanate crosslinking agent. Further, in order to promote the crosslinking reaction, a catalyst or the like may be appropriately used as needed. The content of the crosslinking agent is preferably 5% by mass or more and 90% by mass or less, and more preferably 10% by mass or more and 50% by mass or less based on the urethane resin. When the amount is small, the strength of the coating layer is lowered under high temperature and high humidity, and the adhesion is lowered. When the amount is too large, the flexibility of the resin of the coating layer is lowered, and the adhesion at normal temperature, high temperature and high humidity is lowered. Case. In the present invention, two kinds of crosslinking agents may be blended in order to increase the film strength. Further, in order to promote the crosslinking reaction, a catalyst or the like may be suitably used as needed. In the present invention, particles may be contained in the coating layer. The particles are: (1) cerium oxide, kaolinite, talc, light calcium carbonate, heavy calcium carbonate, zeolite, alumina, barium sulfate, carbon black, zinc oxide, zinc sulfate, zinc carbonate, titanium dioxide, satin Inorganic particles such as white, aluminum silicate, diatomaceous earth, calcium citrate, aluminum hydroxide, hydrated halloysite, magnesium carbonate, magnesium hydroxide, etc.; (2) acrylate or methacrylate, vinyl chloride , vinyl acetate-24- 201132499 ester, nylon, styrene/acrylic, styrene/butadiene, polystyrene/acrylic, polystyrene/isoprene, polystyrene/different Ethylene methacrylate, methyl methacrylate/butyl methacrylate, melamine, polycarbonate, urea, epoxy, urethane, phenol, diallyl phthalate Organic particles such as esters and polyesters. The particles preferably have an average particle diameter of from 1 to 50 〇 11111. The average particle diameter is not particularly limited, and from the viewpoint of maintaining the transparency of the film, it is preferably from 1 to 100 nm. The particles may contain two or more kinds of particles having different average particle diameters. In addition, the above average particle diameter is a cross section of a laminated film formed by a transmission electron microscope (TEM) at a magnification of 120,000 times, and the maximum diameter of particles existing in the cross section 10 or more of the coating layer is measured. The average is eager to find. The content of the particles is preferably 0.5 mass. /〇 is above 20% by mass. If it is small, sufficient blocking resistance cannot be obtained. In addition, it can also cause scratch resistance to deteriorate. If it is too much, the film strength is lowered. The coating layer may contain a surfactant for the purpose of improving the leveling property at the time of coating and defoaming of the coating liquid. The surfactant may be any of a cationic system, an anion system, and a nonionic system, and is preferably an anthracene-acetylene glycol-based or fluorine-based surfactant. The surfactant may be contained in the coating liquid in a range of, for example, 00 00 5 to 0.5% by mass insofar as it does not impair the adhesion to the sealing material. -25- 201132499 In order to impart other functional properties to the coating layer, various additives may be contained in such a range as not to impair the adhesion to the sealing material. The additive includes, for example, a fluorescent dye, a fluorescent whitening agent, a plasticizer, a UV absorber, a pigment dispersant, a suds suppressor, an antifoaming agent, a preservative, an antistatic agent, etc. In the present invention, The method of providing a coating layer on a polyester film is a method of coating and drying a coating liquid containing a solvent, a particle, and a resin on a polyester film. The solvent is an organic solvent including toluene or the like, water or a mixture of water and a water-soluble organic solvent. From the viewpoint of environmental problems, it is preferred that water be mixed with water-soluble organic solvent alone or in water. (Production of the easy-adhesive polyester film for solar cell) The method for producing the optically easy-contact polyester film of the present invention is polyethylene terephthalate (hereinafter, simply referred to as "PET"). The film is exemplified as follows, and of course, it is not limited to these. After the PET resin is sufficiently vacuum-dried, it is supplied to an extruder, and a molten PET resin of about 280 ° C is melt-extruded into a rotary cooling roll by a T-die, and electrostatically applied (electrostatic application) Method) Cooling and curing to obtain an unstretched PET sheet. The unstretched PET sheet may be composed of a single layer or a composite layer using a coextrusion method. The obtained unstretched PET sheet was stretched 2.5 to 5.0 times in the longitudinal direction by a roll heated to 80 to 120 ° C to obtain a uniaxially stretched PET film. Further, the end of the film is held by a jig and introduced into a hot air zone heated to 70 to 140 ° C and extended 2.5 to 5.0 times in the width direction. In the heat treatment zone of 160 to 240 ° C, a heat treatment of 1 to 60 is carried out to complete the crystallization alignment. At any stage of the film production step, the coating liquid is applied to one side of the PET film to form a coating layer as described above. There are no particular problems with the coating layer on both sides of the PET film. The solid content concentration of the composition in the coating liquid is preferably from 2 to 35 % by weight, particularly preferably the weight % / p. The method for applying the coating liquid to the PET film is any method which can be used. For example, reverse roll coating method, gravure rotary type, staple coating method, die coater method, roll brush method, spray method, air knife coating method, wire bar coating method, tubular blade method, and soaking Coating method, curtain coating method, etc. These methods or combinations are applied. In the present invention, the coating layer is applied to the coating liquid in an unstretched or uniaxially stretched PET film, and after drying, at least toward a single axis The square extension is followed by heat treatment. The film formation by the coating method is carried out by a coating method on the production line, so that the adhesion between the layer and the polyester film substrate can be further improved, so that the temperature can be increased. In the present invention, the thickness of the finally obtained coating layer is preferably 3,000 nm, more preferably 10 to 1000 nm, still more preferably 10 to 10, particularly preferably. The thickness of the coating layer is preferably from 0.01 to 3 g/m2, more preferably from 〇1 to 1 g/m2, and at least one second of the formation of the resin group 4 to 1 5 Coating the Doctor with a conventional coating method In the case of high coating, the coating amount of 10 to 500 nm is preferably -27-201132499, 0.01 to 0.5 g/m2, and particularly preferably 0.01 to 0.4 g/m2. If the coating amount of the coating layer is less than 〇.〇1 g/m2, the effect on the adhesion is almost eliminated. On the other hand, when the coating amount is more than 3 g/m2, the blocking resistance is lowered (the back sheet for a solar cell). The back sheet for a solar cell of the present invention is constituted by a polyester film having the above-mentioned coating layer. member. In particular, it is preferably used in the outermost layer in direct contact with the sealing material. According to such a configuration, the back sheet for a solar cell of the present invention can achieve strong adhesion to the sealing material, and good adhesion can be achieved even in a long-term strict environment. Therefore, it is possible to contribute to the moisture resistance of the solar battery element or to improve the barrier property. The form of the back sheet for a solar cell of the present invention is exemplified by, for example, a polyester film/adhesive having the coating layer/film/adhesive/polyvinyl fluoride film or polyester having a metal foil or a metal film layer. The composition of the durable moisture-proof film. Further, the polyester film of the present invention may have a constitution in which the coating layer is provided on both sides. The coating layer of the present invention can also achieve good adhesion to a structure other than the sealing material. Here, a film having a metal foil or a metal film layer can be suitably used for those having water vapor barrier properties. The type of the metal described above includes aluminum, tin, magnesium, silver, stainless steel, etc. Among them, aluminum and silver are particularly preferable because they have a high reflectance and can be easily obtained industrially. The metal layer can be formed into a metal foil and can be formed into a film and laminated on a polyester film or the like. A method of laminating these metals into a thin film can be carried out by vacuum deposition, sputtering, ion plating, plasma chemical vapor deposition (CVD) or the like. -28- 201132499 In the present invention, it is possible to use between a polyester film having the above-mentioned coating layer, a film having a metal foil or a metal film layer, a polyvinyl fluoride film or a polyester-based high-duty moisture-proof film, A general molding method such as a lamination method in which vacuum suction or the like is integrated and subjected to thermocompression bonding, and the above-mentioned respective layers are integrally molded and subjected to thermocompression bonding to produce a solar cell back sheet. In this case, in order to improve the adhesion between the respective films, it is preferred to laminate the layers by means of an adhesive. The adhesive agent is a hot-melt type adhesive, a solvent-based adhesive, and a photo-curing type, which are, for example, a (meth)acrylic resin, an olefin resin, a vinyl resin, or the like, which is a main component of a resin as a vehicle. Agents, etc. The so-called "high-endurance moisture-proof film" is a laminate for the purpose of improving weather resistance, and the high-durability moisture-proof film includes, for example, polytetrafluoroethylene (PTFE), tetrafluoroethylene-perchloroalkoxy copolymer. (PFA), tetrafluoroethylene/hexafluoropropylene copolymer (FEP), ethylene-tetrafluoroethylene copolymer (ETFE), polychlorotrifluoroethylene (PCTFE), polyvinylidene fluoride (PVDF), or polyvinyl fluoride a fluororesin film of (PVF) or the like, or by polycarbonate, polymethyl methacrylate, polyacrylate, polyethylene terephthalate (PET), polyethylene naphthalate ( PEN), a film composition composed of a resin composition obtained by kneading a UV absorber in a resin such as acrylate, and a solar cell module, for example, a glass substrate and a wiring as a light-emitting element The solar cell element is composed of a sealing material inserted in a state in which the solar cell -29-201132499 element is caught, and a solar cell back sheet of the present invention. The blocking agent is preferably an olefin resin such as an ethylene-vinyl acetate copolymer or a polyvinyl butyral resin. In particular, since the coating layer of the present invention has the flexibility as described above, good adhesion can be achieved with, for example, an ethylene-vinyl acetate copolymer or a polyvinyl butyral resin sealing material. The sealing material is a standard curing type which can be classified into: a hardening reaction by a curing step of an oven provided in another production line after thermocompression bonding in a lamination step; and a rapid curing reaction in which a hardening reaction is performed inside the laminating machine of the laminating step Type, but either can be applied. The main component of the sealing material is an olefin resin such as an ethylene/vinyl acetate copolymer or a polyvinyl butyral resin. In addition, the term "main component" as used herein means that the sealing agent contains 50% by mass or more, and more preferably 70% by mass or more. Therefore, for example, a crosslinking agent, a reaction initiator, or the like may be added to carry out the crosslinking reaction. For example, when performing thermal crosslinking, 2,5-dimethylhexane-2,5-dihydroxy peroxide, 2,5-dimethyl-2,5-di(tributyl) can be used. Peroxy)hexyne-3, di-tertiary butyl peroxide, tertiary butyl cumyl peroxide, 2,5-dimethyl-2,5-di(tributyl) An organic peroxide such as oxy)hexane. Further, when photocuring is carried out, a photo sensitizer such as benzophenone, methyl phthalate or benzoin ether can be used. Further, it is also conceivable to blend a decane coupling agent with the glass substrate. There are also cases in which blending for the purpose of promoting adhesion and hardening, and an epoxy group-containing compound can be used: ginseng (2-hydroxyethyl) isocyanuric acid triglycidyl ester, neopentyl glycol di-30 - 201132499 An epoxy group-containing compound such as glycidyl ether, 1,6-hexanediol diglycidyl ether, propylene glycidyl ether or 2-ethylhexyl glycidyl ether. <<Embodiment>> Next, the present invention will be described in detail using examples and comparative examples, but the present invention is not limited to the examples below. Further, the evaluation method used in the present invention is as follows. (1) The intrinsic viscosity is in accordance with JIS K 73 67-5, and the solvent is a mixed solvent of phenol (60% by mass) and 1,1,2,2-tetrachloroethane (40% by mass) at 30 °C. The measurement was carried out. (2) Apparent density of the film The film was cut into four squares of 5 cm square as a sample. Four sheets were laminated, and the thickness thereof was measured using a micrometer to change the position by any significant number of four digits, and the average thickness of the laminated thickness was calculated. The average is divided by 4 and rounded to a significant number of 3 digits as the average thickness (t: β m ) of each slice. The mass (w: gram) of the four samples was measured using a four-digit effective number using an automatic weighing scale, and the apparent density was calculated by the following formula. In addition, the apparent density is the effective number of 3 digits: apparent density (g/cm3) = (wxi〇4) / (5.〇〇X5.〇〇x4xt). <PD 1 1 07 1 8 7 008 5>

-31 - 201132499 (3 )色調 將薄膜切成5公分見方之正方形’疊合成25〇/ζπ1以上 而測定Lab表示系統之l値、a値及b値。 (測定條件) 衣置·色差日十·日本電色工業公司(Nipp〇nDenshoku-31 - 201132499 (3) Hue The film was cut into squares of 5 cm squares. The composite was 25 〇 / ζ π1 or more and Lab was expressed as l値, a値 and b値 of the system. (Measurement conditions) Clothing, color difference, day 10, Nippon Denshoku Industrial Co., Ltd. (Nipp〇nDenshoku

Industries Co·, Ltd.)製造之 ZE-2000 測定方法:反射 標準光:C光源 視野角:2度 (4 )玻璃轉移點溫度 根據JIS K7121準則,使用示差掃描熱量測定計(精 工儀器股份有限公司(Seiko Instruments Inc.)製造之 DSC6200 ),由DSC曲線測定玻璃轉移開始溫度。 (5 )使用紅外線光譜法之吸光度測定 就所獲得太陽能電池用易接著性聚酯薄膜削取塗布層 而採取約1毫克之試料。對所採取之試料施加壓力而製造 成型成厚度約lym之薄膜狀的塗布層試料片(大小:約 50/zmx約50^m)。並且’作爲空白試料而就與基材薄膜 同質之PET樹脂也以與前述相同的方式而製造試料片(空 白試料片)。 將所製得試料片放在KBr板上,以下列條件之顯微透 射法進行測定紅外線吸收光譜。塗布層之紅外線光譜法光 譜是作爲由塗布層試料片所獲得紅外線光譜法光譜與空白 試料片之光譜的光譜差異而測定。 -32- 201132499 將在1460±10 cnT1之區域具有吸收極大的吸收波峰高 度値作爲源於脂肪族系聚碳酸酯成分之1 460 cm·1附近之 吸光度(A146g),而在ISSOilOcnr1之區域具有吸收極大 的吸收波峰高度値則作爲源於胺基甲酸酯成分之1 5 3 0 cnT1附近之吸光度(A153Q)。另外,連接各極大吸收波峰 的兩側下擺之線作爲基線。由所獲得吸光度以下式計算出 吸光度比率: (吸光度比率)= A146Q/A1530。 (測定條件)ZE-2000 manufactured by Industries Co., Ltd. Determination method: Reflected standard light: C light source viewing angle: 2 degrees (4) Glass transition point temperature According to JIS K7121 guidelines, using differential scanning calorimeter (Seiko Instruments Co., Ltd. (DSC6200, manufactured by Seiko Instruments Inc.), the glass transition starting temperature was determined from the DSC curve. (5) Measurement of absorbance by infrared spectroscopy A sample of about 1 mg was taken for the obtained adhesive film for solar cell obtained by peeling off the coating layer. A film-like coating layer sample piece (size: about 50/zmx and about 50 μm) formed into a film having a thickness of about lym was produced by applying pressure to the sample to be taken. Further, a sample piece (a blank sample piece) was produced in the same manner as described above for the PET resin which is the same as the base film as a blank sample. The prepared test piece was placed on a KBr plate, and the infrared absorption spectrum was measured by a microscopic transmission method under the following conditions. The infrared spectroscopy spectrum of the coating layer was measured as the spectral difference between the infrared spectroscopy spectrum obtained from the coating layer sample piece and the spectrum of the blank sample piece. -32- 201132499 It has an absorption peak height 吸收 in the region of 1460±10 cnT1 as the absorbance (A146g) near the 1 460 cm·1 of the aliphatic polycarbonate component, and absorption in the region of ISSOilOcnr1 The maximum absorption peak height 作为 is derived from the absorbance (A153Q) near the 1 5 3 0 cnT1 of the urethane component. In addition, the line connecting the hem of each of the maximal absorption peaks is used as the baseline. The absorbance ratio was calculated from the obtained absorbance by the following formula: (absorbance ratio) = A146Q/A1530. (measurement conditions)

裝置:FT-IR分析裝置:SPECTRA TECH公司製造之 IR β s/SIRM 偵測器:MCT 分解能:4 cnT1 積算次數:128次 (6 )接著性 準備將所獲得太陽能電池用易接著性白色聚酯薄膜切 成100 mm寬xlOO mm長,及將EVA薄片切成70 mm寬X 90 mm長者,並以薄膜(塗布層面)/下述之EVA/ (塗布 層面)薄膜之構成加以疊合,然後以真空積層機且以下述 之接著條件加以熱壓接合而製造試樣。將所製得試樣切成 20 mm寬xlOO mm長後,貼附於SUS板,而以下述之條件 使用拉伸試驗機進行測定薄膜層與EVA層之剝離強度。剝 離強度是超過極大點後穩定地剝離的部分之平均値而測定 。以下列基準進行分等級: -33- 201132499 ◎ : 100N/20mm以上,或薄膜之材料破裂; 〇:75 N/20 mm 以上且低於 100 N/20 mm ; △ : 50 N/20 mm 以上且低於 75 N/20 mm ; X:低於 50N/20mm» (試樣製造條件) 裝置:真空積層機:NPC公司(NPC Incorporated)製 造之LM-3 0X3 0型 加壓:1氣壓 EVA : A. 標準固化型 I.Sunvic 公司(Sunvic Co·,Ltd.)製造之 Urtla Pearl PV (0.4 /z m ) 積層步驟:100°C (真空5分鐘、真空加壓5分鐘) 固化步驟:熱處理150°C (常壓45分鐘) 11 · M i t s ui C h em i c al s F ab r 〇,In c ·製造之 SOLAR EVA SC4 ( 0.4 〆 m ) 積層步驟:130 °C (真空5分鐘、真空加壓5分鐘) 固化步驟:150°C (常壓45分鐘) B. 快速固化型 I. Sunvic 公司製造之 Urtla Pearl PV ( 〇.45μ m) 積層步驟:135 °C (真空5分鐘、真空加壓15分鐘)Device: FT-IR analyzer: IR β s/SIRM detector manufactured by SPECTRA TECH: MCT decomposition energy: 4 cnT1 Total number of calculations: 128 times (6) Adhesive preparation for easy-to-adhere white polyester for solar cells The film is cut into 100 mm wide x 100 mm long, and the EVA sheet is cut into 70 mm wide X 90 mm long and laminated with a film (coating layer) / EVA / (coated layer) film as described below, and then The sample was produced by hot press bonding using a vacuum laminator under the following conditions. The prepared sample was cut into a length of 20 mm width x 100 mm, attached to a SUS plate, and the peel strength of the film layer and the EVA layer was measured using a tensile tester under the following conditions. The peel strength is measured as the average enthalpy of the portion which is stably peeled off after the maximum point. Graded according to the following criteria: -33- 201132499 ◎ : 100N/20mm or more, or the material of the film is broken; 〇: 75 N/20 mm or more and less than 100 N/20 mm; △ : 50 N/20 mm or more Less than 75 N/20 mm; X: Less than 50N/20mm» (Sample manufacturing conditions) Device: Vacuum laminator: LM-3 0X3 manufactured by NPC Incorporated Type 0 Pressurization: 1 Air pressure EVA : A . Standard Curing I. Sunvic Co., Ltd. (Urvla Pearl PV (0.4 /zm)) Lamination step: 100 ° C (vacuum for 5 minutes, vacuum press for 5 minutes) Curing step: heat treatment 150 ° C (Normal pressure 45 minutes) 11 · M its ui C h em ic al s F ab r 〇,In c ·Manufactured SOLAR EVA SC4 ( 0.4 〆m ) Lamination step: 130 °C (vacuum for 5 minutes, vacuum pressurization 5 Minutes) Curing step: 150 ° C (normal pressure 45 minutes) B. Rapid curing type I. Urtla Pearl PV ( 〇.45 μ m) manufactured by Sunvic Company Lamination step: 135 ° C (vacuum for 5 minutes, vacuum pressurization for 15 minutes) )

II. M i t s u i C h e m i c a 1 s F a b r ο,I n c.製造之 S Ο L A R E V A RC02B ( 0.45^ m ) -34- 201132499 積層步驟:l5〇°C (真空5分鐘、真空加壓15分鐘) (測定條件) 裝置:TENSILON 東洋 BALDWIN 公司製造之 RTM-1 00 剝離速度:200毫米/分鐘 剝離角度:1 8 0度 (7 )耐濕熱性 將所獲得太陽能電池用易接著性白色聚酯薄膜在高溫 高濕槽中且在85 °C、85 % RH之環境下放置1000小時。其 次,取出太陽能電池用易接著性白色聚酯薄膜,在室溫常 濕下放置24小時。其後,以與前述(4 )相同的方法測定 剝離強度,並以下列基準進行分等級: ◎ : 100N/2 0mm以上,或薄膜之材料破裂; 〇:75 N/20 mm 以上且低於 100 N/20 mm: △ : 50 N/20 mm 以上且低於 75 N/20 mm; X:低於 50 N/20 mm。 (以脂肪族系聚碳酸酯多元醇作爲構成成分之胺基甲酸酯 樹脂A-1之聚合) 在配備攪拌機、戴氏冷凝器(Dimroth condenser)、 氮氣導入管、矽凝膠乾燥管、及溫度計之四頸燒瓶中,飼 入43.75質量份之4,4-二苯基甲烷二異氰酸酯、12.85質量 份之二羥甲基丁酸、153.4 1質量份之數量平均分子量爲 2000之聚碳酸六亞甲酯二醇、0.03質量份之二月桂酸丁基 -35- 201132499 錫、及84.00質量份之作爲溶劑的丙酮,在氮氣之氣體環 境下且在7 5 °C攪拌3小時’並加以確認反應液已達到吾所 欲之胺當量。其次,將該反應液降溫至40 °C後,添加入8.77 質量份之三乙基胺,以獲得聚胺基甲酸酯預聚物溶液。其 次,在配備可高速攪拌的高速分散機之反應容器中,飼入 450克之水,調整成251:而一邊以2000 min·1攪拌混合, 一邊添加入聚胺基甲酸酯預聚物溶液而加以水分散。其後 ,藉由在減壓下移除丙酮及水之一部分,以調製得固體成 份爲35%之水溶性聚胺基甲酸酯樹脂溶液(A-1 )。所獲得 聚胺基甲酸酯樹脂(A-1)之玻璃轉移點溫度爲-30°C。 (以脂肪族系聚碳酸酯多元醇作爲構成成分之胺基甲酸酯 樹脂A-2之聚合) 在配備攪拌機、戴氏冷凝器、氮氣導入管、矽凝膠乾 燥管、及溫度計之四頸燒瓶中,飼入29.14質量份之4,4-二苯基甲烷二異氰酸酯、7.57質量份之二羥甲基丁酸、 1 7 3.29質量份之數量平均分子量爲3 000之聚碳酸六亞甲 酯二醇、0.03質量份之二月桂酸丁基錫、及84.00質量份 之作爲溶劑的丙酮,在氮氣之氣體環境下且在75°C攪拌3 小時,並加以確認反應液已達到吾所欲之胺當量。其次, 將該反應液降溫至40 °C後,添加入5 · 1 7質量份之三乙基胺 以獲得聚胺基甲酸酯預聚物溶液。其次’在配備可高速攪 拌的高速分散機之反應容器中,飼入450克之水,調整成 25°C而一邊以2000 min·1攪拌混合’一邊添加入聚胺基甲 •36- 201132499 酸酯預聚物溶液而加以水分散。其後,藉由在減壓下移除 丙酮及水之一部分,以調製得固體成份爲3 5 %之水溶性聚 胺基甲酸酯樹脂溶液(A-2 )。 (以脂肪族系聚碳酸酯多元醇作爲構成成分之胺基甲酸酯 樹脂A-3之聚合) 在配備攪拌機、戴氏冷凝器、氮氣導入管、矽凝膠乾 燥管、及溫度計之四頸燒瓶中,飼入43.7 5質量份之4,4-二苯基甲烷二異氰酸酯、11.12質量份之二羥甲基丁酸、 1.97質量份之己二醇、143.40質量份之數量平均分子量爲 2000之聚碳酸六亞甲酯二醇、0.03質量份之二月桂酸丁基 錫、及8 4.00質量份之作爲溶劑的丙酮,在氮氣之氣體環 境下且在7 5 °C攪拌3小時,並加以確認反應液已達到吾所 欲之胺當量。其次,將該反應液降溫至40°C後,添加入8.77 質量份之三乙基胺,以獲得聚胺基甲酸酯預聚物溶液。其 次,在配備可高速攪拌的高速分散機之反應容器中,飼入 450克之水,調整成25°C而一邊以2000 min·1攪拌混合, 一邊添加入聚胺基甲酸酯預聚物溶液而加以水分散。其後 ,藉由在減壓下移除丙酮及水之一部分,以調製得固體成 份爲35%之水溶性聚胺基甲酸酯樹脂溶液(A_3 )。 (以脂肪族系聚碳酸酯多元醇作爲構成成分之含有矽烷醇 基之胺基甲酸酯樹脂A-4之聚合) 在配備攪拌機、戴氏冷凝器、氮氣導入管、矽凝膠乾 燥管、及溫度計之四頸燒瓶中,飼入3 8 · 4 1質量份之異佛 -37- 201132499 酮二異氰酸酯、6.95質量份之二羥甲基丙酸、158.99質量 份之數量平均分子量爲2000之聚碳酸六亞甲酯二醇、0.03 質量份之二月桂酸丁基錫、及84.00質量份之作爲溶劑的 丙酮,在氮氣之氣體環境下且在75 °C攪拌3小時,並加以 確認反應液已達到吾所欲之胺當量。其次’將該反應液降 溫至4(TC後,添加入4.37質量份之三乙基胺以獲得聚胺基 甲酸酯預聚物溶液。其次,添加入3_84質量份之r-(胺 基乙基)胺基丙基三乙氧基矽烷、1.8〇質量份之2-〔 (2- 胺基乙基)胺基〕乙醇與450克之水,並逐滴加入聚胺基 甲酸酯預聚物溶液而加以水分散。其後,藉由在減壓下移 除丙酮及水之一部分,以調製得固體成份爲3 0%之水溶性 含有矽烷醇基之聚胺基甲酸酯樹脂溶液(A-4 )。 (以脂肪族系聚碳酸酯多元醇作爲構成成分之胺基甲酸酯 樹脂A-5之聚合) 除了將水溶性聚胺基甲酸酯樹脂(A- 1 )之數量平均分 子量爲2000之聚碳酸六亞甲酯二醇變更爲數量平均分子 量爲1〇〇〇之聚碳酸六亞甲酯二醇以外,其餘則以相同的方 法而獲得固體成份爲35%之水溶性聚胺基甲酸酯樹脂溶液 (A-5)。 (以脂肪族系聚碳酸酯多元醇作爲構成成分之胺基甲酸酯 樹脂A-6之聚合) 除了將水溶性聚胺基甲酸酯樹脂(A-1)之數量平均分 子量爲2000之聚碳酸六亞甲酯二醇變更爲數量平均分子 -38 - 201132499 量爲500 0之聚碳酸六亞甲酯二醇以外,其餘則以相同 ' 法而獲得固體成份爲3 5 %之水溶性聚胺基甲酸酯樹脂 (A - 6 )。 (以聚酯多元醇作爲構成成分之胺基甲酸酯樹脂之 A-7 ) 除了將水溶性聚胺基甲酸酯樹脂(A-1)之數量平 子量爲2000之聚碳酸六亞甲酯二醇變更爲數量平均 量爲2000的聚酯二醇以外,其餘則以相同的方法而獲 體成份爲35%之水溶性聚胺基甲酸酯樹脂溶液(A-7 ) (以聚醚多元醇作爲構成成分之胺基甲酸酯樹脂之 A-8 ) 除了將水溶性聚胺基甲酸酯樹脂(A- 1 )之數量平 子量爲2000之聚碳酸六亞甲酯二醇變更爲數量平均 量爲2000之聚醚二醇以外,其餘則以相同的方法而獲 體成份爲35%之水溶性聚胺基甲酸酯樹脂溶液(A-8 ) (以脂肪族系聚碳酸酯多元醇作爲構成成分之胺基甲 樹脂A-9之聚合)II. M itsui C hemica 1 s F abr ο,I n c.Manufactured by S Ο LAREVA RC02B ( 0.45^ m ) -34- 201132499 Lamination step: l5〇°C (vacuum for 5 minutes, vacuum pressurization for 15 minutes) Measurement conditions) Device: TENSILON Toyo BALDWIN RTM-1 00 Peeling speed: 200 mm/min Peeling angle: 180 ° (7) Moisture resistance The obtained heat-resistant white polyester film for solar cells is at a high temperature. It was placed in a high-humidity tank at 1000 ° C and 85% RH for 1000 hours. Next, an easy-adhesive white polyester film for a solar cell was taken out and left to stand at room temperature for 24 hours under normal humidity. Thereafter, the peel strength was measured in the same manner as in the above (4), and classified according to the following criteria: ◎ : 100 N/2 0 mm or more, or the material of the film was broken; 〇: 75 N/20 mm or more and less than 100 N/20 mm: △ : 50 N/20 mm or more and less than 75 N/20 mm; X: less than 50 N/20 mm. (Polymerization of urethane resin A-1 having an aliphatic polycarbonate polyol as a constituent component), a mixer, a Dimroth condenser, a nitrogen gas introduction tube, a ruthenium gel drying tube, and In a four-necked flask of a thermometer, 43.75 parts by mass of 4,4-diphenylmethane diisocyanate, 12.85 parts by mass of dimethylolbutanoic acid, and 153.4 parts by mass of a polycarbonate having a number average molecular weight of 2,000 were fed. Methyl diol, 0.03 parts by mass of butyl laurate butyl-35-201132499 tin, and 84.00 parts by mass of acetone as a solvent, stirred under nitrogen atmosphere at 75 ° C for 3 hours' and confirmed reaction The liquid has reached the desired amine equivalent. Next, after the reaction liquid was cooled to 40 ° C, 8.77 parts by mass of triethylamine was added to obtain a polyurethane prepolymer solution. Next, in a reaction vessel equipped with a high-speed disperser capable of high-speed stirring, 450 g of water was fed to adjust to 251: while stirring and mixing at 2000 min·1, the polyurethane prepolymer solution was added thereto. Disperse water. Thereafter, a portion of acetone and water was removed under reduced pressure to prepare a water-soluble polyurethane resin solution (A-1) having a solid content of 35%. The glass transition point temperature of the obtained polyurethane resin (A-1) was -30 °C. (Polymerization of urethane resin A-2 having an aliphatic polycarbonate polyol as a constituent component) A four-neck equipped with a stirrer, a Daimler condenser, a nitrogen gas introduction tube, a hydrazine gel drying tube, and a thermometer In the flask, 29.14 parts by mass of 4,4-diphenylmethane diisocyanate, 7.57 parts by mass of dimethylolbutanoic acid, and 17.3 parts by mass of polyhexamethylene carbonate having a number average molecular weight of 3,000 were fed. The diol, 0.03 parts by mass of butyltin dilaurate, and 84.00 parts by mass of acetone as a solvent are stirred under a nitrogen atmosphere at 75 ° C for 3 hours, and it is confirmed that the reaction liquid has reached the desired amine equivalent. . Next, after the reaction liquid was cooled to 40 ° C, 5 · 17 parts by mass of triethylamine was added to obtain a polyurethane prepolymer solution. Next, 'in a reaction vessel equipped with a high-speed disperser capable of high-speed stirring, feed 450 g of water, adjust to 25 ° C, and mix and mix with 2000 min · 1 while adding polyamine A · 36- 201132499 acid ester The prepolymer solution was water-dispersed. Thereafter, a portion of acetone and water was removed under reduced pressure to prepare a water-soluble polyurethane resin solution (A-2) having a solid content of 35 %. (Polymerization of urethane resin A-3 having an aliphatic polycarbonate polyol as a constituent component) A four-neck equipped with a stirrer, a Dairy condenser, a nitrogen gas introduction tube, a hydrazine gel drying tube, and a thermometer In the flask, 43.7 parts by mass of 4,4-diphenylmethane diisocyanate, 11.12 parts by mass of dimethylolbutanoic acid, 1.97 parts by mass of hexanediol, and 143.40 parts by mass of the number average molecular weight of 2000 were fed. Polyhexamethylene carbonate diol, 0.03 parts by mass of butyltin dilaurate, and 8.00 parts by mass of acetone as a solvent were stirred under a nitrogen atmosphere at 75 ° C for 3 hours, and the reaction solution was confirmed. I have reached the desired amine equivalent. Next, after the reaction liquid was cooled to 40 ° C, 8.77 parts by mass of triethylamine was added to obtain a polyurethane prepolymer solution. Next, in a reaction vessel equipped with a high-speed disperser capable of high-speed stirring, 450 g of water is fed, adjusted to 25 ° C, and stirred while mixing at 2000 min·1, and added to the polyurethane prepolymer solution. And water is dispersed. Thereafter, a portion of acetone and water was removed under reduced pressure to prepare a water-soluble polyurethane resin solution (A_3) having a solid content of 35%. (Polymerization of a stanol group-containing urethane resin A-4 having an aliphatic polycarbonate polyol as a constituent component) A stirrer, a Daimler condenser, a nitrogen gas introduction tube, a ruthenium gel drying tube, And a four-necked flask of a thermometer, fed with 3 8 · 4 1 parts by weight of isophora-37-201132499 keto diisocyanate, 6.95 parts by mass of dimethylolpropionic acid, and 158.99 parts by mass of a number average molecular weight of 2000 Hexamethylene carbonate diol, 0.03 parts by mass of butyltin dilaurate, and 84.00 parts by mass of acetone as a solvent were stirred under a nitrogen atmosphere at 75 ° C for 3 hours, and it was confirmed that the reaction liquid had reached the The desired amine equivalent. Next, 'the reaction liquid was cooled to 4 (after TC, 4.37 parts by mass of triethylamine was added to obtain a polyurethane prepolymer solution. Secondly, 3 to 84 parts by mass of r-(amino group B) was added. Aminopropyltriethoxydecane, 1.8 parts by mass of 2-[(2-aminoethyl)amino]ethanol and 450 g of water, and added dropwise to the polyurethane prepolymer The solution is water-dispersed. Thereafter, by removing a part of acetone and water under reduced pressure, a water-soluble urethane-containing polyurethane resin solution having a solid content of 30% is prepared (A) -4) (Polymerization of urethane resin A-5 having an aliphatic polycarbonate polyol as a constituent) except for the number average molecular weight of the water-soluble polyurethane resin (A-1) The carbonic acid polyamine having a solid content of 35% was obtained in the same manner except that the hexamethylene carbonate diol of 2000 was changed to the hexamethylene carbonate diol having a number average molecular weight of 1 Å. Carbamate resin solution (A-5). Aminocarboxylic acid having an aliphatic polycarbonate polyol as a constituent component Polymerization of Resin A-6) In addition to changing the number average molecular weight of the water-soluble polyurethane resin (A-1) to hexamethylene carbonate diol of 2,000 - 38 - 201132499 In addition to the hexamethylene carbonate diol of 0, the other water-soluble polyurethane resin (A-6) having a solid content of 35% was obtained by the same method. A-7 of the urethane resin of the component, except that the amount of the water-soluble polyurethane resin (A-1) is changed to a quantity average amount of hexamethylene carbonate diol of 2000 In addition to the polyester diol of 2000, the other method is to obtain a water-soluble polyurethane resin solution (A-7) having a body composition of 35% (the amine group with the polyether polyol as a constituent component). A-8 of the acid ester resin, except that the amount of the water-soluble polyurethane resin (A-1), the amount of the carbonic acid hexamethylene glycol diol is changed to a polyether number of 2000 In addition to the alcohol, the other method is to obtain a water-soluble polyurethane resin solution (A-8) having a body composition of 35% ( Aliphatic polycarbonate polyol as the polymerization of the resin component constituting the urethane of A-9)

在配備攪拌機、戴氏冷凝器、氮氣導入管、矽凝 燥管、及溫度計之四頸燒瓶中’飼入32.39質量份之 雙(異氰酸酯基甲基)環己烷、13.09質量份之二羥甲 酸、156.74質量份之數量平均分子量爲2000之聚碳酸 甲酯二醇、0.03質量份之二月桂酸丁基錫、及80.89 份之作爲溶劑的丙酮,在氮氣之氣體環境下且在75 °C 的方 溶液 聚合 均分 分子 得固 〇 聚合 均分 分子 得固 0 酸酯 膠乾 1,3- 基丁 六亞 質量 攪拌 -39- 201132499 3小時’並加以確認反應液已達到吾所欲之胺 ,將該反應液降溫至40 °C後,添加入8.77質量 胺,以獲得聚胺基甲酸酯預聚物溶液。其次, 速攪拌的高速分散機之反應容器中,飼入450 整成25°C而一邊以SOOOmin·1攪拌混合,一邊 基甲酸酯預聚物溶液而加以水分散。其後,藉 移除丙酮及水之一部分,以調製得固體成份爲 性聚胺基甲酸酯樹脂溶液(A-9 )。所獲得聚胺 脂(A-9)之玻璃轉移點溫度爲-30°C。 (以脂肪族系聚碳酸酯多元醇作爲構成成分之 樹脂A-10之聚合) 在配備攪拌機、戴氏冷凝器、氮氣導入管 燥管、及溫度計之四頸燒瓶中,飼入45.93質 二環己基二異氰酸酯、13.09質量份之二羥 23 5.1 1質量份之數量平均分子量爲3 000之聚 酯二醇、0.03質量份之二月桂酸丁基錫、及11 之作爲溶劑的丙酮,在氮氣之氣體環境下1在 小時,並加以確認反應液已達到吾所欲&amp; @胃 將該反應液降溫至4(TC後,添加入8.77質量份 ,以獲得聚胺基甲酸酯預聚物溶液。其次’在 攪拌的高速分散機之反應容器中,飼A 450 &amp; 成25 °C而一邊以2000 min·1攪拌混合’一邊 '添 甲酸酯預聚物溶液而加以水分散。其後’藉由 當量。其次 份之三乙基 在配備可高 克之水,調 添加入聚胺 由在減壓下 35%之水溶 基甲酸酯樹 胺基甲酸酯 、矽凝膠乾 量份之4,4-甲基丁酸、 碳酸六亞甲 7.6 6質量份 7 5 °C攪拌3 量。其次, 之三乙基胺 配備可高速 之水,調整 加入聚胺基 在減壓下移 -40- 201132499 除丙酮及水之一部分,以調製得固體成份爲 聚胺基甲酸酯樹脂溶液(A-1 0 )。所獲得聚 脂(A-10)之玻璃轉移點溫度爲-40°C。 (封端型聚異氰酸酯交聯劑之聚合) 在配備攪拌機、溫度計、回流冷卻管之 100質量份之以六亞甲基二異氰酸酯作爲原 聚氰酸酯結構之聚異氰酸酯化合物(旭化 Asahi Kasei Chemicals Corporation)製造、 )、55質量份之醋酸丙二醇一甲基醚酯、30 二醇一甲基醚(平均分子量 750)在氮氣之 在70°C保持4小時。其後,將反應液溫度降 滴加入4 7質量份之甲基乙基酮肟。測定反應 譜而加以確認異氰酸酯基之吸收已消失,以 爲75質量%之封端型聚異氰酸酯水分散液( (噚唑啉系交聯劑之聚合) 在配備溫度計、氮氣導入管、戴氏冷凝 、及攪拌機之燒瓶中,飼入作爲水性媒介的 子交換水與5 8質量份之異丙醇之混合物、及 合引發劑(2,2’-偶氮雙(2-脒基丙烷)•二 另一方面,在滴液漏斗飼入16質量份之具有 異丙烯基-2-曙唑啉作爲聚合性不飽和單體、 丙烯酸甲氧基乙二醇酯(乙二醇之平均加成 耳、新中村化學工業公司(Shin-Nakamura 3 5 %之水溶性 胺基甲酸酯樹 燒瓶中,飼入 料的具有異三 成工業公司( Duranate TP A 質量份之聚乙 氣體環境下且 至5 0 °C,並逐 液之紅外線光 獲得固體成份 B )。 器、滴液漏斗 5 8質量份之離 4質量份之聚 鹽酸鹽)。在 噚唑啉基之2-32質量份之聚 莫耳數· 9莫 Chemical Co. -41 - 201132499In a four-necked flask equipped with a stirrer, a Dairy condenser, a nitrogen inlet tube, a sputum drying tube, and a thermometer, '32.39 parts by mass of bis(isocyanatemethyl)cyclohexane, 13.09 parts by mass of dihydroxycarboxylic acid were fed. 156.74 parts by mass of a polymethyl carbonate diol having a number average molecular weight of 2000, 0.03 parts by mass of butyltin dilaurate, and 80.89 parts of acetone as a solvent, in a nitrogen atmosphere and a solution at 75 ° C Polymerization is divided into molecules to obtain a solid-state polymerization, and the molecular weight of the solid is 0. The acid ester is dry and the 1,3- butyl hexaethylene mass is stirred -39-201132499 for 3 hours' and it is confirmed that the reaction liquid has reached the desired amine. After the reaction solution was cooled to 40 ° C, 8.77 mass of an amine was added to obtain a polyurethane prepolymer solution. Next, in a reaction vessel of a high-speed disperser which is rapidly stirred, 450 parts of the mixture was fed at 25 ° C, and the mixture was stirred and mixed with SOOOmin·1, and the urethane prepolymer solution was water-dispersed. Thereafter, a part of acetone and water were removed to prepare a solid polyurethane urethane resin solution (A-9). The glass transition point temperature of the obtained polyurethane (A-9) was -30 °C. (Polymerization of Resin A-10 with Aliphatic Polycarbonate Polycarbonate as a Component) In a four-necked flask equipped with a stirrer, a Dairy condenser, a nitrogen introduction tube, and a thermometer, 45.93 bicyclic rings were fed. Hexyl diisocyanate, 13.09 parts by mass of dihydroxy 23, 51 parts by mass of a polyester diol having a number average molecular weight of 3,000, 0.03 parts by mass of butyltin dilaurate, and 11 of acetone as a solvent in a gaseous atmosphere of nitrogen The next 1 hour, and confirm that the reaction solution has reached my desired &amp; @ stomach, the reaction solution is cooled to 4 (TC, added to 8.77 parts by mass to obtain a polyurethane prepolymer solution. 'In a reaction vessel of a stirred high-speed disperser, feed A 450 &amp; at 25 ° C while stirring and mixing the 'one-side' ester prepolymer solution at 2000 min·1 for water dispersion. Equivalent. The third portion of the triethyl group is added with water of high gram, and the polyamine is added to the polyamine by 35% under water pressure, and the dry weight of the gel is 4, 4-methylbutyric acid, hexamethylene carbonate 7.6 6 parts by mass 7 Stir 3 at 5 °C. Secondly, triethylamine is equipped with high-speed water, adjust the addition of polyamine group under reduced pressure to remove -40-201132499, except acetone and water, to prepare the solid component as polyamine. Formate resin solution (A-1 0 ). The glass transition point temperature of the obtained polyester (A-10) is -40 ° C. (Polymerization of blocked polyisocyanate crosslinker) Equipped with a mixer, thermometer, 100 parts by mass of hexamethylene diisocyanate as a polyisocyanate compound of the original polycyanate structure (manufactured by Asahi Kasei Chemicals Corporation), 55 parts by mass of propylene glycol monomethyl ether acetate, 30 diol monomethyl ether (average molecular weight 750) was maintained at 70 ° C for 4 hours under nitrogen. Thereafter, the temperature of the reaction liquid was dropped dropwise to 47 parts by mass of methyl ethyl ketone oxime. The reaction spectrum was measured to confirm that the absorption of the isocyanate group had disappeared, and that 75 mass% of the blocked polyisocyanate aqueous dispersion (polymerization of the oxazoline-based crosslinking agent) was equipped with a thermometer, a nitrogen gas introduction tube, and a Deer condensation. And a mixer flask, fed with a mixture of sub-exchange water as an aqueous medium and 58 parts by mass of isopropyl alcohol, and a combined initiator (2,2'-azobis(2-amidinopropane)•two other On the one hand, 16 parts by mass of isopropenyl-2-oxazoline as a polymerizable unsaturated monomer, methoxyethyl acrylate (ethylene glycol acrylate), new in the dropping funnel Nakamura Chemical Industry Co., Ltd. (Shin-Nakamura 35% water-soluble urethane bottle flask, the feed material has a different industrialization company (Duranate TP A parts by mass of polyethylene gas and up to 50 °C) And the solid component B) is obtained by liquid-infrared light. The apparatus and the dropping funnel are 5 parts by mass of 4 parts by mass of the polyhydrochloride salt. The polymole of 2-32 parts by mass of the oxazoline group. · 9 Mo Chemical Co. -41 - 201132499

Ltd.)製造)、及32質量份之甲基丙烯酸甲酯的混合物, 在氮氣之氣體環境下且在7(TC逐滴加入歷時1小時。逐滴 加入結束後,將反應溶液攪拌9小時並加以冷卻,以獲得 固體成份濃度爲40質量%之具有噚唑啉基之水溶性樹脂溶 液(C )。 (碳化二亞胺系交聯劑之聚合) 在配備攪拌機、溫度計、回流冷卻管之燒瓶中,飼入 168質量份之六亞甲基二異氰酸酯與220質量份之聚乙二 醇一甲基醚(M400、平均分子量400),在120°C攪拌1 小時,並且,加入26質量份之4,4’-二環己基甲烷二異氰 酸酯與3.8質量份(相對於全部異氰酸酯爲2重量%)之 3-甲基-1-苯基-2-膦-1-氧化物作爲碳化二亞胺化觸媒,在 氮氣流下在1 8 5 t再攪拌5小時。測定反應液之紅外線光 譜,加以確認波長2200至23 00 cnT1之吸收已消失。自然 冷卻至6(TC,加入56 7質量份之離子交換水,以獲得固體 成份爲40質量%之碳化二亞胺水溶性樹脂溶液(D )。 〔實施例1〕 (1 )塗布液之調製 將下述之塗布劑加以混合以製造塗布液。 5 5 . 8 6質量% 3 0.0 0質量% 1 3 . 5 2質量% 0.5 9質量% • 水 • 異丙醇 • 聚胺基甲酸酯樹脂溶液(A-1 ) • 粒子 -42- 201132499 (平均粒徑40nm之矽溶膠、固體成份 濃度4 0質量% ) 界面活性劑 0.03質量°/〇 (矽系、固體成份濃度1 00質量% ) (2)太陽能電池用易接著性聚酯薄膜之製造 將作爲薄膜原料高分子之含有〇·〇3質量%之平均粒徑 爲2.5 // m的二氧化矽粒子之PET樹脂九粒(固有黏度爲 0.62 dl/g)在133 Pa之減壓下、在135°C進行乾燥6小時 。其後,供應至擠壓機在約285 °C進行熔融。將該PET樹 脂分別以不銹鋼燒結體濾材(標稱過濾精度爲1 0 M m粒子 截止9 5 % )加以過濾,並加以熔融擠出成薄片狀。在表面 溫度保持於30°C之旋轉冷卻金屬輥上使其驟冷密著固化’ 以獲得未延伸PET薄片。 將該未延伸PET薄片以經加熱的輥群及紅外線加熱器 加熱至1 〇〇°C,其後則以具有周速差之輥群朝長度方向加 以延伸3.5倍,以獲得單軸向延伸PET薄膜。 其次,以輥式塗布法在PET薄膜之單面塗布塗布液後 ,在80°C乾燥20秒鐘。另外,塗布量是加以調整成使得 經最終(經雙軸向延伸後)乾燥後之塗布量爲0. 1 5 g/m2 ( 乾燥後之塗布層厚度爲150 nm)。接著,以拉幅機在120 °C朝寬度方向加以延伸4.0倍,並在固定薄膜之寬度方向 的長度狀態下,在230 °C加熱0.5秒鐘,並且在1〇〇艺歷時 10秒鐘進行3 %之寬度方向的鬆弛處理,以獲得250//m之 太陽能電池用易接著性聚酯薄膜。評估結果如表1所示。 -43- 201132499 〔實驗例1〕 除了將聚胺基甲酸酯樹脂變更爲聚胺基甲酸酯樹脂( A- 5 )以外’其餘則以與實施例i相同的方式而獲得太陽能 電池用易接著性聚酯薄膜。 〔實驗例2〕 除了將聚胺基甲酸酯樹脂變更爲聚胺基甲酸酯樹脂( A-6 )以外’其餘則以與實施例1相同的方式而獲得太陽能 電池用易接著性聚酯薄膜。 〔比較例1〕 除了將聚胺基甲酸酯樹脂變更爲聚胺基甲酸酯樹脂( A- 7 )以外,其餘則以與實施例1相同的方式而獲得太陽能 電池用易接著性聚酯薄膜。 〔比較例2〕 除了將聚胺基甲酸酯樹脂變更爲聚胺基甲酸酯樹脂( A- 8 )以外,其餘則以與實施例1相同的方式而獲得太陽能 電池用易接著性聚酯薄膜。 〔比較例3〕 除了將太陽能電池用易接著性聚酯薄膜之基材厚度變 更爲5 # m以外,其餘則以與實施例1相同的方式而獲得太 陽能電池用易接著性聚酯薄膜。 -44 - 201132499 〔實施例2〕 除了將聚胺基甲酸酯樹脂變更爲聚胺基甲酸醋樹脂( A-2 )以外,其餘則以與實施例〗相同的方式而獲得太陽能 電池用易接著性聚酯薄膜。 〔實施例3〕 除了將聚胺基甲酸酯樹脂變更爲聚胺基甲酸酯樹脂( A-3 )以外,其餘則以與實施例丨相同的方式而獲得太陽能 電池用易接著性聚酯薄膜。 〔實施例4〕 除了將聚胺基甲酸酯樹脂變更爲含有矽烷醇基之聚胺 基甲酸酯樹脂(A - 4 )以外,其餘則以與實施例1相同的方 式而獲得太陽能電池用易接著性聚酯薄膜。 〔實施例5〕 除了將太陽能電池用易接著性聚酯薄膜之基材厚度變 更爲50 ^ m以外,其餘則以與實施例1相同的方式而獲得 太陽能電池用易接著性聚酯薄膜。 〔實施例6〕 除了將太陽能電池用易接著性聚酯薄膜之基材厚度變 更爲1 0 0 e m以外,其餘則以與實施例1相同的方式而獲得 太陽能電池用易接著性聚酯薄膜。 〔實施例7〕 除了將太陽能電池用易接著性聚酯薄膜之基材厚度變 更爲3 5 0 a m以外,其餘則以與實施例1相同的方式而獲得 太陽能電池用易接著性聚酯薄膜。 -45- 201132499 〔實施例8〕 除了將塗布液變更爲下述以外,其餘 相同的方式而獲得太陽能電池用易接著性 • 水 • 異丙醇 • 聚胺基甲酸酯樹脂溶液(A-1 ) • 粒子 (平均粒徑40nm之矽溶膠、固體成伤 濃度4 0質量% ) • 界面活性劑 (矽系、固體成份濃度100質量%) 〔實施例9〕 除了將塗布液變更爲下述以外,其餘 相同的方式而獲得太陽能電池用易接著性 • 水 • 異丙醇 • 聚胺基甲酸酯樹脂溶液(A-1 ) • 粒子 (平均粒徑40 nm之矽溶膠、固體成任 濃度40質量%) • 界面活性劑 (矽系、固體成份濃度1〇〇質量%) 〔實施例1 〇〕 (3 )太陽能電池用背板之製造 則以與實施例1 聚酯薄膜。 6 1 · 5 1 質量。/。 3 0.0 0質量% 8 _ 1 1質量% 〇 · 3 5質量% 0.03 質量 〇/0 則以與實施例1 聚酯薄膜。 4 1 · 7 1質量% 3 0.00質量% 2 7.0 5質量% 1 · 1 8質量% 0.06質量% -46- 201132499 以實施例1之太陽能電池用易接著性聚酯I 酯薄膜(50//m) /鋁箔(30#m) /聚氟乙烯薄 )之構成,且以乾式積層法加以接著而獲得太 背板。 乾式積層用接著劑 TAKELAC A-315(三阱化學公司(Mitsui Inc.)製造)/ΤΑΚΕΝΑΤΕ A-10(三畊化學公司| (固體成份比) 〔實施例1 1〕 除了將聚胺基甲酸酯樹脂變更爲聚胺基甲 A-9 )以外,其餘則以與實施例1相同的方式而 電池用易接著性聚酯薄膜。 〔實施例1 2〕 除了將聚胺基甲酸酯樹脂變更爲聚胺基甲 A-1 0 )以外,其餘則以與實施例1相同的方式 能電池用易接著性聚酯薄膜。 〔實施例1 3〕 (3 )太陽能電池用背板之製造 以實施例1 1之太陽能電池用易接著性聚! 聚酯薄膜(50/zm) /鋁箔(3〇Am) /聚氟乙烯 m)之構成,且以乾式積層法加以接著而獲得太 背板。 ί膜/白色聚 膜(3 8仁m 昜能電池用 Chemicals, 这造)=9/1 酸酯樹脂( 獲得太陽能 酸酯樹脂( 而獲得太陽 眉薄膜/白色 薄膜(38 μ 陽能電池用 -47- 201132499 乾式積層用接著劑 T AKELAC A-3 1 5 (三阱化學公司製造)/τ AKEN ATE A-10 (三哄化學公司製造)=9/1(固體成份比) 就實施例1 〇、及實施例1 3之太陽能電池用背板以太 陽能電池用易接著性聚酯薄膜面作爲照射面,使用岩崎電 氣股份有限公司(Iwasaki Electric Co·,Ltd.)製造之EYE Super UV Tester SUV-W151 &gt; 在 6 3 °C、5 0 % R H、照射強度 爲100m W/cm2下進行100小時之連續UV照射處理》在螢 光燈下以目視確認經UV照射後之太陽能電池背板結果, 在實施例1 0之太陽能電池用背板雖然觀察到少許黃變,在 實施例13之太陽能電池用背板卻在全面並無色的變化而 保持良好的外觀。 、 -48- 201132499 ^ 1-1 1-^ 0.51 1.64 1 1 1.17 1.34 1.12 1.05 τ-Η 1.15 1.13 寸 1.18 1.17 1.20 1.38 1.20 EVA接著性 B.快速固化型 I-H 耐濕熱性 〇 X &lt; X X X 〇 〇 〇 〇 〇 〇 〇 〇 〇 〇 〇 〇 接著性 ◎ 〇 ◎ &lt; &lt;3 &lt; ◎ ◎ ◎ 〇 〇 ◎ ◎ ◎ ◎ ◎ ◎ ◎ Η-Μ 耐濕熱性 ◎ X &lt; X X X ◎ ◎ ◎ 〇 ◎ ◎ 〇 ◎ ◎ ◎ ◎ ◎ 接著性 ◎ ◎ ◎ 〇 ◎ &lt;] ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ A.標準固化型 ΗΗ 耐濕熱性 ◎ X &lt;3 X &lt; 0 ◎ ◎ ◎ 〇 ◎ ◎ 〇 ◎ ◎ ◎ ◎ ◎ 接著性 ◎ ◎ ◎ ◎ ◎ 〇 ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ΗΗ 耐濕熱性 ◎ X &lt;] X &lt; ◎ ◎ ◎ 〇 ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ 接著性 ◎ ◎ ◎ ◎ ◎ 〇 ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ 實施例1 實驗例1 實驗例2 比較例1 比較例2 比較例3 實施例2 實施例3 實施例4 實施例5 實施例6 實施例7 實施例8 實施例9 實施例10 實施例11 實施例12 實施例13 |6寸, 201132499 〔實施例1 4〕 (1 )塗布液之調製 將下述之塗布劑加以混合以製造塗布液。 • 水 5 5 · 8 6質量% • 異丙醇 30.00質量% • 聚胺基甲酸酯樹脂溶液(A-1 ) 13.52質量% • 粒子 0 · 5 9質量% (平均粒徑40 urn之矽溶膠、固體成份 濃度40質量% ) •界面活性劑 0.0 3質量% (矽系、固體成份濃度100質量%) (2)太陽能電池用易接著性白色聚酯薄膜之製造 (空洞顯現材a ) 將60質量%之聚甲基戊烯樹脂、20質量%之聚丙烯樹 脂及20質量%之聚苯乙烯樹脂加以九粒混合後,供應至經 溫調成2 8 5 °C的排氣式雙螺桿擠壓機加以捏合以製造空洞 形成劑(原料a )。 (聚酯b ) 以慣用方法聚合含有二氧化矽粒子之聚對苯二甲酸乙 二醇酯樹脂’以製造含有500 ppm之凝集二氧化矽粒子( 平均粒徑爲2.〇βιη)的固有黏度爲〇.62dl/g之聚對苯二甲 酸乙二醇酯(原料b )。 -50- 201132499 (含有氧化鈦粒子之母粒原料c) 上述聚對苯二甲酸乙二醇酯(原料b)與平均粒徑爲 0.2 // m之銳鈦礦型二氧化鈦粒子(堺化學工業股份有限公 司(Sakai Chemical Industry Co.,Ltd.)製造)以質量比 5 0/5 0混合,並以排氣式捏合擠壓機加以捏合,以製造含有 二氧化鈦粒子之母粒原料(原料c )。 (薄膜之製造) 將經在加熱下施加真空乾燥的前述原料加以連續計量 •連續攪拌成爲a/b/c = 8/82/10(質量比)而作爲A層之 原料。其次,將該原料供應至擠壓機進行熔融捏合,並經 由過濾器而供應至進料分流套管(共擠壓接合器)。 在另一方面,B層之原料則使用將前述原料加以連續 計量成爲b/c== 80/20 (質量比)者,供應至排氣式雙螺桿 擠壓機進行熔融捏合,並經由過濾器而供應至進料分流套 管。 在進料分流套管,將前述B層在前述A層之兩面接合 成爲相同之厚度。此時,將供應至A層及B層之樹脂吐出 量加以控制使得延伸前各層之厚度比率成爲B/A/B = 1 0 / 8 0 /1 0 ’並流延於表面溫度爲3 0 °C之冷卻轉筒上以製造 厚度爲2.4mm之未延伸薄膜。此時,對擠出於冷卻轉筒上 的熔融高分子之相反面吹送10 °C之空氣以使熔融高分子從 兩面進行冷卻•固化。 -51 - 201132499 其次,經以前述方法所獲得未延伸薄膜使用加熱輥加 熱至65 °C後,以周速不相同的輥間加以延伸3.2倍。此時 ,在低速輥與高速輥之中間部,在隔著薄膜而面對面之位 置設置集光紅外線加熱器,以由薄膜之兩面均等地施加爲 均勻地延伸薄膜所需要之充分的熱量。 其次,以輥式塗布法在PET薄膜之單面塗布前述塗布 液後,在80°C乾燥20秒鐘。另外,塗布量是加以調整成 使得經最終(經雙軸向延伸後)乾燥後之塗布量爲0.15 g/m2 〇 接著,導入於拉幅機,一邊加熱升溫成12(TC至150 °C 一邊朝寬度方向加以延伸3.9倍。並且,在拉幅機內吹 上22 0°C之熱風歷時30秒鐘而施加熱處理。其後,一邊緩 慢地冷卻至室溫歷時40秒鐘一邊朝寬度方向施加2%之鬆 弛處理,以獲得視密度爲1.10g/cm3、厚度爲250/zm之含 有空洞之積層雙軸向配向之太陽能電池用易接著性白色聚 酯薄膜。評估結果如表2所示。 〔實施例1 5〕 除了將聚胺基甲酸酯樹脂變更爲聚胺基甲酸酯樹脂( A-2 )以外,其餘則以與實施例1 4相同的方式而獲得太陽 能電池用易接著性白色聚酯薄膜。 〔實施例1 6〕 除了將聚胺基甲酸酯樹脂變更爲聚胺基甲酸酯樹脂( A- 3 )以外,其餘則以與實施例i 4相同的方式而獲得太陽 能電池用易接著性白色聚酯薄膜。 -52- 201132499 〔實施例1 7〕 除了將聚胺基甲酸酯樹脂變更爲含有矽烷醇基之聚胺 基甲酸酯樹脂(A-4 )以外,其餘則以與實施例1 4相同的 方式而獲得太陽能電池用易接著性白色聚酯薄膜。 〔實施例1 8〕 除了將聚胺基甲酸酯樹脂變更爲聚胺基甲酸酯樹脂( A-9 )以外,其餘則以與實施例1 4相同的方式而獲得太陽 能電池用易接著性聚酯薄膜。 〔實施例1 9〕 除了將聚胺基甲酸酯樹脂變更爲聚胺基甲酸酯樹脂( A- 1 0 )以外,其餘則以與實施例1 4相同的方式而獲得太陽 能電池用易接著性聚酯薄膜。 -53- 201132499 (N撇 色調 Η 〇; Γ-; Τ—^ 1&gt; c3 〇 »〇 〇 〇 〇 〇 〇 .-1 95.6 95.8 ㈣ 95.8 95.4 褂Ο 1.17 1.34 CN Η 1.05 1.20 1.38 EVA接著性 B.快速固化型 t—j 耐濕熱性 〇 〇 〇 〇 〇 〇 接著性 ◎ ◎ ◎ ◎ ◎ ◎ 耐濕熱性 ◎ ◎ ◎ ◎ ◎ ◎ 接著性 ◎ ◎ ◎ ◎ ◎ ◎ A.標準固化型 耐濕熱性 ◎ ◎ ◎ ◎ ◎ ◎ 接著性 ◎ ◎ ◎ ◎ ◎ ◎ μ-Η 耐濕熱性 ◎ ◎ ◎ ◎ ◎ ◎ 接著性 ◎ ◎ ◎ ◎ ◎ ◎ 實施例14 實施例15 實施例16 實施例17 實施例18 實施例19 201132499 〔實施例2 Ο〕 (1 )塗布液之調製 將下述之塗布劑加以混合以製造塗布液。 5 5.6 2質量% 3 0 . 〇 〇質量% 1 1.2 9質量% 2.2 6質量% 〇 . 7 1質量% • 水 • 異丙醇 • 聚胺基甲酸酯樹脂溶液(A- 1 ) • 封端型聚異氰酸酯水分散液(B) • 粒子 (平均粒徑40 nm之矽溶膠、固體成份 濃度40質量% ) • 粒子 0.0 7質量% (平均粒徑450 nm之矽溶膠、固體成 份濃度40質量% ) • 界面活性劑 0.0 5質量% (矽系、固體成份濃度1 〇〇質量% ) (2 )太陽能電池用易接著性聚酯薄膜之製造 將作爲薄膜原料高分子之含有〇.〇3質量%之平均粒徑 爲2.5;zm的二氧化矽粒子之PET樹脂九粒(固有黏度爲 0.62 dl/g)在133 Pa之減壓下、在135°C進行乾燥6小時 。其後,供應至擠壓機在約2 8 5 t進行熔融。將該PET樹 脂分別以不銹鋼燒結體濾材(標稱過濾精度爲1 0 M m粒子 截止95% )加以過濾,並加以熔融擠出成薄片狀。在表面 溫度保持於30 °C之旋轉冷卻金屬輥上使其驟冷密著固化, 以獲得未延伸PET薄片。 -55- 201132499 將該未延伸P ET薄片以經加熱的輥群及紅外線加 加熱至100°c,其後則以具有周速差之輥群朝長度方 以延伸3.5倍,以獲得單軸向延伸PET薄膜。 其次,以輥式塗布法在PET薄膜之單面塗布前述 液後,在8 0 °C乾燥2 0秒鐘。另外,塗布量是加以調 使得經最終(經雙軸向延伸後)乾燥後之塗布量爲0.1 5 (乾燥後之塗布層厚度爲150nm)。接著,以拉幅機在 °C朝寬度方向加以延伸4.0倍,並在固定薄膜之寬度 的長度狀態下,在230 °C加熱0.5秒鐘,並且在100 °C 10秒鐘進行3%之寬度方向的鬆弛處理,以獲得250从 太陽能電池用易接著性聚酯薄膜。評估結果如表3所 〔實驗例3〕 除了將聚胺基甲酸酯樹脂變更爲聚胺基甲酸酯樹 A-5 )以外,其餘則以與實施例20相同的方式而獲得 能電池用易接著性聚酯薄膜。 〔實驗例4〕 除了將聚胺基甲酸酯樹脂變更爲聚胺基甲酸酯樹 A-6 )以外,其餘則以與實施例20相同的方式而獲得 能電池用易接著性聚酯薄膜。 〔比較例4〕 除了將聚胺基甲酸酯樹脂變更爲聚胺基甲酸酯樹 A-7 )以外,其餘則以與實施例20相同的方式而獲得 能電池用易接著性聚酯薄膜。 熱器 向加 塗布 整成 g/m2 :120 方向 歷時 m之 不 。 脂( 太陽 脂( 太陽 脂( 太陽 -56- 201132499 〔比較例5〕 除了將聚胺基甲酸酯樹脂變更爲聚胺基甲酸酯樹脂( A-8 )以外,其餘則以與實施例20相同的方式而獲得太陽 能電池用易接著性聚酯薄膜。 〔比較例6〕 除了將太陽能電池用易接著性聚酯薄膜之基材厚度變 更爲5#m以外,其餘則以與實施例20相同的方式而獲得 太陽能電池用易接著性聚酯薄膜。 〔實施例2 1〕 除了將塗布液變更爲下述以外,其餘則以與實施例20 相同的方式而獲得太陽能電池用易接著性聚酯薄膜。 5 8.0 2質量% 3 0 · 0 〇質量% 9.4 7質量% 1 . 8 9質量% 0 · 5 9質量% 水 異丙醇 聚胺基甲酸酯樹脂溶液(A-1 ) 封端型聚異氰酸酯水分散液(B) 粒子 (平均粒徑40 nm之矽溶膠、固體成份 濃度4 0質量% ) • 界面活性劑 0.03質量% (矽系、固體成份濃度1〇〇質量%) 〔實施例22〕 除了將塗布液變更爲下述以外’其餘則以與實施例20 相同的方式而獲得太陽能電池用易接著性聚酯薄膜。 -57- 201132499 5 4.7 5質量% 3 0.00 Μ Λ % 1 2 · 9 9質量% 1 . 5 2質量% 0.7 1質量% 0.0 3質量% 水 異丙醇 聚胺基甲酸酯樹脂溶液(A-1 ) 封端型聚異氰酸酯水分散液(B ) 粒子 (平均粒徑40 nm之矽溶膠、固體成份 濃度4 0質量% ) 界面活性劑 (矽系、固體成份濃度1 〇〇質量% ) 〔實施例2 3〕 除了將塗布液變更爲下述以外,其餘則以與實施例2 0 相同的方式而獲得太陽能電池用易接著性聚酯薄膜。 5 7.3 5質量% 3 0.00 Μ Μ % 8 . 1 2質量% 3.7 9質量% 0.7 1質量% 0.0 3 質量。/〇 水 異丙醇 聚胺基甲酸酯樹脂溶液(Α-1 ) 封端型聚異氰酸酯水分散液(Β ) 粒子 (平均粒徑40 nm之矽溶膠、固體成份 濃度4 0質量% ) 界面活性劑 (矽系、固體成份濃度1 〇〇質量% ) 〔實施例24〕 除了將塗布液變更爲下述以外,其餘則以與實施例2 0 相同的方式而獲得太陽能電池用易接著性聚酯薄膜。 -58- 201132499 水 異丙醇 聚胺基甲酸酯樹脂溶液(A-1 ) 封端型聚異氰酸酯水分散液(B ) 粒子 (平均粒徑40 nm之矽溶膠、固體成份 濃度40質量%) 界面活性劑 (矽系、固體成份濃度1〇〇質量% ) 5 9.9 5質量% 3 0 · 0 0質量% 3.2 5質量% 6.0 6質量% 0.7 1質量% 0.0 3質量% 實施例2 5 除了將塗布液變更爲下述以外,其餘則以與實施例20 相同的方式而獲得太陽能電池用易接著性聚酯薄膜。 水 6 0.8 2質量% 異丙醇 3 0.0 0質量% 聚胺基甲酸酯樹脂溶液(A-1 ) 1.6 2質量% 封端型聚異氰酸酯水分散液(B ) 6.8 2質量% 粒子 0.7 1質量% (平均粒徑40 nm之矽溶膠、固體成份 濃度40質量%) 界面活性劑 0.0 3質量% (矽系、固體成份濃度1〇〇質量% ) -59- 201132499 〔實施例26〕 除了將聚胺基甲酸醋樹脂變更爲聚胺基甲酸酯樹脂( A-2 )以外,其餘則以與實施例2 〇相同的方式而獲得太陽 能電池用易接著性聚酯薄膜。 〔實施例2 7〕 除了將聚胺基甲酸酯樹脂變更爲聚胺基甲酸酯樹脂( A-3 )以外,其餘則以與實施例2〇相同的方式而獲得太陽 能電池用易接著性聚酯薄膜。 〔實施例2 8〕 除了將聚胺基甲酸酯樹脂變更爲含有矽烷醇基之聚胺 基甲酸酯樹脂(A - 4 )以外,其餘則以與實施例2 〇相同的 方式而獲得太陽能電池用易接著性聚醋薄膜。 〔實施例29〕 除了將封端型聚異氰酸酯水分散液(B)變更爲具有噚 唑啉基之水溶性樹脂(C )以外,其餘則以與實施例2 〇相 同的方式而獲得太陽能電池用易接著性聚酯薄膜。 〔實施例3 0〕 除了將封端型聚異氰酸酯水分散液(C)變更爲碳化二 亞胺水溶性樹脂(D )以外,其餘則以與實施例20相同的 方式而獲得太陽能電池用易接著性聚酯薄膜。 〔實施例3 1〕 除了將封端型聚異氰酸酯水分散液(C)變更爲亞胺基 .羥甲基三聚氰胺(固體成份濃度7 〇質量% )以外,其餘 -60- 201132499 則以與實施例2 〇相同的方式而獲得太陽能電池用易接著 性聚酯薄膜。 〔實施例3 2〕 除了將太陽能電池用易接著性聚酯薄膜之基材厚度變 更50 /z m以外,其餘則以與實施例20相同的方式而獲得太 陽能電池用易接著性聚酯薄膜。 〔實施例3 3〕 除了將太陽能電池用易接著性聚酯薄膜之基材厚度變 更爲100 // m以外,其餘則以與實施例20相同的方式而獲 得太陽能電池用易接著性聚酯薄膜。 〔實施例3 4〕 除了將太陽能電池用易接著性聚酯薄膜之基材厚度變 吏爲350ym,其餘則以與實施例20相同的方式而獲得太 陽能電池用易接著性聚酯薄膜。 〔實施例3 5〕 除了將塗布液變更爲下述以外,其餘則以與實施例2 0 相同的方式而獲得太陽能電池用易接著性聚酯薄膜。 • 水 6 2.8 2質量% 3 0 · 0 0 質量。/〇 5.6 7質量% 1 . 1 3質量% 0.3 5質量% 異丙醇 聚胺基甲酸酯樹脂溶液(A-1 ) 封端型聚異氰酸酯水分散液(B ) 粒子 (平均粒徑40 nm之矽溶膠、固體成份 濃度40質量%) -61 - 201132499 • 界面活性劑 0. 〇 3質量% (矽系、固體成份濃度1 00質量% ) 〔實施例3 6〕 除了將塗布液變更爲下述以外’其餘則以與實施例20 相同的方式而獲得太陽能電池用易接著性聚酯薄膜。 • 水 45.99質量% • 異丙醇 30.00質量% • 聚胺基甲酸酯樹脂溶液(A-1 ) 18.99質量% • 封端型聚異氰酸酯水分散液(B) 3.80質量% • 粒子 1 · 1 9質量% (平均粒徑40 nm之矽溶膠、固體成份 濃度40質量%) • 界面活性劑 0.03質量% (矽系、固體成份濃度1 〇〇質量% ) 〔實施例3 7〕 (3 )太陽能電池用背板之製造 以實施例20之太陽能電池用易接著性聚酯薄膜/黑色 聚酯薄膜(50gm) /鋁箔(30#m) /聚氟乙烯薄膜(38/z m)之構成,且以乾式積層法加以接著而獲得太陽能電池用 背板。 乾式積層用接著劑 TAKELAC A-3 1 5 (三阱化學公司製造)/ΤΑΚΕΝΑΤΕ Α-10 (三畊化學公司製造)= 9/1 (固體成份比) 〔實施例3 8〕 -62- 201132499 除了將聚胺基甲酸酯樹脂變更爲聚胺基甲酸酯樹脂( A_9 )以外,其餘則以與實施例20相同的方式而獲得太陽 能電池用易接著性聚酯薄膜。 〔實施例3 9〕 除了將聚胺基甲酸酯樹脂變更爲聚胺基甲酸酯樹脂( A - 1 0 )以外,其餘則以與實施例2 0相同的方式而獲得太陽 能電池用易接著性聚酯薄膜。 〔實施例40〕 (3 )太陽能電池用背板之製造 以實施例3 8之太陽能電池用易接著性聚酯薄膜/黑色 聚酯薄膜(50ym) /鋁箔(30#m) /聚氟乙烯薄膜(38// m )之構成,且以乾式積層法加以接著而獲得太陽能電池用 背板。 乾式積層用接著劑 TAKELAC A-3 1 5 (三阱化學公司製造)/ΤΑΚΕΝΑΤΕ A-1 0 (三畊化學公司製造)=9Π (固體成份比) 就實施例37、及實施例40之太陽能電池用背板以太 陽能電池用易接著性聚酯薄膜面作爲照射面,使用岩崎電 氣股份有限公司製造之Eye Super UV Tester SUV-W151, 在6 3 °C、5 0 % RH、照射強度1 0 0 m W/cm2下進行1 0 0小時 之連續UV照射處理。在螢光燈下以目視確認經uv照射後 之太陽能電池背板之結果,實施例3 7之太陽能電池用背板 雖然觀察到少許黃變,但是實施例40之太陽能電池用背板 卻在全面並無色之變化而保持著良好的外觀。 -63- 201132499 «-〇 鹋§ 0.93 0.37 § 0.93 1.05 0.84 0.63 0.51 1.18 0.90 1.00 0.94 0.91 0.88 0.94 0.92 0.92 0.92 0.93 0.93 0.98 1.21 0.98 担 m is B.快速固化型 |-M 耐濕熱性 ◎ X &lt; X X X ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ 〇 ◎ 〇 〇 ◎ ◎ 〇 ◎ ◎ ◎ ◎ ◎ 接著性 ◎ 〇 ◎ &lt; ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ HH 耐濕熱性 ◎ X &lt; X X X ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ 〇 ◎ ◎ ◎ ◎ ◎ 接著性 ◎ ◎ ◎ 〇 ◎ &lt; ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ W | A.標準固化型 耐濕熱性 ◎ X &lt;] X ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ 〇 ◎ ◎ ◎ ◎ ◎ 接著性 ◎ ◎ ◎ ◎ ◎ 〇 ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ 耐濕熱性 ◎ X &lt;] X &lt;] &lt; ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ 〇 ◎ ◎ ◎ ◎ ◎ 1接著性 ◎ ◎ ◎ ◎ ◎ 〇 ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ 實施例20 | 實驗例3 | 實驗例4 比較例4 比較例5 I 比較例ό 實施例21 實施例22 實施例23 實施例24 實施例25 實施例26 實施例27 實施例28 實施例29 實施例30 實施例31 實施例32 實施例33 實施例34 實施例35 | 實施例36 | 實施例37 實施例38 實施例39 I 實施例40 -寸9丨 201132499 〔實施例4 1〕 (1 )塗布液之調製 將下述之塗布劑加以混合以製造塗布液。 5 5.6 2質量% 3 0.0 0質量% 1 1 . 2 9質量% 2.2 6質量% 0.7 1質量% • 水 • 異丙醇 • 聚胺基甲酸酯樹脂溶液(A-1) • 封端型聚異氰酸酯水分散液(B) • 粒子 (平均粒徑40 nm之矽溶膠、固體成份 濃度40質量%) • 粒子 0 · 0 7質量% (平均粒徑450 nm之矽溶膠、固體成 份濃度40質量% ) • 界面活性劑 0.05質量% (矽系、固體成份濃度1〇〇質量%) (2)太陽能電池用易接著性白色聚酯薄膜之製造 (空洞顯現材a ) 將60質量%之聚甲基戊烯樹脂、20質量%之聚丙烯樹 脂及20質量%之聚苯乙烯樹脂加以九粒混合後,供應至經 調溫成2 8 5 °C之排氣式雙螺桿擠壓機並進行捏合以製造空 洞形成劑(原料a )。 (聚酯b) 將含有二氧化矽粒子之聚對苯二甲酸乙二醇酯樹脂以 慣用方法加以聚合,以製造含有5 00 ppm之凝集二氧化矽 -65- 201132499 粒子(平均粒徑爲2.0ym)且固有黏度爲0.62dl/g之聚對 苯二甲酸乙二醇酯(原料b)。 (含有氧化鈦粒子之母粒原料c ) 上述聚對苯二甲酸乙二醇酯(原料b)與平均粒徑爲 〇. 2 /z m之銳鈦礦型二氧化鈦粒子(堺化學工業股份有限公 司製造)以質量比50/50混合,並以排氣式捏合擠壓機加 以捏合,以製造含有二氧化鈦粒子之母粒原料(原料c ) 〇 (薄膜之製造) 將經在加熱下施加真空乾燥的前述原料加以連續計量 •連續攪拌成爲a/b/c=8/82/10(質量比)而作爲A層之 原料。其次,將該原料供應至擠壓機進行熔融捏合,並經 由過濾器而供應至進料分流套管(共擠壓接合器) 在另一方面,B層之原料則使用將前述原料加以連續 計量成爲b/c= 80/20 (質量比)者,供應至排氣式雙螺桿 擠壓機進行熔融捏合,並經由過濾器而供應至進料分流套 管。 在進料分流套管,將前述B層在前述A層之兩面接合 成爲相同之厚度。此時,將供應至A層及B層之樹脂吐出 量加以控制使得延伸前各層之厚度比率成爲 B/A/B = 10/80/10,並流延於表面溫度爲30°C之冷卻轉筒上以製造 厚度爲2.4 mm之未延伸薄膜。此時,對擠出於冷卻轉筒上 的熔融高分子之相反面吹送1〇 °C之空氣以使熔融高分子從 兩面進行冷卻·固化。 -66- 201132499 其次,經以前述方法所獲得未延伸薄膜使用加熱輥加 熱至65°C後,以周速不相同的輥間加以延伸3.2倍。此時 ,在低速輥與高速輥之中間部,在隔著薄膜而面對面之位 置設置集光紅外線加熱器,以由薄膜之兩面均等地施加爲 均勻地延伸薄膜所需要之充分的熱量。 其次,以輥式塗布法在PET薄膜之單面塗布前述塗布 液後,在8 0°C乾燥20秒鐘。另外,塗布量是調整成爲經 最終(雙軸向延伸後)乾燥後之塗布量爲0.15 g/m2 (乾燥 後之塗布層厚度爲150 nm)。 接著,導入於拉幅機,—邊加熱升溫成12CTC至150 °C 一邊朝寬度方向加以延伸3.9倍》並且,在拉幅機內吹 上22 0 °C之熱風歷時30秒鐘而施加熱處理。其後,一邊緩 慢地冷卻至室溫歷時4 0秒鐘一邊朝寬度方向施加2 %之鬆 弛處理,以獲得視密度爲1.10g/cm3、厚度爲250/zm之含 有空洞之積層雙軸向配向之太陽能電池用易接著性白色聚 酯薄膜。評估結果如表4所示。 〔實施例42〕 除了將聚胺基甲酸酯樹脂變更爲聚胺基甲酸酯樹脂( A-2 )以外,其餘則以與實施例41相同的方式而獲得太陽 能電池用易接著性白色聚酯薄膜。 〔實施例43〕 除了將聚胺基甲酸酯樹脂變更爲聚胺基甲酸酯樹脂( A-3 )以外,其餘則以與實施例4 1相同的方式而獲得太陽 能電池用易接著性白色聚酯薄膜。 -67- 201132499 〔實施例44〕 除了將聚胺基甲酸酯樹脂變更爲含有矽烷醇基之聚胺 基甲酸酯樹脂(A-4 )以外,其餘則以與實施例41相同的 方式而獲得太陽能電池用易接著性白色聚酯薄膜。 〔實施例45〕 除了將聚胺基甲酸酯樹脂變更爲聚胺基甲酸醋樹脂( A - 9 )以外’其餘則以與實施例4 1相同的方式而獲得太陽 能電池用易接著性聚酯薄膜° 〔實施例46〕 除了將聚胺基甲酸酯樹脂變更爲聚胺基甲酸醋樹脂( A-1 0 )以外,其餘則以與實施例4 1相同的方式而獲得太陽 能電池用易接著性聚醋薄膜° -68- 201132499 寸撇 色調 Γ-; »—Η 1-H T-H C^; a ο in 〇 ο in o IT) o o 1 95.8 1 | 95.3 | 1 95.6 1 95.8 | 95.8 | 95.8 吸光度比率 1460/1530 0.93 1.15 1.05 0.84 0.98 1.21 EVA接著性 B.快速固化型 h—j 耐濕熱性 ◎ ◎ ◎ ◎ ◎ ◎ 接著性 ◎ ◎ ◎ ◎ ◎ ◎ KH 耐濕熱性 ◎ ◎ ◎ ◎ ◎ ◎ 接著性 ◎ ◎ ◎ ◎ ◎ ◎ A.標準固化型 j-H 耐濕熱性 ◎ ◎ ◎ ◎ ◎ ◎ 接著性 ◎ ◎ ◎ ◎ ◎ ◎ 耐濕熱性 ◎ ◎ ◎ ◎ ◎ ◎ 接著性 ◎ ◎ ◎ ◎ ◎ ◎ 實施例41 實施例42 實施例43 實施例44 實施例45 實施例46 _ 69丨 201132499 〔產業上之利用可能性〕 本發明之太陽能電池用易接著性聚酯薄膜,由於與封 止材之接著性及在高溫高濕下之接著性(耐濕熱性)優異 ,因此適合用作爲太陽能電池用背板之最內裝之基材薄膜 〇 【圖式簡單說明】 無。 【主要元件符號說明】 ίΚ 。 -70-(manufactured by Ltd.) and a mixture of 32 parts by mass of methyl methacrylate, under a nitrogen atmosphere and at 7 (TC dropwise addition for 1 hour. After the dropwise addition, the reaction solution was stirred for 9 hours and It is cooled to obtain a water-soluble resin solution (C) having an oxazoline group having a solid concentration of 40% by mass. (Polymerization of a carbodiimide crosslinking agent) A flask equipped with a stirrer, a thermometer, and a reflux cooling tube In the above, 168 parts by mass of hexamethylene diisocyanate and 220 parts by mass of polyethylene glycol monomethyl ether (M400, average molecular weight 400) were fed, and the mixture was stirred at 120 ° C for 1 hour, and 26 parts by mass was added. 4,4'-dicyclohexylmethane diisocyanate and 3.8 parts by mass (2% by weight based on total isocyanate) of 3-methyl-1-phenyl-2-phosphonium-1-oxide as carbodiimide The catalyst was stirred at 185 ° for 5 hours under a nitrogen stream. The infrared spectrum of the reaction solution was measured to confirm that the absorption of the wavelength 2200 to 2300 cnT1 had disappeared. Naturally cooled to 6 (TC, 56 7 parts by mass of ions were added. Exchange water to obtain a solid content of 40% by mass Carbonized diimide water-soluble resin solution (D) [Example 1] (1) Preparation of coating liquid The following coating agents were mixed to prepare a coating liquid. 5 5 . 8 6 mass % 3 0.0 0 mass % 1 3 . 5 2 mass % 0.5 9 mass % • Water • Isopropanol • Polyurethane resin solution (A-1 ) • Particles -42- 201132499 (矽 sol with an average particle size of 40 nm, solid concentration 4 0 Mass %) Surfactant 0.03 mass ° / 〇 (lanthanum, solid content concentration 100% by mass) (2) The manufacture of the easy-adhesive polyester film for solar cells will be used as a film raw material polymer containing 〇·〇3 mass Nine of the PET resin (intrinsic viscosity: 0.62 dl/g) of cerium oxide particles having an average particle diameter of 2.5 // m was dried at 135 ° C for 6 hours under a reduced pressure of 133 Pa. Thereafter, the supply was continued. The extruder was melted at about 285 ° C. The PET resin was separately filtered with a stainless steel sintered body filter (nominal filtration accuracy of 10 M m particles cut off by 95%), and melt-extruded into a sheet. On a rotating cooling metal roll whose surface temperature is maintained at 30 ° C, it is quenched and cured. Obtaining an unstretched PET sheet. The unstretched PET sheet is heated to 1 〇〇 ° C with a heated roll group and an infrared heater, and then extended by 3.5 times in the longitudinal direction with a roll group having a peripheral speed difference. A uniaxially stretched PET film was obtained. Next, the coating liquid was applied to one side of the PET film by a roll coating method, and then dried at 80 ° C for 20 seconds. In addition, the coating amount was adjusted so that the final (biaxially) After the stretching, the coating amount after drying was 0.15 g/m2 (the thickness of the coating layer after drying was 150 nm). Subsequently, it was extended by 4.0 times in the width direction at 120 ° C by a tenter, and heated at 230 ° C for 0.5 second in the length direction of the fixed film, and was carried out for 10 seconds at 1 〇〇. Relaxation treatment in the width direction of 3 % to obtain an easily connectable polyester film for solar cells of 250 / / m. The evaluation results are shown in Table 1. -43-201132499 [Experimental Example 1] In addition to changing the polyurethane resin to the polyurethane resin (A-5), the solar cell was easily obtained in the same manner as in Example i. A polyester film. [Experimental Example 2] The easy-adhesive polyester for solar cell was obtained in the same manner as in Example 1 except that the polyurethane resin was changed to the polyurethane resin (A-6). film. [Comparative Example 1] The easy-adhesive polyester for solar cell was obtained in the same manner as in Example 1 except that the polyurethane resin was changed to the polyurethane resin (A-7). film. [Comparative Example 2] The easy-adhesive polyester for solar cell was obtained in the same manner as in Example 1 except that the polyurethane resin was changed to the polyurethane resin (A-8). film. [Comparative Example 3] An easy-adhesive polyester film for a solar cell was obtained in the same manner as in Example 1 except that the thickness of the substrate of the easy-adhesive polyester film for a solar cell was changed to 5 #m. -44 - 201132499 [Example 2] The solar cell was easily obtained in the same manner as in the Example except that the polyurethane resin was changed to the polyurethane resin (A-2). Polyester film. [Example 3] An easy-adhesive polyester for solar cell was obtained in the same manner as in Example except that the polyurethane resin was changed to the polyurethane resin (A-3). film. [Example 4] A solar cell was obtained in the same manner as in Example 1 except that the polyurethane resin was changed to the urethane group-containing polyurethane resin (A - 4 ). Easy-adhesive polyester film. [Example 5] An easy-adhesive polyester film for a solar cell was obtained in the same manner as in Example 1 except that the thickness of the substrate of the easy-adhesive polyester film for a solar cell was changed to 50 μm. [Example 6] An easy-adhesive polyester film for a solar cell was obtained in the same manner as in Example 1 except that the thickness of the substrate of the easy-adhesive polyester film for a solar cell was changed to 100 μm. [Example 7] An easy-adhesive polyester film for a solar cell was obtained in the same manner as in Example 1 except that the thickness of the substrate of the easy-adhesive polyester film for a solar cell was changed to 305 mA. -45-201132499 [Example 8] An easy-to-adhesive for solar cell was obtained in the same manner except that the coating liquid was changed to the following: • Water • Isopropyl alcohol • Polyurethane resin solution (A-1) • Particles (a sol with an average particle diameter of 40 nm and a solid concentration of 40% by mass) • Surfactant (tantalum, solid content concentration: 100% by mass) [Example 9] Except that the coating liquid was changed to the following In the same way, obtain the easy adhesion of solar cells. • Water • Isopropyl alcohol • Polyurethane resin solution (A-1 ) • Particles (average particle size 40 nm sol, solid concentration 40 Mass %) • Surfactant (lanthanum, solid content concentration: 1% by mass) [Example 1 〇] (3) The solar cell back sheet was produced in the same manner as in Example 1 polyester film. 6 1 · 5 1 Quality. /. 3 0.0 0 mass% 8 _ 1 1 mass% 〇 · 3 5 mass% 0.03 mass 〇/0 The polyester film of Example 1 was used. 4 1 · 7 1% by mass 3 0.00% by mass 2 7.0 5 mass% 1 · 1 8 mass% 0.06 mass% -46- 201132499 The easy-adhesive polyester I ester film for solar cell of Example 1 (50//m / / Aluminum foil (30 #m) / Polyfluoroethylene thin), and the dry laminate method is followed to obtain the Tai back plate. Dry laminating adhesive TAKELAC A-315 (manufactured by Mitsui Inc.) / ΤΑΚΕΝΑΤΕ A-10 (San Geng Chemical Co., Ltd. | (solid content ratio) [Example 1 1] except for polyaminocarboxylic acid The epoxy resin film was changed to the polyaminomethyl group A-9), and the battery-adhesive polyester film was used in the same manner as in Example 1. [Example 1 2] An easy-adhesive polyester film for a battery was used in the same manner as in Example 1 except that the polyurethane resin was changed to polyaminomethyl A-1 0 ). [Example 1 3] (3) Production of back sheet for solar cell The solar cell of Example 1 was easily bonded to each other! A polyester film (50/zm) / aluminum foil (3 〇 Am) / polyvinyl fluoride m) was formed and dried by a dry lamination method to obtain a slab.膜 film / white poly film (3 8 ren m 昜 energy battery Chemicals, this made) = 9 / 1 acid ester resin (obtained solar acid resin (and obtained solar eye film / white film (38 μ for solar cells - 47- 201132499 Adhesive for dry lamination T AKELAC A-3 1 5 (manufactured by Mitsui Chemicals Co., Ltd.) / τ AKEN ATE A-10 (manufactured by Sanken Chemical Co., Ltd.) = 9/1 (solid content ratio) As in Example 1 And the backsheet for a solar cell of Example 1 is an EYE Super UV Tester SUV manufactured by Iwasaki Electric Co., Ltd., using an easy-adhesive polyester film surface for a solar cell as an irradiation surface. W151 &gt; 100 hours of continuous UV irradiation treatment at 6 3 ° C, 50% RH, and irradiation intensity of 100 mW/cm 2 "The solar cell backsheet results after UV irradiation were visually confirmed under a fluorescent lamp. In the solar cell backsheet of Example 10, although a slight yellowing was observed, the solar cell backsheet of Example 13 was completely colorless and maintained in a good appearance. -48- 201132499 ^ 1-1 1-^ 0.51 1.64 1 1 1.17 1.34 1.12 1.05 τ-Η 1.15 1.13 inch 1.18 1.17 1.20 1.38 1.20 EVA adhesion B. fast curing type IH heat and humidity resistance &X &lt; XXX 〇〇〇〇〇〇〇〇〇〇〇〇 性 ◎ ◎ ◎ &lt;&lt;3&lt; ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ Η Μ Μ 耐 耐 X X ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ A. Standard curing type 耐 Moisture and heat resistance ◎ X &lt; 3 X &lt; 0 ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ΗΗ 湿 湿 X X X ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ Example 1 Experimental Example 1 Experimental Example 2 Comparative Example 1 Comparative Example 2 Comparative Example 3 Example 2 Example 3 Example 4 Example 5 Example 6 Example 7 Example 8 Example 9 Example 10 Example 12 Example 13 | 6 inch, 201132499 [Examples 1 4] (1) Preparation of coating liquid The following coating agents were mixed to prepare a coating liquid. • Water 5 5 · 8 6 mass% • Isopropyl alcohol 30.00% by mass • Polyurethane resin solution (A-1 ) 13.52% by mass • Particles 0 · 5 9 mass % (average particle size 40 urn sol (solid content concentration: 40% by mass) • Surfactant 0.03% by mass (lanthanum, solid content concentration: 100% by mass) (2) Production of easy-adhesive white polyester film for solar cells (cavity material a) 60 The mass% of the polymethylpentene resin, the 20% by mass of the polypropylene resin, and the 20% by mass of the polystyrene resin are mixed in nine pieces, and then supplied to the vented twin-screw extruder which is adjusted to a temperature of 2 8 5 ° C. The press is kneaded to produce a void forming agent (raw material a). (Polyester b) Polymerization of polyethylene terephthalate resin containing cerium oxide particles by a conventional method to produce an intrinsic viscosity of 500 ppm of aggregated cerium oxide particles (average particle diameter of 2. 〇βιη) It is a polyethylene terephthalate of 62 dl/g (raw material b). -50- 201132499 (Masterbatch raw material c containing titanium oxide particles) The above polyethylene terephthalate (raw material b) and anatase titanium dioxide particles having an average particle diameter of 0.2 // m (堺Chemical Industries Co., Ltd.) Co., Ltd. (manufactured by Sakai Chemical Industry Co., Ltd.) was mixed at a mass ratio of 5 0/5 0 and kneaded by a venting kneading extruder to produce a mother particle raw material (raw material c) containing titanium oxide particles. (Production of Film) The above-mentioned raw materials subjected to vacuum drying under heating were continuously metered. The mixture was continuously stirred to have a/b/c = 8/82/10 (mass ratio) as a raw material of the layer A. Next, the raw material is supplied to an extruder for melt-kneading, and supplied to a feed splitter (co-extrusion adapter) through a filter. On the other hand, the raw material of the layer B is continuously metered to b/c == 80/20 (mass ratio), supplied to a vented twin-screw extruder for melt-kneading, and passed through a filter. And supplied to the feed splitter casing. In the feed splitter sleeve, the B layer is joined to the same thickness on both sides of the A layer. At this time, the amount of resin discharged to the A layer and the B layer is controlled so that the thickness ratio of each layer before the extension becomes B/A/B = 1 0 / 8 0 / 1 0 'and is cast at a surface temperature of 30 ° A cooling drum of C was used to produce an unstretched film having a thickness of 2.4 mm. At this time, air of 10 ° C was blown to the opposite side of the molten polymer extruded on the cooling drum to cool and solidify the molten polymer from both sides. -51 - 201132499 Next, the unstretched film obtained by the above method was heated to 65 °C using a heating roll, and then stretched 3.2 times between rolls having different peripheral speeds. At this time, in the intermediate portion between the low speed roller and the high speed roller, a concentrating infrared heater is disposed at a position facing the surface with the film interposed therebetween, so that the sufficient heat required for uniformly stretching the film is equally applied from both surfaces of the film. Next, the coating liquid was applied to one side of the PET film by a roll coating method, and then dried at 80 ° C for 20 seconds. Further, the coating amount was adjusted so that the coating amount after the final (after biaxial stretching) was 0.15 g/m2, and then introduced into a tenter, and the temperature was raised to 12 (TC to 150 °C) while heating. It was extended 3.9 times in the width direction, and heat treatment was applied by blowing a hot air of 22 ° C for 30 seconds in a tenter, and then slowly cooling to room temperature for 40 seconds while applying 2 to the width direction. The relaxation treatment of % was carried out to obtain an easily connectable white polyester film for a solar cell with a void having an apparent density of 1.10 g/cm3 and a thickness of 250/zm, and the evaluation results are shown in Table 2. Example 1 5] An easy-contact white color for solar cell was obtained in the same manner as in Example 14 except that the polyurethane resin was changed to the polyurethane resin (A-2). Polyester film. [Example 16] A solar cell was obtained in the same manner as in Example i4 except that the polyurethane resin was changed to the polyurethane resin (A-3). Easy-adhesive white polyester film. -52 - 201132499 [Example 1 7] The same procedure as in Example 14 was carried out except that the polyurethane resin was changed to the melamine group-containing polyurethane resin (A-4). An easy-adhesive white polyester film for a solar cell was obtained. [Example 1 8] Except that the polyurethane resin was changed to a polyurethane resin (A-9), the same as in Example 1 4, an easy-adhesive polyester film for solar cells was obtained in the same manner. [Example 1 9] Except that the polyurethane resin was changed to a polyurethane resin (A-100), the rest was An easy-adhesive polyester film for a solar cell was obtained in the same manner as in Example 14. -53- 201132499 (N撇色Η 〇; Γ-; Τ-^ 1&gt; c3 〇»〇〇〇〇〇〇. -1 95.6 95.8 (4) 95.8 95.4 褂Ο 1.17 1.34 CN Η 1.05 1.20 1.38 EVA adhesion B. Rapid curing type t-j Moisture resistance 〇〇〇〇〇〇 ◎ ◎ ◎ ◎ ◎ ◎ Moisture resistance ◎ ◎ ◎ ◎ ◎ ◎ Continuity ◎ ◎ ◎ ◎ ◎ ◎ A. Standard固 ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施17 Example 18 Example 19 201132499 [Example 2 Ο] (1) Preparation of coating liquid The following coating agents were mixed to prepare a coating liquid. 5 5.6 2 mass% 3 0 . 〇〇 mass% 1 1.2 9 mass% 2.2 6 mass% 〇. 7 1 mass% • water • isopropyl alcohol • polyurethane resin solution (A-1) • End cap Polyisocyanate aqueous dispersion (B) • Particles (average particle size 40 nm sol, solid content concentration 40% by mass) • Particles 0.0 7 mass% (average particle size 450 nm bismuth sol, solid component concentration 40% by mass • Surfactant 0.05% by mass (lanthanum, solid content concentration: 1% by mass) (2) The production of easy-to-adherent polyester film for solar cells will be used as a raw material for film raw materials. The average particle diameter was 2.5; nine pieces of PET resin of zm cerium oxide particles (inherent viscosity: 0.62 dl/g) were dried at 135 ° C for 6 hours under reduced pressure of 133 Pa. Thereafter, the supply to the extruder was melted at about 2 8 5 t. The PET resin was filtered through a stainless steel sintered body filter (nominal filtration accuracy of 10 M m particles by 95%), and melt-extruded into a sheet. The spin-cooled metal roll was maintained at a surface temperature of 30 ° C to be quenched and cured to obtain an unstretched PET sheet. -55- 201132499 The unstretched P ET sheet is heated to 100 ° C with a heated roll group and infrared rays, and then extended by 3.5 times toward the length of the roll group having a peripheral speed difference to obtain a uniaxial direction. Extend the PET film. Next, the liquid was applied to one side of the PET film by a roll coating method, and then dried at 80 ° C for 20 seconds. Further, the coating amount was adjusted so that the final coating amount (after biaxial stretching) was 0.15 (the thickness of the coating layer after drying was 150 nm). Next, it was extended by 4.0 times in the width direction at a °C with a tenter, and heated at 230 ° C for 0.5 second under the length of the width of the fixed film, and 3% width at 100 ° C for 10 seconds. The direction of relaxation treatment to obtain 250 easy-to-adhere polyester film from solar cells. The evaluation results are shown in Table 3 (Experimental Example 3) except that the polyurethane resin was changed to the polyurethane tree A-5), and the battery was obtained in the same manner as in Example 20. Easy-adhesive polyester film. [Experimental Example 4] An easy-adhesive polyester film for a battery was obtained in the same manner as in Example 20 except that the polyurethane resin was changed to the polyurethane tree A-6. . [Comparative Example 4] An easy-adhesive polyester film for a battery was obtained in the same manner as in Example 20 except that the polyurethane resin was changed to the polyurethane tree A-7). . The heat is applied to the coating to form a g/m2:120 direction for a duration of m. Fat (Sun Cream (Sun-56-201132499 [Comparative Example 5] except that the polyurethane resin was changed to the polyurethane resin (A-8), and the other example 20 In the same manner, an easy-adhesive polyester film for a solar cell was obtained. [Comparative Example 6] The same as Example 20 except that the thickness of the substrate of the easy-adhesive polyester film for a solar cell was changed to 5 #m. In the same manner as in Example 20, the easy-adhesive polyester for solar cell was obtained in the same manner as in Example 20 except that the coating liquid was changed to the following. Film 5 8.0 2% by mass 3 0 · 0 〇 mass % 9.4 7 mass % 1 . 8 9 mass % 0 · 5 9 mass % water isopropanol polyurethane resin solution (A-1 ) end-capped type Polyisocyanate aqueous dispersion (B) particles (cerium sol having an average particle diameter of 40 nm, solid content concentration of 40% by mass) • 0.03 mass% of surfactant (lanthanum, solid content concentration: 1% by mass) [Examples] 22] In addition to changing the coating liquid to The remaining adhesive polyester film for solar cells was obtained in the same manner as in Example 20. -57- 201132499 5 4.7 5 mass% 3 0.00 Μ Λ % 1 2 · 9 9 mass % 1 . 5 2 Mass% 0.7 1% by mass 0.0 3 mass% Water isopropanol polyurethane solution (A-1) Blocked polyisocyanate aqueous dispersion (B) particles (average particle size 40 nm bismuth sol, solid Component concentration: 40% by mass) Surfactant (lanthanum, solid content concentration: 1% by mass) [Example 2 3] The same procedure as in Example 20 except that the coating liquid was changed to the following Obtained an easy-adhesive polyester film for solar cells. 5 7.3 5 mass% 3 0.00 Μ Μ % 8 . 1 2 mass% 3.7 9 mass% 0.7 1 mass% 0.0 3 mass. / hydrazine isopropanol polyamine A Acid ester resin solution (Α-1) Blocked polyisocyanate aqueous dispersion (Β) particles (矽 sol with an average particle diameter of 40 nm, solid concentration of 40% by mass) Surfactant (lanthanum, solid concentration 1 〇〇质量%) [Example 24] In addition to changing the coating liquid to the next In the same manner as in Example 20, the easy-adhesive polyester film for solar cell was obtained. -58- 201132499 Water isopropanol polyurethane resin solution (A-1) Polyisocyanate aqueous dispersion (B) particles (cerium sol having an average particle diameter of 40 nm, solid concentration of 40% by mass) Surfactant (lanthanum, solid concentration: 1% by mass) 5 9.9 5 mass% 3 0 · 0 0质量% 3.2 5 mass% 6.0 6 mass% 0.7 1 mass% 0.0 3 mass% Example 2 5 The solar cell was easily obtained in the same manner as in Example 20 except that the coating liquid was changed to the following. A polyester film. Water 6 0.8 2% by mass Isopropanol 3 0.0 0% by mass Polyurethane resin solution (A-1) 1.6 2% by mass Blocked polyisocyanate aqueous dispersion (B) 6.8 2% by mass Particles 0.7 1 mass % (矽 sol with an average particle diameter of 40 nm, solid content concentration of 40% by mass) Surfactant 0.03% by mass (lanthanum, solid content concentration: 1% by mass) -59- 201132499 [Example 26] In addition to polymerization The easy-adhesive polyester film for solar cells was obtained in the same manner as in Example 2 except that the urethane resin was changed to the polyurethane resin (A-2). [Example 2 7] The solar cell easy adhesion was obtained in the same manner as in Example 2 except that the polyurethane resin was changed to the polyurethane resin (A-3). Polyester film. [Example 2 8] Solar energy was obtained in the same manner as in Example 2 except that the polyurethane resin was changed to the urethane group-containing polyurethane resin (A - 4 ). Easy-to-adhere polyester film for batteries. [Example 29] A solar cell was obtained in the same manner as in Example 2 except that the blocked polyisocyanate aqueous dispersion (B) was changed to the oxazoline group-containing water-soluble resin (C). Easy-adhesive polyester film. [Example 30] The solar cell was easily obtained in the same manner as in Example 20 except that the blocked polyisocyanate aqueous dispersion (C) was changed to the carbodiimide water-soluble resin (D). Polyester film. [Example 3 1] Except that the blocked polyisocyanate aqueous dispersion (C) was changed to an imido-hydroxymethyl melamine (solid content concentration: 7 〇 mass%), the remaining -60-201132499 was compared with the examples. 2 易 The same way to obtain an easy-adhesive polyester film for solar cells. [Example 3 2] An easy-adhesive polyester film for a solar cell was obtained in the same manner as in Example 20 except that the thickness of the substrate of the easy-adhesive polyester film for a solar cell was changed to 50 / z m. [Example 3 3] An easy-contact polyester film for a solar cell was obtained in the same manner as in Example 20 except that the thickness of the substrate of the easy-adhesive polyester film for a solar cell was changed to 100 // m. . [Example 3 4] An easy-adhesive polyester film for a solar cell was obtained in the same manner as in Example 20 except that the thickness of the substrate of the easy-adhesive polyester film for a solar cell was changed to 350 μm. [Example 3 5] An easy-adhesive polyester film for a solar cell was obtained in the same manner as in Example 20 except that the coating liquid was changed to the following. • Water 6 2.8 2% by mass 3 0 · 0 0 Quality. /〇5.6 7 mass% 1.1.3 mass% 0.3 5 mass% isopropyl alcohol polyurethane resin solution (A-1) blocked polyisocyanate aqueous dispersion (B) particles (average particle size 40 nm矽Sol, solid concentration 40% by mass) -61 - 201132499 • Surfactant 0. 〇3 mass% (lanthanum, solid content concentration 100% by mass) [Example 3 6] In addition to changing the coating liquid to the next In the same manner as in Example 20, the easy-adhesive polyester film for solar cells was obtained. • Water 45.99% by mass • Isopropyl alcohol 30.00% by mass • Polyurethane resin solution (A-1) 18.99% by mass • Blocked polyisocyanate aqueous dispersion (B) 3.80% by mass • Particle 1 · 1 9 % by mass (矽 sol with an average particle diameter of 40 nm, solid content concentration of 40% by mass) • 0.03 mass% of surfactant (lanthanum, solid content concentration: 1% by mass) [Example 3 7] (3) Solar cell The back sheet was fabricated by the easy-adhesive polyester film/black polyester film (50 gm) / aluminum foil (30 #m) / polyvinyl fluoride film (38 / zm) for the solar cell of Example 20, and was dry. The laminate method is followed by obtaining a back sheet for a solar cell. Dry laminating adhesive TAKELAC A-3 1 5 (manufactured by Mitsui Chemicals Co., Ltd.) / ΤΑΚΕΝΑΤΕ Α-10 (manufactured by Sangen Chemical Co., Ltd.) = 9/1 (solid content ratio) [Example 3 8] -62- 201132499 The easy-adhesive polyester film for solar cells was obtained in the same manner as in Example 20 except that the polyurethane resin was changed to the polyurethane resin (A_9). [Example 3 9] In addition to changing the polyurethane resin to the polyurethane resin (A - 1 0 ), the solar cell was easily obtained in the same manner as in Example 20 Polyester film. [Example 40] (3) Production of back sheet for solar cell The easy-adhesive polyester film/black polyester film (50 μm) / aluminum foil (30#m) / polyvinyl fluoride film for solar cell of Example 38 The structure of (38//m) was followed by a dry buildup method to obtain a back sheet for a solar cell. Dry laminating adhesive TAKELAC A-3 1 5 (manufactured by Mitsui Chemicals Co., Ltd.) / ΤΑΚΕΝΑΤΕ A-1 0 (manufactured by Sangen Chemical Co., Ltd.) = 9 Π (solid content ratio) Solar cells of Examples 37 and 40 The back surface is used as the irradiation surface of the easy-adhesive polyester film surface for solar cells, and the Eye Super UV Tester SUV-W151 manufactured by Iwasaki Electric Co., Ltd. is used at 63 ° C, 50% RH, and the irradiation intensity is 100. A continuous UV irradiation treatment of 100 hours was performed under mW/cm2. The solar cell backsheet after UV irradiation was visually confirmed under a fluorescent lamp. Although the solar cell backsheet of Example 37 was observed to have a little yellowing, the solar cell backsheet of Example 40 was comprehensive. There is no change in color and it maintains a good appearance. -63- 201132499 «-〇鹋§ 0.93 0.37 § 0.93 1.05 0.84 0.63 0.51 1.18 0.90 1.00 0.94 0.91 0.88 0.94 0.92 0.92 0.92 0.93 0.93 0.98 1.21 0.98 付 m is B. Fast curing type |-M Moisture and heat resistance ◎ X &lt; ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ HH湿 ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ W | A. Standard curing type moist heat resistance ◎ X &lt;] X ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ 〇 〇 ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ 1 ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ Example 20 | Experimental Example 3 | Experimental Example 4 Comparative Example 4 Comparative Example 5 I Comparative Example 实施 Example 21 Example 22 Example 23 Example 24 Example 25 Example 26 Example 27 Example 28 Example 29 Example 30 Example 31 Example 32 Example 33 Example 34 Example 35 Example 16 Example 37 Example 38 Example 39 I Example 40 - inch 9 丨 201132499 [Example 4 1] (1) Preparation of coating liquid The following coating agents were mixed to prepare a coating liquid. 5 5.6 2% by mass 3 0.0 0% by mass 1 1. 2 9 mass% 2.2 6 mass% 0.7 1 mass% • Water • Isopropanol • Polyurethane resin solution (A-1) • End-capped poly Isocyanate aqueous dispersion (B) • Particles (average particle size 40 nm sol, solid concentration 40% by mass) • Particle 0 · 0 7 mass% (average particle size 450 nm bismuth sol, solid concentration 40% by mass • Surfactant 0.05% by mass (lanthanum, solid content concentration: 1% by mass) (2) Production of easy-adhesive white polyester film for solar cells (cavity material a) 60% by mass of polymethyl group The pentene resin, 20% by mass of the polypropylene resin, and 20% by mass of the polystyrene resin are mixed in nine pieces, and then supplied to a vented twin-screw extruder adjusted to 285 ° C and kneaded. A void forming agent (raw material a) is produced. (Polyester b) A polyethylene terephthalate resin containing cerium oxide particles is polymerized by a conventional method to produce agglomerated cerium oxide-65-201132499 particles containing 500 ppm (average particle diameter of 2.0) Ym) and polyethylene terephthalate (raw material b) having an intrinsic viscosity of 0.62 dl/g. (Masterbatch raw material c containing titanium oxide particles) The above-mentioned polyethylene terephthalate (raw material b) and anatase type titanium dioxide particles having an average particle diameter of 〇. 2 /zm (manufactured by Suga Chemical Industry Co., Ltd.) Mixing at a mass ratio of 50/50 and kneading in a vent type kneading extruder to produce a mother particle raw material (raw material c) containing titanium oxide particles (manufacture of a film), which is subjected to vacuum drying under heating The raw material is continuously metered and continuously stirred to a/b/c = 8/82/10 (mass ratio) to be used as a raw material for the layer A. Next, the raw material is supplied to an extruder for melt-kneading, and is supplied to a feed splitter sleeve (co-extruded joint) via a filter. On the other hand, the raw material of the layer B is continuously metered using the aforementioned raw materials. To be b/c = 80/20 (mass ratio), it is supplied to a vented twin-screw extruder for melt-kneading, and is supplied to a feed splitter bush through a filter. In the feed splitter sleeve, the B layer is joined to the same thickness on both sides of the A layer. At this time, the amount of resin discharged to the A layer and the B layer is controlled so that the thickness ratio of each layer before the extension becomes B/A/B = 10/80/10, and the cooling is performed at a surface temperature of 30 ° C. An unstretched film having a thickness of 2.4 mm was fabricated on the barrel. At this time, air of 1 ° C was blown to the opposite side of the molten polymer extruded on the cooling drum to cool and solidify the molten polymer from both sides. -66-201132499 Next, the unstretched film obtained by the above method was heated to 65 ° C using a heating roll, and then stretched 3.2 times between rolls having different peripheral speeds. At this time, in the intermediate portion between the low speed roller and the high speed roller, a concentrating infrared heater is disposed at a position facing the surface with the film interposed therebetween, so that the sufficient heat required for uniformly stretching the film is equally applied from both surfaces of the film. Next, the coating liquid was applied to one side of the PET film by a roll coating method, and then dried at 80 ° C for 20 seconds. Further, the coating amount was adjusted so that the coating amount after the final (after biaxial stretching) drying was 0.15 g/m2 (the thickness of the coating layer after drying was 150 nm). Subsequently, it was introduced into a tenter, and was heated to a temperature of 12 CTC to 150 °C while extending 3.9 times in the width direction. Further, heat treatment was applied by blowing a hot air of 22 °C for 30 seconds in a tenter. Thereafter, while slowly cooling to room temperature for 40 seconds, a relaxation treatment of 2% was applied in the width direction to obtain a biaxial alignment containing voids having an apparent density of 1.10 g/cm 3 and a thickness of 250/zm. An easy-to-adhesive white polyester film for solar cells. The evaluation results are shown in Table 4. [Example 42] The easy-adhesive white polymerization for solar cells was obtained in the same manner as in Example 41 except that the polyurethane resin was changed to the polyurethane resin (A-2). Ester film. [Example 43] An easy-contact white color for solar cell was obtained in the same manner as in Example 41 except that the polyurethane resin was changed to the polyurethane resin (A-3). Polyester film. -67-201132499 [Example 44] The same procedure as in Example 41 was carried out except that the polyurethane resin was changed to the melamine group-containing polyurethane resin (A-4). An easy-adhesive white polyester film for solar cells was obtained. [Example 45] An easy-contact polyester for solar cell was obtained in the same manner as in Example 41 except that the polyurethane resin was changed to the polyurethane resin (A - 9 ). Films [Example 46] In the same manner as in Example 41 except that the polyurethane resin was changed to the polyurethane resin (A-1 0 ), the solar cell was easily used. Polyester film ° -68- 201132499 inch tone Γ-; »—Η 1-H TH C^; a ο in 〇ο in o IT) oo 1 95.8 1 | 95.3 | 1 95.6 1 95.8 | 95.8 | 95.8 Absorbance Ratio 1460/1530 0.93 1.15 1.05 0.84 0.98 1.21 EVA adhesion B. Rapid curing type h-j Moisture resistance ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ KH Moisture resistance ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ A. Standard curing type jH Moisture resistance ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ ◎ Example 41 Implementation Example 42 Example 43 Implementation [Example 45] Example 46 _ 69 丨 201132499 [Industrial Applicability] The easy-adhesive polyester film for solar cell of the present invention has adhesion to a sealing material and adhesion under high temperature and high humidity ( It is excellent in heat and humidity resistance, so it is suitable as the most suitable base film for solar cell backsheets. [Simplified illustration] None. [Main component symbol description] ίΚ. -70-

Claims (1)

201132499 七、申請專利範圍: 1. 一種太陽能電池用易接著性聚酯薄膜,其係至少在單面 具有塗布層之基材厚度爲20至500/zm之聚酯薄膜,且 該塗布層是含有以脂肪族系聚碳酸酯多元醇作爲構 成成分之胺基甲酸酯樹脂。 2. 如申請專利範圍第1項之太陽能電池用易接著性聚酯薄 膜,其中該塗布層是以脂肪族系聚碳酸酯多元醇作爲構 成成分之胺基甲酸酯樹脂爲主成分,且 在該塗布層之紅外線光譜法光譜中,源於脂肪族系 聚碳酸酯成分之1460 CHT1附近之吸光度(A146G)與源於 胺基甲酸酯成分之1 5 3 0 cnT1附近之吸光度(A! 53〇)的比 率(Ai46〇/Ai530)爲 〇.7〇 至 1.60。 3 .如申請專利範圍第1項之太陽能電池用易接著性聚酯薄 膜,其中該塗布層是以脂肪族系聚碳酸酯多元醇作爲構 成成分之胺基甲酸酯樹脂與交聯劑爲主成分,且 在該塗布層之紅外線光譜法光譜中,源於脂肪族系 聚碳酸酯成分之1460 CHT1附近之吸光度(A146〇)與源於 胺基甲酸酯成分之1530 CHT1附近之吸光度(Α153ϋ)的比 率(Αΐ46〇/Αΐ530)爲 0.50 至 1.55。 4.如申請專利範圍第3項之太陽能電池用易接著性聚酯薄 膜,其中該交聯劑是選自三聚氰胺系交聯劑、異氰酸酯 系交聯劑、碳化二亞胺系交聯劑、曙唑啉系交聯劑中之 至少一種交聯劑。 -71 - 201132499 5 .如申請專利範圍第3項之太陽肯旨 膜,其中在該塗布層中之該交聯 酸酯樹脂爲5質量。/。以上且90質 6.如申請專利範圍第1至5項之太 酯薄膜,其中該聚酯薄膜爲白色 7 . —種太陽能電池用背板,其係積 至6項之太陽能電池用易接著性 :電池用易接著性聚酯薄 劑的含量相對於胺基甲 量%以下。 :陽能電池用易接著性聚 聚酯薄膜。 層如申請專利範圍第1 聚酯薄膜而成。 -72- 201132499 四、指定代表圖: (一) 本案指定代表圖為:無。 (二) 本代表圖之元件符號簡單說明: 無0 五、本案若有化學式時,請揭示最能顯示發明特徵的化學式:201132499 VII. Patent application scope: 1. An easy-contact polyester film for solar cells, which is a polyester film having a coating layer having a coating thickness of 20 to 500/zm at least on one side, and the coating layer contains A urethane resin containing an aliphatic polycarbonate polyol as a constituent component. 2. The easy-adhesive polyester film for a solar cell according to the first aspect of the invention, wherein the coating layer is a urethane resin containing an aliphatic polycarbonate polyol as a constituent component, and In the infrared spectroscopy spectrum of the coating layer, the absorbance (A146G) in the vicinity of 1460 CHT1 derived from the aliphatic polycarbonate component and the absorbance in the vicinity of 1 5 3 0 cnT1 derived from the urethane component (A! 53) The ratio of 〇) (Ai46〇/Ai530) is 〇.7〇 to 1.60. 3. The easy-adhesive polyester film for solar cell according to claim 1, wherein the coating layer is mainly composed of an aliphatic polycarbonate polyol as a constituent urethane resin and a crosslinking agent. In the infrared spectroscopy spectrum of the coating layer, the absorbance (A146〇) in the vicinity of 1460 CHT1 derived from the aliphatic polycarbonate component and the absorbance in the vicinity of 1530 CHT1 derived from the urethane component (Α153ϋ) The ratio (Αΐ46〇/Αΐ530) is 0.50 to 1.55. 4. The easy-adhesive polyester film for solar cells according to claim 3, wherein the crosslinking agent is selected from the group consisting of a melamine crosslinking agent, an isocyanate crosslinking agent, a carbodiimide crosslinking agent, and a hydrazine. At least one crosslinking agent in the oxazoline crosslinking agent. -71 - 201132499 5. The solar cell film of claim 3, wherein the crosslinked acid ester resin in the coating layer is 5 mass. /. The above and 90 quality 6. The acylate film of the first to fifth aspects of the patent application, wherein the polyester film is white 7. The back sheet for a solar cell, which is tied to the solar cell for easy adhesion. The content of the easy-adhesive polyester thinner for a battery is less than or equal to the amount of the amino group. : Easy-adhesive polyester film for solar cells. The layer is made of the first polyester film of the patent application range. -72- 201132499 IV. Designated representative map: (1) The representative representative of the case is: None. (2) A brief description of the symbol of the representative figure: None 0. If there is a chemical formula in this case, please disclose the chemical formula that best shows the characteristics of the invention:
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