TW200427797A - Method for coated composite film - Google Patents

Method for coated composite film Download PDF

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Publication number
TW200427797A
TW200427797A TW093107130A TW93107130A TW200427797A TW 200427797 A TW200427797 A TW 200427797A TW 093107130 A TW093107130 A TW 093107130A TW 93107130 A TW93107130 A TW 93107130A TW 200427797 A TW200427797 A TW 200427797A
Authority
TW
Taiwan
Prior art keywords
temperature
coating
weight
resin
film
Prior art date
Application number
TW093107130A
Other languages
Chinese (zh)
Inventor
Takayuki Fujita
Takuhiro Kakii
Masakazu Watanabe
Original Assignee
Nippon Paint Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nippon Paint Co Ltd filed Critical Nippon Paint Co Ltd
Publication of TW200427797A publication Critical patent/TW200427797A/en

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05DPROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D7/00Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials
    • B05D7/50Multilayers
    • B05D7/56Three layers or more
    • B05D7/57Three layers or more the last layer being a clear coat
    • B05D7/572Three layers or more the last layer being a clear coat all layers being cured or baked together
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05DPROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D7/00Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials
    • B05D7/02Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials to macromolecular substances, e.g. rubber
    • B05D7/04Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials to macromolecular substances, e.g. rubber to surfaces of films or sheets
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05DPROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D3/00Pretreatment of surfaces to which liquids or other fluent materials are to be applied; After-treatment of applied coatings, e.g. intermediate treating of an applied coating preparatory to subsequent applications of liquids or other fluent materials
    • B05D3/02Pretreatment of surfaces to which liquids or other fluent materials are to be applied; After-treatment of applied coatings, e.g. intermediate treating of an applied coating preparatory to subsequent applications of liquids or other fluent materials by baking
    • B05D3/0254After-treatment
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05DPROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D7/00Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials
    • B05D7/14Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials to metal, e.g. car bodies
    • 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
    • C08G18/4205Polycondensates having carboxylic or carbonic ester groups in the main chain containing cyclic groups
    • C08G18/423Polycondensates having carboxylic or carbonic ester groups in the main chain containing cyclic groups containing cycloaliphatic groups
    • 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
    • C08G18/70Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
    • C08G18/72Polyisocyanates or polyisothiocyanates
    • C08G18/80Masked polyisocyanates
    • C08G18/8061Masked polyisocyanates masked with compounds having only one group containing active hydrogen
    • 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05DPROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D3/00Pretreatment of surfaces to which liquids or other fluent materials are to be applied; After-treatment of applied coatings, e.g. intermediate treating of an applied coating preparatory to subsequent applications of liquids or other fluent materials
    • B05D3/02Pretreatment of surfaces to which liquids or other fluent materials are to be applied; After-treatment of applied coatings, e.g. intermediate treating of an applied coating preparatory to subsequent applications of liquids or other fluent materials by baking
    • B05D3/0209Multistage baking

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Wood Science & Technology (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Materials Engineering (AREA)
  • Application Of Or Painting With Fluid Materials (AREA)
  • Paints Or Removers (AREA)

Abstract

Disclosed is a coated composite film formation method by a three-coat one-bake method, which can form a coated composite film excellent in appearance, in particular, gloss appearance, and excellent in anti-chipping properties. The method comprises forming an electrocoated film on a substrate, and then successively applying an intermediate paint, a base paint and a clear paint in a wet-on-wet manner, followed by baking and curing the applied three layers at once, wherein the baking and curing includes both a low-temperature heating stage of heating at a temperature which is 25 to 80% of a curing temperature for a time which is 5 to 30% of a curing time, and a high-temperature heating stage of heating at a temperature which exceeds 80% and is not more than 120% of a curing temperature for a time which is 30 to 130% of a curing time.

Description

200427797 玖、發明說明: 【發明戶斤屬之技術領域3 發明領域 本發明係有關一種形成經塗覆之複合薄膜之方法,特 5 別係有關一種經由三塗膜一次烤乾方法來形成經塗覆之複 合薄膜之方法。 I:先前技術:! 發明背景 有兩種形成經塗覆之複合薄膜之方法。其中一種方法 10 為每層塗覆膜於塗覆後個別烤乾及硬化。另一種方法為經 由塗覆兩種或兩種以上塗料形成經塗覆之複合薄膜而未硬 化,然後才一次硬化。例如兩層塗膜一次烤乾方法通常係 用來形成金屬塗膜。JP-ANo. 11-114489揭示一種形成經塗 覆之複合薄膜之方法,包含連續形成一彩色底塗膜、一金 15 屬底塗膜以及一透明塗膜,然後同時烤乾且硬化三層,俾 促進薄膜外觀。 當中間塗膜、底塗膜及透明塗膜係藉三塗膜一次烤乾 方法形成時,可免除中間塗膜硬化用之烤爐。如此,可減 少耗用能量及縮短操作時間,於經濟觀點及環保方面有重 20 大優勢。 但於三塗膜一次烤乾方法,三層塗膜係於濕態或濕氣-乾態鋪設。因此理由故溶劑之逃逸路徑減少或有限,因此 比較習知連續烤乾法或二塗膜一次烤乾法,經塗覆之複合 薄膜内之非揮發性成分含量增高。結果一層塗膜所含的溶 5 200427797 良影響 办動至塗膜。特別於加熱時移動至眺鄰塗膜 溶劑的移動容易增加所謂之烤乾與硬化時之相混合現象 其中此鄰塗膜彼此互相溶解,個別塗膜所含之成分彼此、、θ 合。當發生相混合現象時,結果所賴合_顿顯著= 化。特別’減合對經塗覆之複合薄膜之光科觀造成不200427797 发明 Description of the invention: [Technical Field of the Invention] 3 Field of the Invention The present invention relates to a method for forming a coated composite film, and in particular 5 relates to a method for forming a coated film through a three-coat baking method. Method for covering composite film. I: Prior technology:! BACKGROUND OF THE INVENTION There are two methods for forming coated composite films. One method 10 is to dry and harden each coating film individually after coating. Another method is to form a coated composite film by applying two or more coatings without hardening, and then hardening it once. For example, a two-layer baking method is usually used to form a metal coating film. JP-ANo. 11-114489 discloses a method for forming a coated composite film, which comprises continuously forming a color base coating film, a metal 15 base coating film, and a transparent coating film, and then baking and hardening three layers simultaneously,俾 Promote film appearance. When the intermediate coating film, the base coating film and the transparent coating film are formed by baking the three coating films once, the oven for curing the intermediate coating film can be eliminated. In this way, energy consumption can be reduced and operating time can be shortened, which has important advantages in terms of economics and environmental protection. However, in the three-coat film drying method, the three-layer coating film is laid in a wet state or a moisture-dry state. For this reason, the escape route of the solvent is reduced or limited. Therefore, the conventional continuous baking method or the two-coat baking method is used to increase the content of non-volatile components in the coated composite film. As a result, the solvent contained in one layer of coating film has a good effect. Especially when moving to the adjacent coating film during heating, the movement of the solvent tends to increase the so-called mixing phenomenon during baking and hardening. The adjacent coating films dissolve each other, and the components contained in the individual coating films are combined with each other. When the phase mixing phenomenon occurs, the result depends on the significant difference. In particular, the subtraction does not affect the optical science of the coated composite film.

另一方面,JP-A Νο. 2000_84463提示一種於二階段加 熱條件下進行烤乾與硬化步驟之方法,來作為使用溶劑型 熱固塗料形成光滑度絕佳之塗膜之方法。於此種方法择 Η)由溫和蒸發去除塗層所含之溶劑,可防止塗膜表面的粗棱, 但三塗膜一次烤乾方法有下列問題。On the other hand, JP-A No. 2000_84463 suggests a method of performing the drying and hardening steps under two-stage heating conditions as a method for forming a smooth coating film using a solvent-based thermosetting coating. The choice of this method Η) The solvent contained in the coating is removed by gentle evaporation, which can prevent rough edges on the surface of the coating film, but the three-coat baking method has the following problems.

某些情況下藉由所謂之切晶片而發生塗覆膜之剝離, 當行進中的車輛撞顺纟卩石,而鶴彡卩石碰撞塗膜時發生切 晶片。於習知經塗覆之複合膜形成方法,例如每次施用塗 15料個別烤乾方法、及二塗膜一次烤乾方法,底塗膜及中間 塗膜分別烤乾與硬化。因此,對耐切晶片的策略可採用形 成耐切晶片塗膜於中間塗膜上方或下方,或經由調整頂塗 膜壳度及底塗膜梵度,形成尚未見脫落之中間塗膜來達成。 例如JP-A Νο.2002-249699及JP-A Νο.9-208882描述一 20種切晶片打底劑塗覆組成物,以及於經塗覆之複合膜形成 而才切晶片塗膜。 此外,JP-ANo.6-256714或JP-ANo.6-254482中,由中 間塗料組成物觀點來研究改良耐切晶片性質,但其改良程 度不足以用於三塗膜一次烤乾方法。 6 200427797 t ^^明内容;1 發明概要 本發明解決習知問題,本發明之目的係提供一種經由 三塗膜一次烤乾方法形成具有良好外觀,特別為光澤性質 5 及絕佳耐切晶片性質之經塗覆之複合薄膜之方法。 本發明提供一種製造一經塗覆之複合薄膜之方法,包 含形成一電塗覆薄膜於一基材上,以及然後以濕於濕方式 連續施用一種中間塗料、一種底塗料以及一種透明塗料, 接著一次烤乾與硬化所施用之三層,其中 10 該烤乾與硬化包括一低溫加熱階段,係於硬化溫度之 25%至80%溫度加熱經歷硬化時間之5%至3〇%時間;以及一 高溫加熱階段,其係於超過硬化溫度8〇%但不高於12〇%之 溫度加熱經歷硬化時間30%至130%之時間。 C實施方式】 15 較佳實施例之詳細說明 塗膜之形成 於本毛明之經塗覆之複合薄膜形成方法,中間塗膜係 藉中間塗料形成,底塗膜係藉底塗料形成,以及透明塗膜 係藉透明塗料形成,各塗膜係以濕於濕方式接續形成於一 20 基材上。 ” “ I車體用作為基材時,於車體鋼板上預先形成電 儿積腰作騎飿技(通常稱為「底塗膜」)。於施用中間塗料 一 ▲料係藉多階段式塗覆施用,較佳係藉靜電噴塗 作二階段錢€铜;或可毅氣靜電噴塗及/或使用旋轉 7 霧化靜電塗覆機施用,該機器稱作為「微微貝機(# micro) bel)」、「微貝機(# (micr〇) bei)」或「美它貝機 (metabel)」〇 由中間塗料所形成之乾塗膜厚度依據預定用途改變。 多種情況下可使用10微米至60微米厚度。當厚度超過上限 時,影像之銳度降低,於某些情況下於塗層出現例如不均 勻及凹fo等缺點,而當厚度低於下限時,表面可能被遮蓋 而發生不均勻塗層。 於本發明之經塗覆之複合薄膜形成方法,底塗料及透 明塗料係以濕於施方式塗覆於未經硬化之中間塗膜上,來 形成底塗膜及透明塗膜。 用於形成底塗膜之底塗料可藉靜電噴塗施用,或使用 旋轉霧化靜電塗覆機如美它貝機、微微貝機、微貝機等施 用。塗膜之乾厚度狀為5至35微米,且較佳為7至25微米。 當底塗膜厚度超過35微米時,影像銳度降低,某些情況下 出現不均勻或凹陷。當厚度小於5微米時,表面遮蓋性質不 足,偶而出現非均勻塗層(非連續膜狀態)。 當存在有底塗膜所致之非均勻時,或當含 顏料時’形成透明塗膜供保護用,遮蓋所形成之細小凸: 3塗ίΓ二特別較佳使用旋轉霧化靜電塗覆機如微微 ^彳放貝機等而形成塗膜。 透明塗膜之乾厚度較佳為約10微米至80微米, 約2〇m6G微米。當乾厚度超過上限時, 下出現爆開及凹陷等缺陷。當厚度低於下限時,、無 表面不規則。 如此經塗覆之複合薄膜係藉同時加熱硬化。該方法通 稱為三塗膜-次烤乾方法 '經塗覆之複合薄膜厚度大半為 30至30G微米且難為5〇至2電米。當厚度超過上限時, 薄膜之物理性質如溫度週期試驗減低。當厚度低於下限 時,薄膜強度減低。 為了充分硬化施用於基材表面之塗覆層,對熱固塗料 設定硬化條件。當_塗_於未滿足硬化條件之條件下 硬化時’經塗覆之複合薄膜之㈣程度不足,經塗覆之複 合薄膜之效能降低。通常作為熱固塗料之硬化條件,設定 硬化溫度(°c)及硬化時間。 硬化溫度係指當塗覆膜藉習知單_階段加熱方法烤乾 及硬化時,雜塗紅複合薄_在之環境溫度。通常為 經塗覆之複合薄膜放置於其中之乾燥㈣設定的溫度。硬 化溫度係依據經塗覆之複合薄膜之交聯系統反應溫度、以 及實際應用生產線設施決定。 又 硬化時間係指於硬化溫度硬化經塗覆之複合薄膜所需 時間。至於硬化時間,最佳值係依據塗料種類及經塗覆之 稷合膜厚度以實驗方式決定。硬化相伽獲得實際所需 經塗覆之複合薄膜效能之時間決定, 而 ^ 且將只際應用生產線 之設施模式之硬化溫度列入考慮。 於本發明方法,烤乾-硬化經塗覆之三層之牛驟八成 低溫加熱階段及-高溫加熱階段,各個階段進 時間。於短時間進行低溫加熱時’總加熱時間並非:當: 200427797 時間,且工作效率不會減低。考慮因所沉積之揮發成分可 經由進行低溫加熱階段增高,故可避免各層之相混合。 於本舍明之低溫加熱階段,形成於基材表面之熱固塗 料層係於占硬化溫度25%至80%且較佳35至60°/。之溫度加 5熱,經歷5至30%且較佳10至20%硬化時間。當硬化溫度及 硬化時間係在該範圍以外時,技術效果不足。例如當硬化 溫度為14〇艺時,低溫加熱溫度為35t:至112°C且較佳為49 C至84C。當硬化溫度為,低溫加熱溫度為25。〔至 80C且較佳為35°C至60°C。此外,當硬化時間為3〇分鐘時, 1〇低溫加熱時間為2至9分鐘且較佳為3至6分鐘。當硬化時間 為60分鐘時,低溫加熱時間為3至18分鐘錄佳為6至收 鐘。 於高溫加熱階段,熱固塗料層進一步於超過硬化溫度 之8〇%但不命於120%且較佳為之溫度加熱經 5歷硬化日守間之聽至⑽%且較佳$㈣至_%時間。當硬化 溫度及硬化時間超過上限時,應力應變累積,某些情況下 經塗覆之複合薄膜出現裂痕。例如當硬化溫度為丄賊時, 高溫加熱溫度超過112。0但不高於16代且較佳為12代至 15代。當硬化溫度為時,高溫加熱溫度超過8(rc但 20不南於12(TCi較佳為㈣至峨。此外當硬化時間為 ^里可阿'现加熱日守間為10至40分鐘且較佳為15至30分 、·里^硬化日^·間為6G分鐘時,高温加熱時間_至财鐘 且較佳為30至60分鐘。 加熱可使用熟諳技藝人士已知方法進行。通常其上塗 10 200427797 覆有熱固塗料之物件可維持於調整於加熱溫度之乾燥烘箱 内。 特別該方法包括: 一種安置欲塗覆物件於乾燥烘箱之程序,該物件上已 5 經塗覆有熱固塗料,該烘箱係控制於較低溫加熱溫度,維 持經歷低溫加熱時間,以及隨後調整乾燥烘箱溫度至高溫 加熱溫度,以及維持經歷高溫加熱時間; 一種製備隧道型乾燥器之程序,其中兩端之入口及出 口為開啟,乾燥係藉帶式輸送器移動材料於隧道型乾燥器 10 内進行乾燥,將隧道内部分成一低溫區及一高溫區,調整 低溫區溫度於低溫加熱溫度’以及調整南溫區溫度於向溫 加熱溫度,首先將物件通過低溫區經歷低溫加熱時間,以 及隨後將該物件通過南溫區經歷南溫加熱時間,以及 一種程序包含準備一第一乾燥烘箱調整於低溫加熱溫 15 度,以及一第二乾燥烘箱調整於高溫加熱溫度,然後將其 上塗覆有熱固塗料之欲塗覆物件維持於第一乾燥烘箱經歷 低溫加熱時間,以及維持該物件於第二乾燥烘箱經歷高溫 加熱時間。 中間塗膜 20 於本發明之塗膜形成方法,中間塗料用來形成中間塗 膜,中間塗料含有(a)經胺基甲酸酯改性之聚酯樹脂,(b)蜜 胺樹脂,(c)嵌段異氰酸酯化合物,(d)具有芯-殼結構之非水 性分散液樹脂及(e)片狀顏料。中間塗料進一步含有多種有 機或無機著色顏料及增量劑顏料。 11 200427797 經胺基甲酸酯改性之聚酯樹脂(a)可經由含羥基聚酯樹 脂與脂肪族異氰酸酯化合物反應獲得。 通常,聚酯樹脂可經由酸成分如羧酸、酸酐及酸氯與 一羥基醇或多羥基醇縮聚合而製備。本發明使用之含羥基 5 聚酯樹脂含有以酸成分之總莫耳數為基準,80莫耳%或以 上之間苯二甲酸於縮聚合反應使用之酸成分。當間苯二甲 酸於酸成分之含量低於80莫耳%時,所得含羥基聚酯樹脂 之玻璃轉換溫度(Tg)變成低於期望範圍。 間苯二甲酸以外之酸成分例如包括磷苯二甲酸、磷苯 10 二曱酐、四氫磷苯二甲酸、四氫磷苯二甲酐、六氫磷苯二 甲酸、六氫磷苯二甲酐、甲基四氫磷苯二甲酸、甲基四氫 石舞苯二曱酐、希蜜酸(himic acid)酐、偏苯三酸、偏苯三酐、 均苯四酸、均苯四酐、對苯二甲酸、順丁烯二酸、順丁烯 二酐、反丁稀二酸、衣康酸、己二酸、壬二酸、癸二酸、 15 丁二酸、丁二酐、十二碳烯基丁二酸、十二碳烯基丁二酐 等。另外至於酸成分,可含有常用於製備聚酯樹脂之多價 羧酸及多價羧酸酐以外之酸。此種酸例如包括一羧酸及羥 基羧酸。至於用於製備含羥基之聚酯樹脂之酸,可單獨使 用間苯二甲酸,或可混合其它酸來使用。 20 多經基醇例如包括乙二醇、二乙二醇、多乙二醇、丙 二醇、二丙二醇、多丙二醇、新戊二醇、1,2-丁二醇、1,3-丁 二醇、1,4-丁 二醇、2,3-丁 二醇、1,5-戊二醇、1,6-己二醇、 1,4-壞己二醉、2,2-二甲基-3-經基丙基-2,2-二甲基-3-經基丙 酸酯、2,2,2-三甲基-1,3-戊二醇、多四亞甲基醚二醇、多己 12 200427797 内酯多元醇、甘油、山梨糖醇、安尼糖醇(annit〇1)、三羥甲 基乙烷、三羥甲基丙烷、三羥甲基丁烷、己三醇、季戊四 醇、二季戊四醇等。 於製備含羥基之聚酯樹脂時,除了酸成分及多羥基醇 5之外,也可使用其它可與此等成分反應之成分。此等其它 成分例如包括酸氯、内酯類之酸衍生物、環氧化合物及乾 性油及半乾性油及其脂肪酸衍生物。内酯類經由開環加成 至多價羧酸及多羥基醇所形成之聚酯樹脂而可形成接枝 鏈。内酯類例如包括冷-丙内酯、二甲基丙内酯、丁内酯、 10 戊内酯、ε _己内酯、γ _己内酯、γ _辛内酯、巴豆内酯、 戊内酯、己内酯等。特別以ε _己内酯為最佳。特例 包括一環氧基化合物如卡久拉(Carjula) Ε(殼牌化學公司製 造)己内酯類。 含經基之聚酯樹脂具有玻璃轉換溫度(Tg)為4〇它至85 15 °C且較佳為45°C至75它。當玻璃轉換溫度(Tg)低於40°C 時,薄膜硬度減低。當Tg高於80°c時,耐切晶片效能減低。 脂肪族異氰酸酯化合物例如包括六亞甲基二異氰酸 酯、二甲基六亞甲基二異氰酸酯、環己烷二異氰酸酯、 一壞己基甲烷-4,4-二異氰酸酯、甲基環己烷二異氰酸酯及 20異佛爾S同二異氰酸酯。 特別由經塗覆之複合薄膜之耐切晶片效能及耐候性觀 點^交佳使用六亞甲基二異氰酸g旨或三甲基六亞甲基二異 鼠酸酯。可使用雙縮脲、異氰尿酸酯及其加合物。 含羥基聚酯樹脂與脂肪族異氰酸酯化合物之反應可經 13 200427797 由熟諳技藝人士已知方法進行。 經胺基甲酸酯改性之聚酯樹脂(a)具有數目平均分子量 (Μη)為1500至3000且較佳為17〇〇至25〇〇。當分子量小於 1500時,工作性及硬化性不足。當分子量超過3〇〇〇時,於 5塗覆時之非揮發物含量過低,工作能力反而低劣。此處數 目平均分子量係藉GPC方法,使用聚苯乙烯作為標準品測 定。 經胺基甲酸酯改性之聚酯樹脂⑷具有羥基值(〇HV)較 佳為30至180及更佳為40至160。當羥基值超過180,經塗覆 10 之複合薄膜之防水性降低。當羥基值小於30時,經塗覆之 複合薄膜之硬化性降低。此外,樹脂具有酸價(AV)較佳為3 至30毫克KOH/克,更佳為5至25毫克KOH/克。當酸價超過 30毫克KOH/克時,經塗覆之複合薄膜之防水性降低。當酸 價小於3毫克KOH/克時,經塗覆之複合薄膜之硬化性降低。 15 含於中間塗料之經胺基甲酸酯改性之聚酯樹脂(a)含 量,以樹脂之固型物含量為基準,含量為40至56%重量比 且較佳43至50%重量比。當含量小於40%重量比時,耐切晶 片效能變不足。當含量超過56°/。重量比時,經塗覆之複合 薄膜硬度降低。 20 考慮經由含括以胺基甲酸酯改性之聚酯樹脂作為中間 塗料成分,經塗覆之複合薄膜之彈性改良,經塗覆之複合 薄膜之耐切晶片性也改良。 後文說明之蜜胺樹脂(b)及嵌段異氰酸酯化合物(〇為 用於硬化以胺基甲酸酯改性之聚酯樹脂0)之成分。 14 蜜胺樹脂⑼並無特殊限制,但包括甲基化蜜胺樹脂、 丁基化蜜胺樹脂或甲基、丁其、β入以_ 合性蛍胺樹脂。例如包括 「賽莫(Cymel)-303」、「赛簟^ 胥吴254」、優邦(U ban )128」及「優 邦20N60」係由三井東壓公引山 、 1出售’以及「蘇敏那(sumimar) 系列」由住友化學公司出售。 以樹脂固體於塗料之合旦舌s力甘处 丨τ心3里重1為基準,中間塗料之蜜 胺樹脂(b)含量為1 0至30%舌曰α 土 主川/°重Ϊ比且較佳為15至25%重量 比田虫胺树月日之含夏低於1〇%重量比時,經塗覆之複合 10 薄膜之硬化不足。而當含量超過20%重量比時,硬化後之 經塗覆之複合薄膜太硬且太脆。 甘入段異氰酉夂酉日化合物⑷係經由添加嵌段劑至脂肪族異 氛酸醋或其衍生物獲得。當纽異聽自旨化合物被加熱 時,後段劑解離,而產生異氰酸基,異氰酸基與以胺基甲 酸酯改性之聚酯樹脂之羥基反應而硬化材料。 15In some cases, the peeling of the coating film occurs by so-called dicing wafers, and the dicing wafers occur when a moving vehicle hits vermiculite and the crane vermiculite hits the coating film. In the conventional method of forming a coated composite film, for example, an individual baking method for applying 15 coating materials and a one-time baking method for two coating films, the base coating film and the intermediate coating film are respectively baked and hardened. Therefore, strategies for cutting-resistant wafers can be achieved by forming a cutting-resistant wafer coating film above or below the intermediate coating film, or by adjusting the top coating film shell degree and the bottom coating film vandal degree to form an intermediate coating film that has not yet come off. For example, JP-A No. 2002-249699 and JP-A No. 9-208882 describe 20 kinds of wafer-cutting primer coating compositions, and the wafer coating film is cut after the coated composite film is formed. In addition, in JP-A No. 6-256714 or JP-A No. 6-254482, the improvement of the cut-resistant wafer properties is studied from the viewpoint of an intermediate coating composition, but the degree of improvement is not sufficient for a three-coat film drying method. 6 200427797 t ^^ Description; 1 Summary of the invention The present invention solves the conventional problems. The purpose of the present invention is to provide a three-coat film drying method to form a good appearance, especially the gloss 5 and excellent chip resistance. Method of coated composite film. The invention provides a method for manufacturing a coated composite film, comprising forming an electro-coated film on a substrate, and then continuously applying an intermediate coating, a base coating, and a transparent coating in a wet-on-wet manner, and then once Three layers applied for baking and hardening, of which 10 the baking and hardening include a low-temperature heating stage at 25% to 80% of the hardening temperature and heating for 5% to 30% of the hardening time; and a high temperature In the heating stage, it is heated at a temperature exceeding 80% but not higher than 120%, and the heating time is 30% to 130%. Embodiment C] 15 Detailed description of the preferred embodiment of the method for forming a coated composite film formed in Ben Maoming, the intermediate coating film is formed by an intermediate coating, the base coating film is formed by a base coating, and the transparent coating is formed. The film system is formed by a transparent paint, and each coating film is sequentially formed on a 20 substrate in a wet-on-wet manner. "" When the car body is used as a base material, an electric waist is formed on the car body steel plate in advance as a riding technique (commonly called a "bottom coating film"). In the application of the intermediate coating, the material is applied by multi-stage coating, preferably by electrostatic spraying for two-stage copper; or by electrostatic spraying and / or using a rotary 7 atomizing electrostatic coating machine, the The machine is called "# micro) bel", "# (micr〇) bei" or "metabel". The thickness of the dry coating film formed by the intermediate coating Intended use changed. A thickness of 10 to 60 microns can be used in many cases. When the thickness exceeds the upper limit, the sharpness of the image decreases, and in some cases, defects such as unevenness and concave fo appear in the coating, and when the thickness is lower than the lower limit, the surface may be covered and uneven coating may occur. In the method for forming a coated composite film of the present invention, a primer and a transparent coating are applied on an unhardened intermediate coating film by wet application to form a base coating film and a transparent coating film. The base coating used to form the base coating film can be applied by electrostatic spraying, or by using a rotary atomizing electrostatic coater such as a meta shell, pico shell, or micro shell machine. The dry thickness of the coating film is 5 to 35 microns, and preferably 7 to 25 microns. When the thickness of the base coating film exceeds 35 micrometers, the sharpness of the image is reduced, and unevenness or dents appear in some cases. When the thickness is less than 5 micrometers, the surface covering properties are insufficient, and occasionally a non-uniform coating (discontinuous film state) appears. When there is non-uniformity caused by the base coating film, or when it contains pigments, 'form a transparent coating film for protection, covering the small protrusions formed: 3 coating Γ 2 is particularly preferred to use a rotary atomizing electrostatic coating machine such as The coating film is formed by slightly releasing the shell machine. The dry thickness of the transparent coating film is preferably about 10 μm to 80 μm, and about 20 μm to 6 μm. When the dry thickness exceeds the upper limit, defects such as bursting and dents appear below. When the thickness is below the lower limit, there is no surface irregularity. The composite film thus coated is hardened by simultaneous heating. This method is commonly referred to as the three-coat film-sub-bake method. The thickness of the coated composite film is mostly 30 to 30 G micrometers and difficult to be 50 to 2 electric meters. When the thickness exceeds the upper limit, the physical properties of the film, such as a temperature cycle test, decrease. When the thickness is lower than the lower limit, the film strength decreases. In order to sufficiently harden the coating layer applied to the surface of the substrate, the curing conditions are set for the thermosetting paint. When _coating_ is hardened under conditions that do not satisfy the hardening conditions, the coated composite film is insufficient in degree, and the efficiency of the coated composite film is reduced. Generally used as the curing conditions of thermosetting coatings, setting the curing temperature (° c) and curing time. The hardening temperature refers to the ambient temperature where the coating film is dried and hardened by the conventional single-stage heating method. It is usually the temperature at which the coated composite film is placed to dry. The hardening temperature is determined based on the reaction temperature of the crosslinked system of the coated composite film and the actual production line facilities. The hardening time refers to the time required to harden the coated composite film at the hardening temperature. As for the hardening time, the optimal value is determined experimentally based on the type of coating and the thickness of the coated composite film. The time required for the hardening phase to obtain the actual required performance of the coated composite film is determined, and the hardening temperature of the facility mode of the application-only production line is considered. In the method of the present invention, the coated three-layered beef is roasted and hardened in a low temperature heating stage and a high temperature heating stage, and each stage is advanced in time. When performing low-temperature heating in a short time, the total heating time is not: when: 200427797 time, and the working efficiency will not be reduced. It is considered that because the deposited volatile components can be increased through the low-temperature heating stage, the mixing of the layers can be avoided. In the low temperature heating stage of Ben Sheming, the thermosetting coating layer formed on the surface of the substrate is 25% to 80% and preferably 35 to 60 ° /. The temperature is increased by 5 hours, and the hardening time is 5 to 30% and preferably 10 to 20%. When the curing temperature and curing time are outside this range, the technical effect is insufficient. For example, when the hardening temperature is 140 ° C, the low-temperature heating temperature is 35t: to 112 ° C and preferably 49C to 84C. When the hardening temperature is, the low-temperature heating temperature is 25. [To 80C and preferably 35 ° C to 60 ° C. Further, when the hardening time is 30 minutes, the 10 low-temperature heating time is 2 to 9 minutes and preferably 3 to 6 minutes. When the hardening time is 60 minutes, the low-temperature heating time is 3 to 18 minutes, and the best time is 6 to closing hours. In the high-temperature heating stage, the thermosetting coating layer is further heated at a temperature exceeding 80% of the hardening temperature but not at 120% and preferably at a temperature of 5% and preferably $ ㈣ to _ %time. When the hardening temperature and hardening time exceed the upper limit, stress and strain accumulate, and in some cases cracks appear on the coated composite film. For example, when the hardening temperature is a thief, the high-temperature heating temperature exceeds 112. 0 but is not higher than 16th generation and preferably 12th to 15th generation. When the hardening temperature is high, the high-temperature heating temperature exceeds 8 (rc but 20 is not less than 12 (TCi is preferably P. to E. In addition, when the hardening time is ^ Rico ', the current heating day is 10 to 40 minutes and more It is preferably 15 to 30 minutes, and the hardening time is 6G minutes, and the high-temperature heating time is _ to the financial clock, and preferably 30 to 60 minutes. Heating can be performed by a method known to those skilled in the art. Usually, the upper coating is applied. 10 200427797 Objects covered with thermosetting coating can be maintained in a drying oven adjusted to the heating temperature. In particular, the method includes: A procedure for placing the object to be coated in the drying oven, the object has been coated with thermosetting coating. The oven is controlled at a lower temperature heating temperature to maintain the low-temperature heating time, and then adjust the drying oven temperature to a high-temperature heating temperature, and maintain the high-temperature heating time; a procedure for preparing a tunnel-type dryer, in which the inlets at both ends and The outlet is open. The drying is carried out by the belt conveyor to move the material in the tunnel dryer 10, and the inside of the tunnel is divided into a low temperature zone and a high temperature zone. The temperature in the low temperature zone is adjusted to Warming temperature 'and adjusting the temperature of the south temperature zone to the warming temperature, first passing the object through the low temperature zone to the low temperature heating time, and then passing the object through the south temperature zone to the south temperature heating time, and a program including preparing a first The drying oven is adjusted to a low-temperature heating temperature of 15 degrees, and a second drying oven is adjusted to a high-temperature heating temperature, and then the object to be coated with the thermosetting coating is maintained in the first drying oven to undergo the low-temperature heating time, and to maintain the The object is subjected to high-temperature heating time in the second drying oven. Intermediate coating film 20 In the coating film forming method of the present invention, the intermediate coating is used to form an intermediate coating film, and the intermediate coating contains (a) a urethane-modified polyester Resin, (b) melamine resin, (c) block isocyanate compound, (d) non-aqueous dispersion resin with core-shell structure and (e) flake pigment. The intermediate coating further contains various organic or inorganic pigments and Expander pigment. 11 200427797 Polyurethane resin modified with urethane (a) can pass through hydroxyl-containing polyester resin and aliphatic isocyanate The compound is obtained by reaction. Generally, the polyester resin can be prepared by polycondensation of an acid component such as a carboxylic acid, an acid anhydride, and acid chloride with a monohydric alcohol or a polyhydric alcohol. The hydroxyl-containing 5 polyester resin used in the present invention contains a total of acid components. Molar number as a reference, 80 mol% or more of the acid component used in the polycondensation reaction of phthalic acid. When the content of isophthalic acid in the acid component is less than 80 mol%, the obtained hydroxyl-containing polyester resin The glass transition temperature (Tg) becomes lower than a desired range. The acid component other than isophthalic acid includes, for example, phosphophthalic acid, phosphobenzene 10 dianhydride, tetrahydrophosphoric acid, tetrahydrophosphophthalic anhydride, and Hydrophosphalic acid, hexahydrophosphic phthalic anhydride, methyltetrahydrophosphoric acid, methyltetrahydrophthalic anhydride, himic acid anhydride, trimellitic acid, trimellitic acid Trianhydride, pyromellitic acid, pyromellitic anhydride, terephthalic acid, maleic acid, maleic anhydride, fumaric acid, itaconic acid, adipic acid, azelaic acid, sebacic acid Acid, 15 succinic acid, succinic anhydride, dodecenyl succinic acid, dodecenyl succinic anhydride, and the like. In addition, the acid component may contain acids other than polyvalent carboxylic acids and polyvalent carboxylic anhydrides which are commonly used in the preparation of polyester resins. Such acids include, for example, monocarboxylic acids and hydroxycarboxylic acids. As for the acid used for preparing the hydroxyl-containing polyester resin, isophthalic acid may be used alone, or other acids may be used in combination. 20 Polyacryl alcohols include, for example, ethylene glycol, diethylene glycol, polyethylene glycol, propylene glycol, dipropylene glycol, polypropylene glycol, neopentyl glycol, 1,2-butanediol, 1,3-butanediol, 1,4-butanediol, 2,3-butanediol, 1,5-pentanediol, 1,6-hexanediol, 1,4-adipylene, 2,2-dimethyl-3 -Ethylpropyl-2,2-dimethyl-3-acrylic acid propionate, 2,2,2-trimethyl-1,3-pentanediol, polytetramethylene ether glycol, polyether Hexa 12 200427797 lactone polyol, glycerol, sorbitol, annotol1, trimethylolethane, trimethylolpropane, trimethylolbutane, hexanetriol, pentaerythritol, Dipentaerythritol and so on. In the preparation of the hydroxyl-containing polyester resin, in addition to the acid component and the polyhydric alcohol 5, other components that can react with these components can also be used. These other components include, for example, acid chlorides, acid derivatives of lactones, epoxy compounds, and dry and semi-dry oils and fatty acid derivatives thereof. Lactones can form graft chains by ring-opening addition to polyester resins formed from polyvalent carboxylic acids and polyhydric alcohols. Lactones include, for example, cold-propiolactone, dimethylpropiolactone, butyrolactone, 10-valerolactone, ε-caprolactone, γ-caprolactone, γ-caprolactone, crotonolide, pentyl Lactone, caprolactone, etc. Particularly, ε_caprolactone is most preferable. Specific examples include an epoxy compound such as Carjula E (manufactured by Shell Chemical Co.) caprolactones. The warp-containing polyester resin has a glass transition temperature (Tg) of 40 to 85 15 ° C and preferably 45 to 75 ° C. When the glass transition temperature (Tg) is lower than 40 ° C, the film hardness decreases. When Tg is higher than 80 ° c, the cut-resistant chip performance is reduced. The aliphatic isocyanate compound includes, for example, hexamethylene diisocyanate, dimethylhexamethylene diisocyanate, cyclohexane diisocyanate, mono-hexylmethane-4,4-diisocyanate, methylcyclohexane diisocyanate, and 20 Isophor S is the same as diisocyanate. In particular, the cut-resistant wafer performance and weather resistance of the coated composite film ^ good use of hexamethylene diisocyanate g or trimethylhexamethylene diisomyrate. Biuret, isocyanurate and adducts thereof can be used. The reaction of the hydroxyl-containing polyester resin with the aliphatic isocyanate compound can be carried out by a method known to those skilled in the art through 13 200427797. The urethane-modified polyester resin (a) has a number average molecular weight (Mη) of 1500 to 3000 and preferably 17,000 to 250,000. When the molecular weight is less than 1500, workability and hardenability are insufficient. When the molecular weight exceeds 3,000, the non-volatile content at the time of 5 coating is too low, but the working ability is inferior. The number average molecular weight here is determined by GPC method using polystyrene as a standard. The urethane-modified polyester resin ⑷ has a hydroxyl value (OHV) of preferably 30 to 180 and more preferably 40 to 160. When the hydroxyl value exceeds 180, the water resistance of the 10-coated composite film decreases. When the hydroxyl value is less than 30, the hardenability of the coated composite film decreases. In addition, the resin has an acid value (AV) of preferably 3 to 30 mg KOH / g, more preferably 5 to 25 mg KOH / g. When the acid value exceeds 30 mg KOH / g, the water resistance of the coated composite film decreases. When the acid value is less than 3 mg KOH / g, the hardenability of the coated composite film decreases. 15 Urethane-modified polyester resin (a) contained in the intermediate coating, based on the solid content of the resin, the content is 40 to 56% by weight and preferably 43 to 50% by weight . When the content is less than 40% by weight, the cut-resistant wafer efficiency becomes insufficient. When the content exceeds 56 ° /. At a weight ratio, the hardness of the coated composite film decreases. 20 Considering the improvement of the elasticity of the coated composite film by including a urethane-modified polyester resin as an intermediate coating component, the chip resistance of the coated composite film is also improved. The components of the melamine resin (b) and the block isocyanate compound (0 is used to harden the urethane-modified polyester resin 0) described later. 14 Melamine resins are not particularly limited, but include methylated melamine resins, butylated melamine resins, or methyl, butane, and beta-containing amidine resins. For example, "Cymel-303", "Sai ^ ^ Wu Wu 254", "U Ban" 128 "and" Ubon 20N60 "are sold by Mitsui Tokiyama, 1" and "Su Min The "sumimar series" is sold by Sumitomo Chemical. Based on the solid weight of the resin in the coating, the weight of the resin is 3, and the weight of the melamine resin (b) in the intermediate coating is 10 to 30%. And preferably, when 15 to 25% by weight is less than 10% by weight based on the summer content of azoxystrobin, the hardening of the coated composite 10 film is insufficient. When the content exceeds 20% by weight, the coated composite film after hardening is too hard and too brittle. Isocyanuric compounds of Ganjin segment are obtained by adding a blocking agent to an aliphatic isocyanate or a derivative thereof. When the neostigmine compound is heated, the latter dissociates to produce isocyanate groups, which react with the hydroxyl groups of the polyester resin modified with urethane to harden the material. 15

脂肪族異氰酸酯及其衍生物例如包括用於製備以胺基 甲酸Ss改性之聚酯樹脂之化合物。嵌段劑例如包括具有活 性亞甲基之化合物如乙醯基丙酮、乙醯基乙酸乙酯及丙二 酸乙酯。經由使用嵌段劑,經塗覆之複合薄膜之彈性改良, 經塗覆之複合薄膜之耐切晶片性也改良。 甘欠段兴氣酸自旨化合物例如由旭化學工業公司出隹為活 性亞甲基型嵌段異氰酸酯「枉蘭内特(Duranate) MF-K60X」。 中間塗料之嵌段異氰酸醋化合物(c)之含量,以塗料之 樹脂固體重量含量為基準,為15至30%重量比且較佳為17 15 200427797 至25%重量比。各八b y , 里比田3罝小於15%重量比時,硬化性不足;而 當含量超=%重量比時,硬化後之薄膜太硬也太脆。 ’、有心砍結構之非水性分散液樹脂⑷可經由分散安 定樹脂與可共聚合單體於含有機溶劑之混合溶液共聚合而 製備,共聚合獲得樹脂呈非交聯樹絲子,姉子不溶於 祕合溶液。欲於分懿安定樹脂存在下,共聚合來獲得 非父如_日粒子之單體並無特殊限制,只要為可基團聚合 不飽和單體即可。The aliphatic isocyanate and its derivative include, for example, a compound for producing a polyester resin modified with urethane Ss. Blocking agents include, for example, compounds having an active methylene group such as ethyl acetone, ethyl acetoacetate, and ethyl malonate. By using a blocking agent, the elasticity of the coated composite film is improved, and the chip resistance of the coated composite film is also improved. The glycine-dans gas acid compounds are produced, for example, by Asahi Chemical Industry Co., Ltd. as active methylene block isocyanate "Duranate MF-K60X". The content of the block isocyanate compound (c) of the intermediate coating is 15 to 30% by weight and preferably 17 15 200427797 to 25% by weight based on the resin solid content of the coating. When each b b y, Libita 3 罝 is less than 15% by weight, the hardenability is insufficient; and when the content is over =% by weight, the hardened film is too hard and brittle. ', Non-aqueous dispersion resin with a heart-cut structure can be prepared by copolymerizing a dispersion stabilizer resin and a copolymerizable monomer in a mixed solution containing an organic solvent. The copolymerization obtains a resin that is non-crosslinked, and the sister is insoluble. In the secret solution. There is no particular limitation on the monomers to be copolymerized to obtain non-parent particles in the presence of a stable stabilizer resin, as long as it is a group-polymerizable unsaturated monomer.

為了合成分散液安定樹脂及非水性分散液,較佳使用 1〇具有官能基之可聚合單體,原因在於具有官能基之非水性 分散液可與硬化劑連同與含官能基之分散液安定樹脂反應 而形成-種三維交聯之經塗覆之複合薄膜。 刀政液女疋㈣亚無特殊限制,只要可於有機溶劑穩 定合成非水性分散液即可。特別較佳使用丙烯酸系樹脂、In order to synthesize dispersion stabilizer resins and non-aqueous dispersions, it is preferred to use 10 polymerizable monomers having functional groups, because non-aqueous dispersions having functional groups can be combined with hardeners and dispersion stabilizers containing functional groups. The reaction forms a three-dimensionally cross-linked coated composite film. Daozhengye Nuwaya is not limited as long as it can stably synthesize a non-aqueous dispersion in an organic solvent. Particularly preferred is the use of acrylic resins,

15㈣樹脂、聚嶋脂、聚碳_旨樹脂、聚胺基甲酸醋樹脂 等’其具有值10至25G且較㈣謹,酸值G至職 克KOH/克且較佳〇至%毫克κ⑽克以及數目平均分子量 800至100,_且較佳為、_,_。當前述各項參數超 過上限時’樹脂的操控性質降低,非水性分散液之操控性 20質也降低。當參數低於下限時,塗膜可能被解吸附,當調 配成經塗覆之複合薄膜時,粒子穩定性降低。 分散液安定樹脂之合成方法並無特殊限制,但較佳包 括於基團聚合引發劑存在下經由基團聚合獲得樹脂之方 法’以及經由縮合方法或加成反應獲得樹脂之方法。此外, 16 200427797 用於獲得分散液安錢脂之單體可依據樹脂性質適當選 用’但較佳使料有官《(㈣基、酸鱗)之單體,該等 官能基為用於合成非水性分散液之可聚合單體所具有⑶ 後詳述);進—步若有所需,可使用具有官能基如縮水甘油 5 基、異氰酸基等之單體。 此外,分散液安定樹脂與可聚合單體之重量比可依據 使用目的任意選用。例如以兩種成分總重為基準,分散液 安定樹脂為3至80%重量比,特別5至6〇%重量比,可聚合單 體為97至20%重量比且特別為95至4〇%重量比。此外,以總 10重為基準,分散液安定樹脂及可聚合單體於有機溶劑之總 濃度較佳為30至80%重量比,特別為4〇至6〇%重量比。 非水性分散液可經由於分散液安定樹脂存在下,聚合 可基團聚合單體獲得。於本非水性分散液,較佳羥基值為 50至400,較佳為100至300,酸價為0至200毫克K0H/克且 15較佳為〇至50毫克KOH/克以及平均粒子直徑(1)5())為〇〇5至 10微米且較佳為〇·1至2微米。當參數低於下限時,無法維 持粒子形狀。而當參數超過上限時,分散於塗料之穩定性 下降。 用來合成非水性分散液之具有官能基之可聚合單體之 20 代表例包括含羥基之單體如(甲基)丙烯酸羥基乙酯、(甲基) 丙烯酸經基丙酯、(甲基)丙烯酸羥基丁酯、(甲基)丙烯酸羥 基甲S旨、丙烯醇,以及(甲基)丙烯酸羥基乙酯與ε -己内酯 之加合物。 另一方面,具有酸基之單體例如包括具有羧基、磺酸 17 200427797 基等之可聚合單體。具有羧基之單體例如包括(甲基)丙烯 酸、巴豆酸、乙基丙烯酸、丙基丙烯酸、異丙基丙烯酸、 衣康酸、順丁烯二酐、反丁烯二酸等。具有磺酸基之可聚 合單體例如包括第三丁基丙烯醯胺磺酸等。當使用具有酸 5 基之可聚合單體時,較佳部分酸基為羧酸基。 此外,具有官能基之可聚合單體例如包括含縮水甘油 基之不飽和單體如(甲基)丙烯酸縮水甘油酯;及含異氰酸基 之不飽和單體如間-異丙烯基二甲基苄基異氰酸 酯、丙烯酸異氰酸基乙酯等。 10 其它可聚合单體例如包括(甲基)丙細酸烧基醋’例如 (甲基)丙烯酸甲酯、(曱基)丙烯酸乙酯、(甲基)丙烯酸異丙 酯、(甲基)丙烯酸正丙酯、(甲基)丙烯酸正丁酯、(甲基)丙 烯酸第三丁酯、(甲基)丙烯酸異丁酯、(甲基)丙烯酸2-乙基 己酯、(曱基)丙烯酸正辛酯、(甲基)丙烯酸月桂酯、(曱基) 15 丙烯酸硬脂酯及(甲基)丙烯酸十三烷酯;油脂肪酸與具有環 氧乙烷結構之丙烯酸或曱基丙烯酸酯單體之加成反應產物 (例如硬脂酸與甲基丙烯酸縮水甘油酯之加成反應產物 等);含Q或以上烷基之環氧乙烷化合物與丙烯酸或甲基丙 烯酸之加成反應產物、苯乙烯、α-甲基苯乙烯、鄰-曱基笨 20 乙烯、間-曱基苯乙烯、對-甲基苯乙烯、對-第三丁基笨乙 烯、(曱基)丙烯酸苄酯、衣康酸酯(衣康酸二甲酯)、順丁稀 二酸酯(順丁烯二酸二甲酯)、反丁烯二酸酯(反丁烯二酸二 甲酯);以及其它可聚合單體例如丙烯腈、甲基丙稀腈、甲 基異丙烯基甲酮、乙酸乙烯酯、微巴(Veoba)單體(殼牌化學 18 A司製造’商品名)、丙酸乙烯酯、特戊酸乙烯酯、丙峻乙 烯酉曰、乙烯、丙烯、丁二烯、丙烯酸N,N_二甲基胺基乙_、 甲基丙歸酸N,N-二甲基胺基乙酯、丙烯醯胺及乙烯基Π比呀。 車交佳用於獲得非水性分散液之聚合反應係於基團聚人 弓丨發劑存在下進行。基團聚合引發劑例如包括以偶氮為主 之引發劑,例如2,2,_偶氮貳異丁腈及2,2,-偶氮貳(2,‘二甲 基戊腈)、過氧化笨甲醯、過氧化月桂醯、過辛酸第三丁蜎 等。較佳相對於總量1〇〇份重量比可聚合單體,此種引發叫 用ΐ為0.2至1〇份重量比且較佳為〇.5至5份重量比。較佳用 於獲得於一種含分散液安定樹脂之有機溶劑之非水性分散 液之聚合反應通常係於約6〇。(:至16〇。(:之溫度範圍進行1至 15小時。 此外’非水性分散液為與交聯聚合物粒子不同之塗料 中之粒子成分,但其具有於經塗覆之複合薄膜不會形成粒 子結構之特性。換言之,非水性分散液與交聯聚合物粒子 之差異在於,由於粒子並無交聯位置,故粒子形狀於烤乾 過程改變,可為樹脂成分。15% resin, polyester resin, polycarbon resin, polyurethane resin, etc., which have a value of 10 to 25G and are more cautious, and have an acid value of G to KOH / g and preferably 0 to% mg. And the number average molecular weight is 800 to 100, and preferably, _, _. When the foregoing parameters exceed the upper limit, the handling properties of the resin are reduced, and the handling properties of the non-aqueous dispersion are also reduced. When the parameter is lower than the lower limit, the coating film may be desorbed, and when formulated into a coated composite film, the particle stability is reduced. The method for synthesizing the dispersion stabilizer resin is not particularly limited, but preferably includes a method of obtaining a resin through group polymerization in the presence of a group polymerization initiator 'and a method of obtaining a resin through a condensation method or addition reaction. In addition, 16 200427797 monomers used to obtain dispersions of antacene can be appropriately selected according to the properties of the resin, but the monomers ((fluorenyl, acid scale)) are preferably used, and these functional groups are used for the synthesis of non- The polymerizable monomers of the aqueous dispersion are detailed later (3); further-if necessary, monomers having functional groups such as glycidyl 5 group, isocyanate group, etc. can be used. In addition, the weight ratio of the dispersion stabilizer resin to the polymerizable monomer can be arbitrarily selected according to the purpose of use. For example, based on the total weight of the two components, the dispersion stabilizer resin is 3 to 80% by weight, particularly 5 to 60% by weight, and the polymerizable monomer is 97 to 20% by weight and particularly 95 to 40%. weight ratio. In addition, based on the total weight of 10, the total concentration of the dispersion stabilizer resin and the polymerizable monomer in the organic solvent is preferably 30 to 80% by weight, and particularly 40 to 60% by weight. The non-aqueous dispersion can be obtained by polymerizing a group-polymerizable monomer in the presence of a dispersion stabilizer resin. In this non-aqueous dispersion, the preferred hydroxyl value is 50 to 400, preferably 100 to 300, the acid value is 0 to 200 mg KOH / g and 15 is preferably 0 to 50 mg KOH / g and the average particle diameter ( 1) 5 ()) is from 0.05 to 10 microns and preferably from 0.1 to 2 microns. When the parameter is below the lower limit, the particle shape cannot be maintained. When the parameter exceeds the upper limit, the stability of the dispersion in the coating decreases. 20 representative examples of polymerizable monomers having functional groups for synthesizing non-aqueous dispersions include hydroxyl-containing monomers such as hydroxyethyl (meth) acrylate, propyl (meth) acrylate, and (meth) Hydroxybutyl acrylate, hydroxymethyl (meth) acrylate, acryl alcohol, and adducts of hydroxyethyl (meth) acrylate and ε-caprolactone. On the other hand, the monomer having an acid group includes, for example, a polymerizable monomer having a carboxyl group, a sulfonic acid 17 200427797 group, and the like. The monomer having a carboxyl group includes, for example, (meth) acrylic acid, crotonic acid, ethacrylic acid, propyl acrylic acid, isopropyl acrylic acid, itaconic acid, maleic anhydride, fumaric acid, and the like. The polymerizable monomer having a sulfonic acid group includes, for example, tertiary butylacrylamide sulfonic acid and the like. When a polymerizable monomer having an acid group is used, it is preferable that a part of the acid group is a carboxylic acid group. Further, the polymerizable monomer having a functional group includes, for example, a glycidyl group-containing unsaturated monomer such as glycidyl (meth) acrylate; and an isocyanate group-containing unsaturated monomer such as m-isopropenyldimethylformate. Benzyl isocyanate, ethyl isocyanate and the like. 10 Other polymerizable monomers include, for example, (meth) acrylic acid, such as methyl (meth) acrylate, ethyl (fluorenyl) acrylate, isopropyl (meth) acrylate, and (meth) acrylic acid. N-propyl ester, n-butyl (meth) acrylate, third butyl (meth) acrylate, isobutyl (meth) acrylate, 2-ethylhexyl (meth) acrylate, n-butyl (meth) acrylate Octyl ester, lauryl (meth) acrylate, (fluorenyl) 15 stearyl acrylate and tridecyl (meth) acrylate; oil fatty acids and acrylic or fluorenyl acrylate monomers having an ethylene oxide structure Addition reaction products (such as the addition reaction products of stearic acid and glycidyl methacrylate, etc.); addition reaction products of ethylene oxide compounds containing Q or more alkyl groups and acrylic acid or methacrylic acid, styrene , Α-methylstyrene, ortho-fluorenyl 20 ethylene, m-fluorenyl styrene, p-methylstyrene, p-tert-butyl styrene, benzyl (fluorenyl) acrylate, itaconic acid Ester (dimethyl itaconic acid), maleate (maleic acid Methyl ester), fumarate (dimethyl fumarate); and other polymerizable monomers such as acrylonitrile, methyl acrylonitrile, methyl isopropenyl ketone, vinyl acetate, Veoba monomer ("trade name" manufactured by Shell Chemicals 18A Division), vinyl propionate, vinyl pivalate, propylene oxide, ethylene, propylene, butadiene, acrylic acid N, N_dimethyl Aminoaminoethyl, methylpropionate N, N-dimethylaminoethyl, acrylamide, and vinyl. Che Jiaojia's polymerization reaction used to obtain a non-aqueous dispersion was carried out in the presence of a group of human hair bowers. Group polymerization initiators include, for example, azo-based initiators, such as 2,2, -azo azoisobutyronitrile and 2,2, -azo hydrazone (2, 'dimethylvaleronitrile), peroxide Stupid formazan, laurel peroxide, tertiary butanone, etc. The polymerizable monomer is preferably 100 parts by weight with respect to the total amount, and such an initiator is 0.2 to 10 parts by weight and more preferably 0.5 to 5 parts by weight. The polymerization reaction which is preferably used to obtain a non-aqueous dispersion in an organic solvent containing a dispersion stabilizer resin is usually about 60. (: To 160. The temperature range is from 1 to 15 hours. In addition, the 'non-aqueous dispersion liquid is a particle component in a coating material different from the cross-linked polymer particles, but it has no effect on the coated composite film. The characteristic of forming a particle structure. In other words, the difference between a non-aqueous dispersion and a cross-linked polymer particle is that since the particle has no cross-linking position, the shape of the particle changes during the baking process and can be a resin component.

此外,例如也可使用稱作為NAD(非水性分散液)之樹 脂粒子,述於著色材料第48期(1975年)28-34頁,且用於NAD 塗料。 以樹脂固型物含量重量為基準,中間塗料之非水性分 散液樹脂(d)之含量為4至15%重量比且較佳為5至12%重量 比。當含量小於4%重量比時,經塗覆之複合薄膜之外觀不 足;而當含量超過15%重量比時,耐切晶片效能降低。 200427797 經由使用非水性分散液樹脂(d),可防止各塗層間之溶 混且外觀改善。 片狀顏料(e)包括雲母、鋁氧、滑石及矽氧;由切晶片 效能觀點,以滑石為佳。 5 較佳片狀顏料(e)具有長直徑為1至10微米,以及數目平 均粒子直徑為2至6微米之尺寸。當長直徑係在該範圍以外 時,薄膜外觀低劣,無法獲得足夠耐切晶片效能。而當粒 子直徑於該範圍以外時,同理,經塗覆之複合薄膜之外觀 變差,且無法獲得足夠耐切晶片效能。 10 當塗料之樹脂固型物含量重量為1〇〇份重量比時,片狀 顏料(e)之含量為0·4至2份重量比。以0.5至1.5份重量比為更 佳。當含量於該範圍以外時,因與底塗膜之黏著性降低, 固無法獲得足夠耐切晶片效能。 其它可包含之樹脂並無特殊限制,包括丙烯酸系樹 15 脂、聚酯樹脂、醇酸樹脂、環氧樹脂等。此等樹脂可單獨 使用或組合兩種或兩種以上使用。 著色顏料例如包括以偶氮螯合為主之顏料、不溶性以 偶氮為主之顏料、稠合以偶氮為主之顏料、以酞花青為主 之顏料、以苯嵌萘酮為主之顏料、以二萘羥苯為主之顏料、 20 以二氧己環為主之顏料、以喳吖啶酮為主之顏料、以異吲 口朶啉酮為主之顏料、金屬錯合物顏料等作為有機鹼。至於 無機鹼,可使用鉻黃、黃色氧化鐵、紅色氧化鐵、碳黑、 二氧化鈦等。此外可使用增量劑顏料,包括碳酸#5、硫酸 鋇、鋁粉、高嶺土等。 20 200427797 至於標準品,使用含有碳黑及二氧化鈦之以灰色為主 之著色顏料作為主要顏料。此外,也可使用具有色調與頂 塗層色調可相容之著色顏料,及多種顏料的組合。 此外,為了防止各層與頂塗膜相容混,且維持塗覆工 5 作能力,可添加流變劑至中間塗料。流變劑例如包括通常 具有觸變性質之材料,例如以多胺為主之化學劑例如脂肪 酸醯胺、醯胺脂肪酸、長鏈多胺醯胺磷酸鹽等之溶脹分散 液;以聚乙烯為主之化學劑例如聚環氧乙烷等之膠體溶脹 分散液;以有機皂土為主之化學劑如有機酸綠土、蒙脫土 10 等;無機顏料如矽酸鋁、硫酸鋇等;片狀顏料顯示之黏度 係依據顏料形狀、交聯樹脂粒子等決定。 本發明使用之中間塗料之固型物含量總量於施用時為 30至80%重量比且較佳為35至65%重量比。當含量於此範圍 之外時,塗料穩定度降低。當含量超過上限時,黏度過高, 15 經塗覆之複合薄膜外觀下降。當含量低於下限時,黏度過 低,出現如各層溶混以及不均勻等劣化外觀。 除了該等分外,其它通常添加至塗料之添加劑例如表 面調整劑、抗氧化劑、消泡劑等也可攙混於本發明使用之 中間塗料。攙混量係於熟諳技藝人士已知之範圍。 20 此外,其它樹脂可含於以胺基甲酸酯改性之聚酯樹 脂。此種樹脂並無特殊限制,反而包括丙浠酸系樹脂、聚 酯樹脂、醇酸樹脂、環氧樹脂等。樹脂可單獨使用或組合 兩種或兩種以上使用。 一種製備本發明使用之塗料組成物之方法包括後述方 21 200427797 二二4寸殊限制,熟諳技藝人士眾所周知之方法例如使 用此、、柬機、輥及SG磨機混練且分散顏料纔合物之任一種方 法皆可使用。 底塗膜 5 用於本發明之塗獅成方狀底塗料制來使用透明 ^料^/成頂、塗膜。底塗料含有塗膜形成性樹脂、硬化劑、 著色顏料,以及若有所需含有光澤彩色顏料等。 底塗料所含之成膜樹脂並無特殊限制,其範例包括丙 稀酸系樹脂、聚酉旨樹脂、醇酸樹脂、環氧樹脂、胺基甲酸 10酯樹脂等。此等樹脂可單獨使用或組合兩種或兩種以上使 用。 成膜樹脂可經由與硬化劑組合使用。由多種效能及所 得塗膜成本觀點,較佳使用胺基樹脂及/或嵌段異氰酸酯樹 脂0 15 以成膜樹脂之固型物含量重量為基準,硬化劑含量較 佳為20至60%重量比及更佳為3〇至50%重量比。當含量小於 20%重量比時,硬化能力不足。當含量高於6〇%重量比時, 硬化後之薄膜太硬太脆。 此外,至於著色顏料,例如可含有對中間塗料舉例說 20 明之著色顏料。 底塗料選擇性含有之光澤性彩色顏料的形狀並無特殊 限制。光澤彩色顏料可進一步經著色。例如以具有平均粒 子直徑(ho)為2至50微米,厚度〇」至5微米之光澤彩色顏料 為佳。此外,具有平均粒子直徑為1〇至35微米範圍之光澤 22 200427797 彩色顏料之光澤彩色感覺絕佳,更適合使用。塗料中之光 澤彩色顏料之顏料濃度(PWC)通常為20.0%重量比或以 下。當濃度超過上限時,塗覆膜外觀下降。濃度較佳為0.01 至18.0%重量比,以及更佳為0.1至15.0%重量比。當光澤彩 5 色顏料之含量超過20.0%重量比時,塗膜外觀下降。 光澤彩色顏料例如包括金屬或合金如铭、銅、鋅、鐵、 鎳、錫及氧化鋁及其混合物等金屬或合金之未經著色或經 著色之金屬光澤彩色顏料。此外,干擾雲母顏料、白雲母 顏料、石墨顏料及其它經著色或未經著色之片狀顏料也可 10 結合使用。 塗料中,光澤彩色顏料及全部其它顏料之總顏料濃度 (PWC)為0.1至50%重量比,較佳為0.5至40%重量比,及更 佳為1.0至30%重量比。當濃度超過上限時,塗覆膜之外觀 下降。 15 此外,如同於中間塗料,為了維持塗覆工作性,較佳 添加流變劑至底塗料。流變劑用來形成不含非均勻與凹陷 之塗膜,通常含有具有觸變性質之化學劑。至於此種流變 劑,可含有對中間塗料舉例說明之流變劑。 除了此等成分外,通常添加於塗料之添加劑例如表面 20 調整劑、流變劑、抗氧化劑、紫外光抑制劑及消泡劑等, 也可攙混於本發明使用之底塗料。其攙混量係於熟諸技藝 人士已知之範圍。 本發明使用之底塗料於施用時總固形物含量為10至 60%重量比且較佳為15至50%重量比。當含量高於上限或低 23 200427797 於下限時,塗料穩定性降低。當含量超過上限時,黏度過 高,塗膜外觀下降。當含量低於下限時,黏度過低,出現 各層相溶混以及不均勻等劣化外觀。 透明塗膜 5 為了形成透明塗膜,使用透明塗料。透明塗料並無特 殊限制,反而可使用含有成膜熱固樹脂及硬化劑之透明塗 料。至於透明塗料形式,例如包括溶液型、水性型及粉末 型。 由透明度及對酸蝕刻之耐性而言,溶液型透明塗料較 10 佳例如包括丙烯酸系樹脂及/或聚酯樹脂與胺基樹脂之組 合、丙烯酸系樹脂及/或聚酯樹脂與異氰酸酯化合物之組合 以及丙烯酸系樹脂及/或具有羧酸-環氧基硬化系統之聚酯 樹脂。 此外,水性型透明塗料例如包括含有樹脂之塗料,該 15 塗料係經由使用鹼中和範例水性型透明塗料之成膜樹脂而 獲得,不容易變成水性。中和可於聚合前或聚合後,藉添 加第三級胺如二甲基乙醇胺及三乙基胺進行。 相反地,至於粉末型透明塗料,可使用例如熱塑粉末 塗料及熱固粉末塗料等習知粉末塗料。因含有具較佳物理 20 性質之塗膜,故以熱固粉末塗料為佳。熱固粉末塗料例如 包括以環氧樹脂為主、以丙烯酸系為主及以聚酯樹脂為主 之粉末透明塗料,但以具有較佳耐候性之以丙烯酸系為主 之粉末透明塗料為特佳。 至於本發明使用之粉末型透明塗料,由於硬化時不含 24 200427797 揮發性物質,可獲得較佳外觀且罕見黃化,故以含環氧樹 脂之丙烯酸系樹脂/以多價羧酸為主之粉末塗料為特佳。 此外,如同於中間塗料,為了維持塗覆工作性,較佳 添加流變劑至透明塗料。至於流變劑,通常含有具觸變性 5 質之化學劑。至於流變學作用劑,可含有對中間塗料舉例 說明之流變劑。若有所需,可含有硬化催化劑、表面調整 劑等。 基材 本發明之經塗覆之複合薄膜形成方法較佳用於各種基 10 材,例如金屬、塑膠、發泡材料等。較佳為金屬及成形物 件。該方法特別適合用於可藉陽離子塗覆之金屬產物。 金屬產物例如包括鐵、銅、鋁、錫、鋅等及含有此等 金屬之合金。具體實施例包括汽車、卡車、摩托車、大客 車等之車體及零組件。特佳金屬為以磷酸鹽、鉻酸鹽等預 15 先接受化學處理之金屬。 此外,於用於本發明之經塗覆之複合薄膜形成方法之 基材,電沉積塗膜可形成於經化學處理之鋼板上。至於形 成電沉積塗膜之電沉積塗料,可使用陽離子型或陰離子 型,以陽離子型電沉積塗料組成物為佳,該塗料可獲得絕 20 佳防蝕性之塗膜。 實施例 本發明將於後文實施例說明其細節,但本發明絕非囿限 於該等實施例。後文中「份數」及「百分比」係以重量計。 製備例1 25 200427797 以胺基甲酸酯改性之聚酯樹脂之製備 44〇伤間苯二甲酸,20份六氩鄰苯二甲酸,40份壬二 酸、300份三羥甲基丙烷及200份新戊二醇置於2升反應容器 内,反應容器裝配有氮氣導入管、攪拌器、溫度調節器、 5添加漏斗及裝配有傾析器之冷卻管;當原料藉加熱溶解 時’變成可以攪拌,添加〇·2份二丁基氧化錫,開始攪拌, 反應層溫度由18〇。〇徐缓升高至22〇°C經歷3小時。產生之縮 合水由系統蒸餾去除。當溫度達220°C時,維持該溫度1小 時’徐緩添加20份二甲苯至反應層,允許於溶劑存在下進 10行縮合反應。當樹脂酸價達1〇毫克KOH/克時,材料冷卻至 100C ’以30分鐘時間徐緩添加1〇〇份六亞甲基二異氰酸 醋。此外’溫度維持1小時,添加2〇〇份二甲苯及2〇〇份乙酸 丁醋’獲得以胺基曱酸酯改性之聚酯樹脂,具有固型物含 量70%,平均分子量2000,酸價8毫克KOH/克,羥基值120 15 及樹脂Tg 60°C。 製備例2 非水性分散液之製備 (a)分散液安定樹脂之製備 90份乙酸丁酯置於裝配有攪拌器、溫度控制器及回流 20 冷凝器之容器。然後20份溶液具組成如後: 表1 甲基丙烯酸甲酯 甲基丙烯酸硬脂酯 丙烯酸2_羥基乙酯 偶氮貳異丁腈 38.9 份 38.8 份 22.3 份 5.0份In addition, for example, resin particles called NAD (non-aqueous dispersion) can be used, which is described in Coloring Material Issue 48 (1975), pages 28-34, and is used for NAD coatings. The content of the non-aqueous dispersion liquid resin (d) of the intermediate coating is 4 to 15% by weight and preferably 5 to 12% by weight based on the weight of the resin solid content. When the content is less than 4% by weight, the appearance of the coated composite film is insufficient; while when the content is more than 15% by weight, the cut-resistant wafer performance is reduced. 200427797 By using non-aqueous dispersion resin (d), it is possible to prevent miscibility between coatings and improve appearance. The flake pigment (e) includes mica, alumina, talc and silica; from the viewpoint of chip performance, talc is preferred. 5 The preferred flake pigment (e) has a size having a long diameter of 1 to 10 m and a number average particle diameter of 2 to 6 m. When the long diameter is outside this range, the appearance of the film is poor, and sufficient chip-cutting resistance cannot be obtained. When the particle diameter is out of this range, the appearance of the coated composite film becomes worse by the same way, and sufficient chip-cutting resistance cannot be obtained. 10 When the resin solid content of the coating is 100 parts by weight, the content of the flake pigment (e) is 0.4 to 2 parts by weight. It is more preferably 0.5 to 1.5 parts by weight. When the content is outside the range, the adhesiveness with the base coating film is decreased, and sufficient chip-resistant chip performance cannot be obtained. Other resins that can be included are not particularly limited, including acrylic resins, polyester resins, alkyd resins, and epoxy resins. These resins may be used alone or in combination of two or more. Colored pigments include, for example, azo-chelated pigments, insoluble azo-based pigments, azo-based pigments, phthalocyanine-based pigments, and benzonaphthone-based pigments. Pigments, pigments based on pernaphthol, 20 pigments based on dioxane, pigments based on fluoracridone, pigments based on isoindolinone, metal complex pigments Etc. as organic base. As for the inorganic base, chrome yellow, yellow iron oxide, red iron oxide, carbon black, titanium dioxide, and the like can be used. In addition, extender pigments can be used, including # 5 carbonate, barium sulfate, aluminum powder, kaolin, and the like. 20 200427797 As the standard, a gray-based coloring pigment containing carbon black and titanium dioxide is used as the main pigment. In addition, coloring pigments having a color tone compatible with that of the top coat, and a combination of various pigments can also be used. In addition, in order to prevent the layers from being compatible with the top coating film and maintain the coating work ability, a rheological agent may be added to the intermediate coating. Rheological agents include, for example, materials that generally have thixotropic properties, such as polyamine-based chemical agents such as swelling dispersions of fatty acid amidines, ammonium fatty acids, long-chain polyamine ammonium phosphates, etc .; polyethylene-based Chemical agents such as colloidal swelling dispersions of polyethylene oxide; chemical agents based on organic bentonite such as organic acid smectite, montmorillonite 10, etc .; inorganic pigments such as aluminum silicate, barium sulfate, etc .; flake The viscosity displayed by the pigment is determined based on the shape of the pigment, crosslinked resin particles, and the like. The total solid content of the intermediate coating used in the present invention is 30 to 80% by weight and preferably 35 to 65% by weight when applied. When the content is outside this range, paint stability decreases. When the content exceeds the upper limit, the viscosity is too high, and the appearance of the coated composite film decreases. When the content is lower than the lower limit, the viscosity is too low, and the appearance of deterioration such as miscibility and unevenness of the layers occurs. In addition to these ingredients, other additives commonly added to coatings such as surface conditioners, antioxidants, defoamers, etc. can also be blended into the intermediate coatings used in the present invention. The mixing amount is in a range known to those skilled in the art. 20 In addition, other resins may be contained in urethane-modified polyester resins. This resin is not particularly limited, but includes a propionic acid resin, a polyester resin, an alkyd resin, an epoxy resin, and the like. The resins can be used alone or in combination of two or more. A method for preparing the coating composition used in the present invention includes the following limitation: 21, 2004, 27, 797, 22, 4 inches. The method is well known to those skilled in the art, such as using this, Cambodian machine, roller and SG mill to knead and disperse pigments. Either method can be used. Base coating film 5 is used for the lion-shaped square base coating of the present invention to use a transparent coating material. The primer contains a film-forming resin, a hardener, a coloring pigment, and if necessary, a gloss color pigment. The film-forming resin contained in the primer is not particularly limited, and examples thereof include acrylic resins, polyurethane resins, alkyd resins, epoxy resins, and urethane resins. These resins may be used alone or in combination of two or more. The film-forming resin can be used in combination with a hardener. From the viewpoints of various performances and the cost of the obtained coating film, it is preferred to use an amine-based resin and / or a block isocyanate resin. Based on the solid content and weight of the film-forming resin, the hardener content is preferably 20 to 60% by weight. And more preferably 30 to 50% by weight. When the content is less than 20% by weight, the hardening ability is insufficient. When the content is higher than 60% by weight, the hardened film is too hard and brittle. In addition, as for the coloring pigment, for example, a coloring pigment, which is exemplified by the intermediate paint, may be contained. There is no particular limitation on the shape of the glossy color pigment that the primer selectively contains. Glossy color pigments can be further colored. For example, a glossy color pigment having an average particle diameter (ho) of 2 to 50 m and a thickness of 0 "to 5 m is preferred. In addition, it has a gloss with an average particle diameter in the range of 10 to 35 micrometers. The pigment concentration (PWC) of the gloss color pigments in coatings is usually 20.0% by weight or less. When the concentration exceeds the upper limit, the appearance of the coating film decreases. The concentration is preferably 0.01 to 18.0% by weight, and more preferably 0.1 to 15.0% by weight. When the content of the gloss 5 color pigment exceeds 20.0% by weight, the appearance of the coating film decreases. Gloss color pigments include, for example, uncolored or tinted metallic gloss color pigments of metals or alloys such as metal, copper, zinc, iron, nickel, tin, alumina, and mixtures thereof. In addition, interference mica pigments, muscovite pigments, graphite pigments, and other pigmented flake pigments can also be used in combination. In the coating, the total pigment concentration (PWC) of the gloss color pigment and all other pigments is 0.1 to 50% by weight, preferably 0.5 to 40% by weight, and more preferably 1.0 to 30% by weight. When the concentration exceeds the upper limit, the appearance of the coating film decreases. 15 Also, as with intermediate coatings, to maintain coating workability, it is better to add a rheological agent to the primer. Rheological agents are used to form coatings that are free of inhomogeneities and depressions. They usually contain chemicals with thixotropic properties. As for this rheological agent, the rheological agent exemplified for the intermediate coating may be contained. In addition to these ingredients, additives such as surface modifiers, rheological agents, antioxidants, UV inhibitors, and defoamers that are usually added to coatings can also be blended into the base coatings used in the present invention. Its mixing amount is within the range known to those skilled in the art. The base coating material used in the present invention has a total solids content of 10 to 60% by weight and preferably 15 to 50% by weight when applied. When the content is higher than the upper limit or lower, the stability of the coating is reduced. When the content exceeds the upper limit, the viscosity is too high, and the appearance of the coating film is reduced. When the content is lower than the lower limit, the viscosity is too low, and the appearance of the layers is miscible and uneven. Clear coating film 5 In order to form a clear coating film, a clear paint is used. There are no particular restrictions on clear coatings. Instead, clear coatings containing film-forming thermosetting resins and hardeners can be used. As for the clear coating form, it includes, for example, a solution type, an aqueous type, and a powder type. In terms of transparency and resistance to acid etching, solution-based clear coatings are better than 10, such as including acrylic resins and / or polyester resins and amine resins, acrylic resins and / or polyester resins and isocyanate compounds. And acrylic resins and / or polyester resins having a carboxylic acid-epoxy curing system. In addition, the water-based transparent coating material includes, for example, a resin-containing coating material, which is obtained by neutralizing a film-forming resin of an exemplary water-based transparent coating material with an alkali, and does not easily become water-based. Neutralization can be performed before or after polymerization by adding tertiary amines such as dimethylethanolamine and triethylamine. Conversely, as the powder type clear coating material, conventional powder coating materials such as thermoplastic powder coating materials and thermosetting powder coating materials can be used. Because it contains a coating film with better physical properties, a thermosetting powder coating is preferred. Thermosetting powder coatings include, for example, epoxy transparent powder coatings, acrylic powder coatings, and polyester resin powder coatings, but acrylic powder coatings with better weather resistance are particularly preferred. . As for the powder type transparent coating used in the present invention, since it does not contain 24 200427797 volatile substances when hardened, it can obtain better appearance and rarely yellowing. Therefore, it is mainly based on acrylic resins containing epoxy resins and polyvalent carboxylic acids. Powder coatings are particularly preferred. In addition, as with intermediate coatings, in order to maintain coating workability, it is preferable to add a rheological agent to the clear coating. As for rheological agents, they usually contain thixotropic chemicals. As for the rheological agent, the rheological agent exemplified for the intermediate coating may be contained. If necessary, a hardening catalyst, a surface conditioner, and the like may be contained. Substrate The coated composite film forming method of the present invention is preferably applied to various substrates, such as metal, plastic, and foamed materials. Preferred are metal and shaped articles. This method is particularly suitable for metal products that can be coated by cations. Metal products include, for example, iron, copper, aluminum, tin, zinc, and the like, and alloys containing these metals. Specific embodiments include car bodies and components of automobiles, trucks, motorcycles, buses, and the like. Particularly preferred metals are those that have been chemically treated with phosphate, chromate, etc. in advance. In addition, on the substrate used in the coated composite film forming method of the present invention, an electrodeposition coating film may be formed on a chemically-treated steel sheet. As for the electrodeposition coating for forming an electrodeposition coating film, a cationic or anionic type may be used, and a cationic electrodeposition coating composition is preferable, and the coating can obtain a coating film with excellent corrosion resistance. Examples The present invention will be described in detail in the following examples, but the present invention is by no means limited to these examples. "Parts" and "percentages" in the following are based on weight. Preparation Example 1 25 200427797 Preparation of Polyurethane Resin Modified with Urethane 44. Isophthalic acid, 20 parts of hexaargon phthalic acid, 40 parts of azelaic acid, 300 parts of trimethylolpropane and 200 parts of neopentyl glycol was placed in a 2 liter reaction vessel. The reaction vessel was equipped with a nitrogen introduction tube, a stirrer, a temperature regulator, a 5 addition funnel and a cooling tube equipped with a decanter; when the raw materials were dissolved by heating, it became ' It can be stirred, 0.2 parts of dibutyltin oxide is added, and stirring is started, and the temperature of the reaction layer is changed from 180 °. 〇 Rising slowly to 22 ° C for 3 hours. The resulting condensation water is removed by system distillation. When the temperature reached 220 ° C, maintaining the temperature for 1 hour 'slowly added 20 parts of xylene to the reaction layer, and allowed 10 condensation reactions in the presence of a solvent. When the resin acid value reached 10 mgKOH / g, the material was cooled to 100C 'and 100 parts of hexamethylene diisocyanate was slowly added over a period of 30 minutes. In addition, 'the temperature was maintained for 1 hour, and 200 parts of xylene and 2000 parts of butyric acid acetate were added' to obtain a polyester resin modified with an amino ester, having a solid content of 70%, an average molecular weight of 2000, and an acid. Valence 8 mg KOH / g, hydroxyl value 120 15 and resin Tg 60 ° C. Preparation Example 2 Preparation of Non-Aqueous Dispersion Liquid (a) Preparation of dispersion liquid stabilizer resin 90 parts of butyl acetate was placed in a container equipped with a stirrer, a temperature controller, and a reflux 20 condenser. Then 20 parts of the solution have the following composition: Table 1 Methyl methacrylate Stearyl methacrylate 2-hydroxyethyl acrylate Azo isobutyronitrile 38.9 parts 38.8 parts 22.3 parts 5.0 parts

26 200427797 添加至其中,藉加熱、攪拌升高溫度。85份其餘混合 溶液於ll〇t:逐滴添加3小時,然後以30分鐘時間逐滴添加 0.5份偶氮貳二異丁腈及10份乙酸丁酯溶液。反應溶液又回 流攪拌2小時來提升改變成樹脂之速率,反應完成,獲得丙 5 烯酸系樹脂,具有固型物含量50%,數目平均分子量5600 及SP值9.5。 (b)非水性分散液之製備 90份乙酸丁酯及60份(a)分散液穩定樹脂之製備所得之 丙烯酸系樹脂,置於容器内,容器裝配有攪拌器、冷凝器 10 及控溫器。然後具如下組成之溶液: 表2 苯乙烯 7.0份 甲基丙烯酸 1.8份 甲基丙烯酸甲酯 12.0 份 丙烯酸乙酯 8.5份 丙烯酸2-羥基乙酯 40.7 份 偶氮貳異丁腈 1.4份 於100°C逐滴添加3小時,然後以30分鐘時間逐滴添加 0.1份偶氮貳異丁腈及1份乙酸丁酯溶液。反應溶液持續攪 15 拌1小時,獲得固型物含量60%及粒子直徑180奈米之乳 液。此乳液以乙酸丁酯稀釋,獲得芯-殼型乙酸丁酯分散 液,具有非水性分散液含量40%,黏度300 cps (25°C)及粒 子直徑180奈米。此種非水性分散液樹脂具有Tg 23°C,羥 基值162及SP值11.8 ;殼部為分散液穩定樹脂與本全體非水 27 200427797 性分散液樹脂之SP值差異為2.3。 實施例1 中間塗料 107份先前製備所得之以胺基甲酸酯改性之聚酯樹脂 5清漆,280份CR-97(石原產業公司製造之氧化鈦),13份 MA-100(碳黑顏料,三菱化學公司製造),7份MS-1〇〇(鱗狀 滑石,富士滑石公司製造),47份乙酸丁酯及47份二甲苯置 於1升谷态,放置與進料總量等量之GB503M(粒子直徑1.6 *米之玻璃珠),材料於室溫使用桌上型8(}磨機分散3小時 10獲得灰色顏料糊。分散完成時使用研磨錶測得粒子直徑為5 微米或以下。玻璃珠經過濾獲得顏料糊。顏料糊製備成為 具有表3所示組成之中間塗料。塗料使用4號福特杯,以丙 酸乙氧基乙酯/S-100(芳香族烴溶劑,艾克森公司製造)=";[ 稀釋至19秒/20°C。施用時之非揮發物含量為49〇/〇。 中間塗覆組成 顏料糊 100份 聚酯樹脂 130份 非水性分散液 53份 I胺,脂(「優邦128(商品名)」三井赛鐵克 (Cyteck)公司製造 71份 商品名」} 71份 樹脂固型物比 g雙樹脂/非水性分散液/蜜胺樹脂/嵌段異氰 酸酯 50/10/20/20 顏料比 氧化鈦/碳黑/滑石 28/1.3/0.7 PWC 30% 28 200427797 底塗料 以丙晞酿基蜜胺為主之金屬底顏料「歐加(〇rga) τ〇 Η600卿金屬」(日本塗料公司製造)使㈣福特杯以 丙酸乙氧基乙麟·_(芳香族烴溶劑,艾克森公司製造)之 混合溶劑稀釋至Π秒/2(TC。塗料施用時之非揮發物含量為 31%。沉積時之非揮發物含量為65%。 透明塗料 10 15 20 以酉夂性ί衣乳樹脂硬化為主之透明塗料「馬克⑽峨) j〇〇透明」(日本塗料公司製造)使用4號福特杯以丙酸 乙氧基乙醋/S-U)0(芳香族烴溶劑,艾克森公司製造)稀釋成 26^2〇t。塗料施用時之非揮發物含量為·。此外,沉 積日寸之非揮發物含量為61 %。 經塗覆之複合薄膜形成方法 、陽離子性電沉積塗料「包爾托普(p〇werT叩)v_2〇」(曰 ,^料A司製造)電沉積塗覆於spc鋼板上,鋼板厚〇·8毫 米、長30厘米,寬1〇厘米,已經使用磷酸辞處理,經電沉 積主设㈣成塗膜,具有乾膜厚度2G微米,接著於160。(:烤 乾30刀知。然後其上已經形成電沉積塗膜之鋼板附著於移 一藉「微貝機」(旋轉霧化型靜電塗覆機)於移動中塗 、中間塗料,來形成乾膜厚度20微米之塗膜。放置1〇分 鐘任其硬化。26 200427797 was added to it, and the temperature was raised by heating and stirring. 85 parts of the remaining mixed solution was added at 10 t: dropwise for 3 hours, and then 0.5 part of azobisisobutyronitrile and 10 parts of butyl acetate solution were added dropwise over a period of 30 minutes. The reaction solution was stirred under reflux for 2 hours to increase the rate of change to resin. After the reaction was completed, an acrylic resin was obtained with a solid content of 50%, a number average molecular weight of 5600, and an SP value of 9.5. (b) Preparation of non-aqueous dispersion liquid 90 parts of butyl acetate and 60 parts (a) Preparation of dispersion resin stabilized acrylic resin obtained in a container, the container is equipped with a stirrer, a condenser 10 and a temperature controller . Then it has a solution with the following composition: Table 2 Styrene 7.0 parts methacrylic acid 1.8 parts methyl methacrylate 12.0 parts ethyl acrylate 8.5 parts 2-hydroxyethyl acrylate 40.7 parts azoisobutyronitrile 1.4 parts at 100 ° C The solution was added dropwise for 3 hours, and then 0.1 part of azobisisobutyronitrile and 1 part of butyl acetate solution were added dropwise over a period of 30 minutes. The reaction solution was continuously stirred for 15 hours and stirred for 1 hour to obtain an emulsion with a solid content of 60% and a particle diameter of 180 nm. This emulsion was diluted with butyl acetate to obtain a core-shell type butyl acetate dispersion with a non-aqueous dispersion content of 40%, a viscosity of 300 cps (25 ° C), and a particle diameter of 180 nm. This non-aqueous dispersion resin has a Tg of 23 ° C, a hydroxyl value of 162, and an SP value of 11.8; the difference between the SP value of the dispersion-stabilized resin in the shell portion and the non-aqueous 27 200427797 dispersion resin is 2.3. Example 1 107 parts of an intermediate coating, a urethane-modified polyester resin 5 varnish, 280 parts of CR-97 (titanium oxide manufactured by Ishihara Industries), 13 parts of MA-100 (carbon black pigment) , Manufactured by Mitsubishi Chemical Corporation), 7 parts of MS-100 (scaly talc, manufactured by Fuji Talc), 47 parts of butyl acetate and 47 parts of xylene are placed in a 1 liter valley state, and the amount is equal to the total amount of feed GB503M (glass beads with a particle diameter of 1.6 * m), the material was dispersed at room temperature using a table type 8 (} mill for 3 hours and 10 hours to obtain a gray pigment paste. When the dispersion was completed, the particle diameter was measured using a grinding table to be 5 microns or less. The glass beads were filtered to obtain a pigment paste. The pigment paste was prepared as an intermediate coating having the composition shown in Table 3. The coating used a No. 4 Ford Cup with ethoxyethyl propionate / S-100 (aromatic hydrocarbon solvent, Exxon). (Manufactured by the company) = [Diluted to 19 seconds / 20 ° C. The non-volatile content at the time of application is 49/0. The intermediate coating composition pigment paste 100 parts polyester resin 130 parts non-aqueous dispersion 53 parts I Amine, fat ("Ubibond 128 (trade name)" made by Mitsui Cyteck Co., Ltd. 71 copies Product name "} 71 parts resin solids ratio g double resin / non-aqueous dispersion / melamine resin / block isocyanate 50/10/20/20 pigment ratio titanium oxide / carbon black / talc 28 / 1.3 / 0.7 PWC 30 % 28 200427797 The base paint is a metallic base pigment "Orga τ〇 600 600 Metal" (made by Japan Coatings Co., Ltd.) based on melamine melamine. _ (Aromatic hydrocarbon solvent, manufactured by Exxon Corporation) The mixed solvent is diluted to Πsec / 2 (TC. The non-volatile content at the time of coating application is 31%. The non-volatile content at the time of deposition is 65%. Clear coating 10 15 20 Transparent paint "Mark Saga" j〇〇 (made by Japan Coatings Co., Ltd.), which is mainly based on hardened milky resin, uses No. 4 Ford Cup with ethoxyethyl propionate / SU) 0 (Aromatic hydrocarbon solvent, manufactured by Exxon Corporation) Diluted to 26 ^ 20t. The non-volatile content at the time of coating application was · In addition, the non-volatile content of the deposited day was 61%. The coated composite Method for forming thin film, cationic electrodeposition coating "PowwerT 叩" v_2〇 " ) Electrodeposition coated on the steel plate of SPC, the thickness of the steel plate is 0.8mm, the length is 30cm, the width is 10cm, and it has been treated with phosphoric acid. At 160. (: Bake dry 30 knives. Then the steel plate on which the electrodeposition coating film has been formed is attached to the mobile coating and intermediate coating by the "micro shell machine" (rotary atomizing electrostatic coating machine). A coating film with a dry film thickness of 20 microns was formed. Leave it for 10 minutes to allow it to harden.

&脅然後底塗料分成二階段使用「微貝機」及「美它貝機」 f覆,然後乾膜厚15微米。兩次施用間間隔2·5分鐘。第2 知用後固化8分鐘。然後使用「微貝機」以丨階段塗覆透 29 200427797 明塗料乾膜尽度3 5微米,進行1 〇分鐘硬化。所層合經塗 覆之複合薄膜之硬化條件為硬化溫度14〇。〇,硬化時間30分 鐘。 如此製備得之塗覆板置於4〇cc第一乾燥烘箱内,維持5 5分鐘,移至設定於140°C之第二乾燥烘箱且維持20分鐘。隨 後由乾燥烘箱去除塗覆板,讓其冷卻至室溫。 (1)目測評比硬化後之經塗覆之複合薄膜外觀是否存在 有光澤。測試結果顯示於表5。 表4 評比標準 3 光澤外觀優異,似乎透明塗料施用厚度足夠 2 光澤外觀略差,似乎透明塗料厚度小 光澤外觀低劣,似乎未塗覆透明塗料 ⑺然後使用巨大化學公司(Big Chemie)製造之經塗覆 之複合薄膜外觀測量裝置「波掃描D〇I (Wave Scan D0I)」, 測試硬化後之經塗覆之複合薄膜表面狀態。結果顯示於表 15 5 ° /貝J里值Wa表不表面串珠之粗度量為至毫米,表 塗覆之複合㈣之光澤外觀。—表示表面串珠粗度量i 至3毫米,表示經塗覆之複合薄膜之表面遮蓋性質。Wd表 7F红土设之複口薄膜之表面串珠粗度3至1^毫米,代表經塗 20覆之複合薄膜光滑。隨著數值的變小,測量值變佳。 (3)此外,所传塗覆板之耐切晶片性質評比如後。試驗 結果顯示於下表5。 30 2〇0^119 伏用葛拉貝羅(glabero)測試器(蘇加(Su㈣測試儀器公 男製造),3〇〇塊7號碎石由35厘米距離,以空氣壓力3〇千克 力/个方厘米以45度角度碰撞薄膜。以水洗滌及乾燥後,使 用尼奇邦(Nichiban)公司製造之工業用黏膠帶進行剝離試 · 5 驗,隨後就玻璃直徑及玻璃數視覺觀察及評比剝離程度。 實施例2至4 根據實施例1所述方法之相同方式,但硬化溫度及硬化 時間改變成如表5所示。製備經硬化之經塗覆之複合薄膜且 測試。測試結果顯示於表5。 · 10 比較例1 根據實施例1所述方法之相同方式,但於140°C以一階 段式加熱30分鐘,進行未硬化之經塗覆之複合薄膜之烤乾 與硬化步驟,製備硬化後之經塗覆之複合薄膜及測試。試 驗結果顯示於表6。 15 比較例2 根據實施例1所述方法之相同方式,但使用日本塗料公 司製造之以聚酯-蜜胺為主之中間塗料「歐加το H870灰」 · 作為中間塗料,硬化溫度及硬化時間改變成如表6所示。製 備經硬化之經塗覆之複合薄膜且測試。測試結果顯示於表 、 20 6。 參考例1 陽離子性電沉積塗料「包爾托普V-20」(日本塗料公司 製造)電沉積塗覆於SPC鋼板上,鋼板厚〇·8毫米,長30厘 米,寬10厘米,已經使用磷酸鋅處理,經電沉積塗覆而形 31 成塗膜,形成乾膜具有厚度2〇微米,接著於丨⑼^烤乾3〇分 1里。然後其上已經形成電沉積塗膜之鋼板附著於移動本 體,藉「微貝機」(旋轉霧化型靜電塗覆機)於移動中塗覆以 中間塗料,來形成乾膜具有厚度2〇微米之塗膜,施用後, 放置10分鐘任其硬化。 此塗覆板置於設定於140°c之乾燥烘箱位置20分鐘。隨 後塗覆板由乾燥烘箱取出’讓其冷卻至室溫。底塗料及透 明塗料如實施例丨施用於塗覆板上獲得經塗覆之複合薄膜。 如此製備後之塗覆板置於14代乾燥烘箱,維持3〇分 鐘。隨後域舰箱錄塗覆板,料冷卻至室溫。根據 貫施例丨所述方法之姻方式,㈣所得硬化後之經塗覆之 複合薄膜。測試結果顯示於表6。 參考例2 根據參考例1所述方法之相同方式,但使用日本塗料公 司製造之以聚_ -蜜胺為主之中間塗料「歐加TO Η870灰」 作為中間塗料,硬化溫度及硬化時間改變成如表6所示。製 備經硬化之«覆之複合薄膜且,。職結果顯示於表 200427797 表5 實施例編號 1 2 3 4 中間經塗覆 之複合薄膜 種類 實施例1 實施例1 實施例1 實施例1 烤乾 - - - - 經塗覆之複 合薄膜烤乾 低溫 40°Cx 5分鐘 60°Cx 3分鐘 60°Cx 5分鐘 100°Cx 5分鐘 南溫 140°Cx 30分鐘 140°Cx 30分鐘 140°Cx 30分鐘 140°Cx 30分鐘 外觀(視覺評比) 3 3 3 3 表面狀態 Wa 16.3 14.7 13.6 16.6 Wc 13.4 14.4 12.2 16.2 Wd 8.7 8.2 7.3 10.3 财切晶片 剝離 直徑 2毫米 1.8毫米 1.7毫米 2毫米 數目 20 18 16 19& Then the primer is divided into two stages using a "micro shell machine" and "meta shell machine" f, and then the dry film thickness is 15 microns. The interval between the two applications was 2.5 minutes. 2nd curing after 8 minutes. Then use a "micro-shell machine" to coat the coating in stages 29 200427797. The dry film of the clear coating is as fine as 35 microns and hardened for 10 minutes. The curing condition of the laminated composite film was a curing temperature of 14 °. 〇, the hardening time is 30 minutes. The coated plate thus prepared was placed in a 40 cc first drying oven, maintained for 55 minutes, and moved to a second drying oven set at 140 ° C., and maintained for 20 minutes. The coated plate was then removed from the drying oven and allowed to cool to room temperature. (1) Visually evaluate whether the coated composite film after the hardening has a glossy appearance. The test results are shown in Table 5. Table 4 Evaluation criteria 3 Excellent gloss appearance, it seems that the thickness of the transparent coating is sufficient 2 The gloss appearance is slightly worse, it seems that the thickness of the transparent coating is small, the gloss appearance is inferior, it seems that the clear coating is not applied, and then a coated coating made by Big Chemie The coated composite film appearance measuring device "Wave Scan D0I" tests the surface state of the coated composite film after hardening. The results are shown in Table 15. The value of 5 ° / Beijing Wa indicates that the rough measure of the surface beading is up to millimeters, and the gloss appearance of the coated composite concrete is shown. — Represents the rough measurement of the surface bead i to 3 mm, and represents the surface hiding property of the coated composite film. Wd Table 7F The thickness of the beaded surface of the compound film set on laterite is 3 to 1 mm, which indicates that the composite film coated with 20 is smooth. As the value becomes smaller, the measured value becomes better. (3) In addition, the properties of the cut-resistant wafers of the coated board were evaluated. The test results are shown in Table 5 below. 30 2 0 0 ^ 119 volts with a glabero tester (manufactured by Su㈣ Testing Instruments), 3,000 pieces of 7 crushed stones are at a distance of 35 cm, and the air pressure is 30 kgf / piece The square centimeter collided with the film at an angle of 45 degrees. After washing with water and drying, the peeling test was performed using an industrial adhesive tape manufactured by Nichiban. After that, the glass diameter and number of glasses were visually observed and evaluated for peeling. Examples 2 to 4 According to the same method as described in Example 1, but the curing temperature and curing time were changed as shown in Table 5. The cured coated composite film was prepared and tested. The test results are shown in Table 5 · 10 Comparative Example 1 According to the same method as in Example 1, but heating at 140 ° C in one step for 30 minutes, the baking and curing steps of the uncured coated composite film were performed. The coated composite film and test. The test results are shown in Table 6. 15 Comparative Example 2 The same method as described in Example 1 was used, but using a polyester-melamine based intermediate coating manufactured by Japan Coatings Co., Ltd. "Oga "H870 gray" · As an intermediate coating, the hardening temperature and hardening time were changed as shown in Table 6. The hardened coated composite film was prepared and tested. The test results are shown in Table and 20 6. Reference Example 1 Cationic electrodeposition Coating "Baltorp V-20" (manufactured by Japan Coatings Co., Ltd.) is electrodeposited and coated on SPC steel plate. The steel plate is 0.8 mm thick, 30 cm long and 10 cm wide. Overlay 31 to form a coating film, forming a dry film with a thickness of 20 microns, and then baking and drying for 30 minutes 1 mile. Then the steel plate on which the electrodeposition coating film has been formed is attached to the moving body, and the "micro shell" Machine (rotary atomizing electrostatic coating machine) is applied with intermediate coating on the move to form a dry film with a thickness of 20 microns. After application, it is left to harden for 10 minutes. This coated plate is placed in the setting The drying oven was placed at 140 ° C for 20 minutes. Then the coated plate was taken out of the drying oven and allowed to cool to room temperature. The primer and transparent coating were applied to the coated plate as in Example 丨 to obtain a coated composite film. After this preparation The cover plate was placed in a 14th generation drying oven and maintained for 30 minutes. Then the coated plate was recorded and cooled to room temperature. According to the marriage method of the method described in Example 丨, the obtained hardened coated The composite film. The test results are shown in Table 6. Reference Example 2 The same method as described in Reference Example 1 was used, but the poly-melamine-based intermediate coating "Omega TO Η 870 Gray" manufactured by Japan Coatings Co. was used as The intermediate coating, curing temperature and curing time were changed as shown in Table 6. The cured composite film was prepared. The results are shown in Table 200427797 Table 5 Example No. 1 2 3 4 Intermediate coated composite film Kind Example 1 Example 1 Example 1 Example 1 Bake dry----Coated composite film Bake dry low temperature 40 ° Cx 5 minutes 60 ° Cx 3 minutes 60 ° Cx 5 minutes 100 ° Cx 5 minutes South temperature 140 ° Cx 30 minutes 140 ° Cx 30 minutes 140 ° Cx 30 minutes 140 ° Cx 30 minutes Appearance (visual evaluation) 3 3 3 3 Surface state Wa 16.3 14.7 13.6 16.6 Wc 13.4 14.4 12.2 16.2 Wd 8.7 8.2 7.3 10.3 Financial chip wafer peeling Diameter 2 mm 1.8 mm 1.7mm 2mm number 20 18 16 19

表6 實施例編號 比較例1 比較例2 參考例1 參考例2 中間經塗覆 之複合薄膜 種類 實施例1 Orga TO 實施例1 Orga TO 烤乾 - - 140°Cx 30分鐘 140°Cx 0分鐘 經塗覆之複 合薄膜烤乾 低溫 - 60°Cx 5分鐘 - - 南溫 140°Cx 30分鐘 140°Cx 30分鐘 140°Cx 30分鐘 140°Cx 30分鐘 外觀(視覺評比) 2 1 3 3 表面狀態 Wa 23.1 45.3 13.1 12.9 Wb 21.0 61.4 11.5 11.4 Wc 18.5 35.6 8.4 9.1 财切晶片 剝離 直徑 2毫米 3.5毫米 2.0毫米 2.5毫米 數目 20 106 16 30Table 6 Example No. Comparative Example 1 Comparative Example 2 Reference Example 1 Reference Example 2 Types of Composite Films Coated in the Middle Example 1 Orga TO Example 1 Orga TO Bake--140 ° Cx 30 minutes 140 ° Cx 0 minutes The coated composite film is baked at low temperature-60 ° Cx 5 minutes--South temperature 140 ° Cx 30 minutes 140 ° Cx 30 minutes 140 ° Cx 30 minutes 140 ° Cx 30 minutes Appearance (visual evaluation) 2 1 3 3 Surface state Wa 23.1 45.3 13.1 12.9 Wb 21.0 61.4 11.5 11.4 Wc 18.5 35.6 8.4 9.1 Financial cut wafer peel diameter 2 mm 3.5 mm 2.0 mm 2.5 mm Number 20 106 16 30

33 200427797 本發明之實施例中,即使經塗覆之複合薄膜係藉三塗 膜一次烤乾方法形成,仍然可獲得三塗膜兩次烤乾方法所 得之同等光澤外觀。此外,本發明進行塗覆系統具有耐切 晶片性等於藉三塗膜兩次烤乾方法所得之經塗覆之複合薄 5 膜之财切晶片性質,但烤乾次數減少。 L圖式簡單說明】 (無) 【圖式之主要元件代表符號表】 (無)33 200427797 In the embodiment of the present invention, even if the coated composite film is formed by the three-coat film baking method, the same gloss appearance obtained by the three-coat film baking method can be obtained. In addition, the coating system of the present invention has the property of cut-resistant wafers equal to the properties of the coated composite thin film obtained by the three-coating and double-baking method, but the number of baking-drying is reduced. Brief description of L scheme] (none) [Representative symbol table of main elements of diagram] (none)

3434

Claims (1)

200427797 拾、申請專利範圍: 1. 一種製造一經塗覆之複合薄膜之方法,包含形成一電塗 覆薄膜於一基材上,以及然後以濕於濕方式連續施用一 種中間塗料、一種底塗料以及一種透明塗料,接著一次 5 烤乾與硬化所施用之三層,其中 該烤乾與硬化包括一低溫加熱階段,係於硬化溫度 之25%至80%溫度加熱經歷硬化時間之5%至30%時間; 以及一高溫加熱階段,其係於超過硬化溫度80%但不高 於120%之溫度加熱經歷硬化時間30%至130%之時間。 10 2.如申請專利範圍第1項之方法,其中 該中間塗料包含: (a) 40至56%重量比之以胺基甲酸酯改性之聚酯樹 脂,具有數目平均分子量1500至3000,係經由脂肪族異 氰酸酯化合物與具有玻璃轉換溫度(Tg)為40°C至80°C 15 之含羥基之聚酯樹脂反應獲得,該聚酯樹脂係經由含 80%或以上間苯二甲酸之酸性成分與多羥基醇縮聚合 獲得; (b) 10至30%重量比之蜜胺樹脂; (c) 15至30%重量比之嵌段異氰酸酯化合物; 20 (d) 4至15%重量比之具有芯-殼結構之非水性分散 液樹脂,(a)至(d)之含量係以樹脂固型物含量之重量為 基準;以及 (e) 0·4至2份重量比之片狀顏料,係以100份重量比 樹脂固型物含量為基準。 35 200427797 3. 如申請專利範圍第2項之方法,其中該嵌段異氰酸酯化 合物係以具有活性亞甲基之化合物嵌段。 4. 一種經塗覆之複合薄膜,其係經由如申請專利範圍第1 至3項中任一項之方法形成。200427797 Patent application scope: 1. A method for manufacturing a coated composite film, comprising forming an electro-coated film on a substrate, and then continuously applying an intermediate coating, a primer and a wet and wet method, and A clear coating, followed by three layers of 5 baking and hardening at a time, wherein the baking and hardening includes a low-temperature heating stage at 25% to 80% of the hardening temperature and heating of 5% to 30% of the hardening time Time; and a high-temperature heating stage, which is a time between 30% and 130% of the hardening time when the heating exceeds 80% but not more than 120% of the hardening temperature. 10 2. The method of claim 1, wherein the intermediate coating comprises: (a) 40 to 56% by weight of a urethane-modified polyester resin having a number average molecular weight of 1500 to 3000, It is obtained by reacting an aliphatic isocyanate compound with a hydroxyl-containing polyester resin having a glass transition temperature (Tg) of 40 ° C to 80 ° C 15. The polyester resin is obtained by using an acid having 80% or more isophthalic acid. Ingredients and polyhydric alcohols are obtained by condensation polymerization; (b) 10 to 30% by weight of melamine resin; (c) 15 to 30% by weight of block isocyanate compounds; 20 (d) 4 to 15% by weight of having Core-shell structured non-aqueous dispersion liquid resin, the content of (a) to (d) is based on the weight of the solid content of the resin; Based on 100 parts by weight of resin solid content. 35 200427797 3. The method according to item 2 of the patent application, wherein the block isocyanate compound is a compound block having an active methylene group. 4. A coated composite film formed by a method such as any one of claims 1 to 3 of the scope of patent application. 36 200427797 柒、指定代表圖: (一) 本案指定代表圖為:第( )圖。(無) (二) 本代表圖之元件代表符號簡單說明: 捌、本案若有化學式時,請揭示最能顯示發明特徵的化學式:36 200427797 (1) Designated representative map: (1) The designated representative map in this case is: (). (None) (II) Brief description of the element representative symbols of this representative diagram: 捌 If there is a chemical formula in this case, please disclose the chemical formula that can best show the characteristics of the invention:
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