TW200427795A - Method for coated composite film - Google Patents
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- TW200427795A TW200427795A TW93107129A TW93107129A TW200427795A TW 200427795 A TW200427795 A TW 200427795A TW 93107129 A TW93107129 A TW 93107129A TW 93107129 A TW93107129 A TW 93107129A TW 200427795 A TW200427795 A TW 200427795A
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
- C08L23/16—Elastomeric ethene-propene or ethene-propene-diene copolymers, e.g. EPR and EPDM rubbers
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D7/00—Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials
- B05D7/14—Processes, 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
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D7/00—Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials
- B05D7/50—Multilayers
- B05D7/56—Three layers or more
- B05D7/57—Three layers or more the last layer being a clear coat
- B05D7/572—Three layers or more the last layer being a clear coat all layers being cured or baked together
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L75/00—Compositions of polyureas or polyurethanes; Compositions of derivatives of such polymers
- C08L75/04—Polyurethanes
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- Chemical Kinetics & Catalysis (AREA)
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- Application Of Or Painting With Fluid Materials (AREA)
- Paints Or Removers (AREA)
Abstract
Description
200427795 玖、發明說明: t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。 L先前技術3 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-A No. 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。但三塗膜一次烤乾方法具有例如下列各項問題。 某些情況下藉由所謂之切晶片而發生塗覆膜之剝離, 當行進中的車輛撞到鵝卵石,而鵝卵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 料個別烤乾方法、及二塗膜一次烤乾方法,底塗膜及中間 5 200427795 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 堂膜党度及底塗膜亮度,形成尚未見脫落之中間塗膜來 達成。 5 例如 Jp-A Ν〇·2002·249699及JP-A No.9-208882描述一 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 10 度不足以用於三塗膜一次烤乾方法。 此外,汽車車體有許多凹凸部分,當車體全部表面係 藉三塗膜一次烤乾方法塗覆時有容易造成外觀劣化之問 題,依據各部分而定出現各層的爆開與溶混。 【明内3 15 發明概要 本發明可解決前述習知問題,本發明之目的係提供一 種由二塗膜'一次烤乾方法形成耐切晶片性質絕佳之經塗 覆之複合薄膜之方法。 本發明提供一種該中間塗料,以樹脂固型物含量為基 20 準,含有 (a) 5至30%重量比之以胺基甲酸酯改性之聚酯樹脂 ,其具有數目平均分子量1,500至3,000,其係經由脂肪族異 氰酸酯化合物與具有玻璃轉換點(Tg)為40°C至80°C之含羥 基之聚酯樹脂反應獲得,該聚酯係經由含8〇莫耳%或以上 6 200427795 之間苯二甲酸與多羥基醇縮聚合獲得, (b) 30至60%重量比之具有酸基及/或羥基之聚烯烴 彈性體,以及 10至30%重量比之嵌段異氰酸酯化合物。 5 【實施方式】 較佳實施例之詳細說明 中間塗膜 於本發明之塗膜形成方法,用以形成中間塗膜之中間 塗料含有以胺基甲酸酯改性之聚酯樹脂(a),聚烯烴彈性體 10 (b)及嵌段異氰酸酯化合物(c)。若有所需,中間塗料可進一 步含有蜜胺樹脂(d)、具有芯-殼結構之非水性分散液樹脂(e) 及片狀顏料(f)。 經胺基曱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。 15 通常,聚酯樹脂可經由酸成分如羧酸、酸酐及酸氣與 一羥基醇或多羥基醇縮聚合而製備。本發明使用之含羥基 聚酯樹脂含有以酸成分之總莫耳數為基準,80莫耳%或以 上之間苯二曱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 20 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曱酸、磷苯 二甲酐、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 磷苯二甲酐、希蜜酸(himic acid)酐、偏苯三酸、偏苯三酐 7 200427795 、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 、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 5 價叛酸及多價緩酸酐以外之酸。此種酸例如包括一魏酸及 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。 多羥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、1,3-10 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 - ϊ哀己二酵、2,2 -二甲基-3 -技基丙基-2,2 -二甲基-3 -經基 丙酸酯、2,2,2-三曱基-1,3-戊二醇、多四亞甲基醚二醇、多 己内酯多元醇、甘油、山梨糖醇、安尼糖醇(annitol)、三羥 甲基乙烷、三羥甲基丙烷、三羥甲基丁烷、己三醇、季戊 15 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 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。内自旨類經由開環加成 20 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、T -戊内S旨、ε-己内S旨、己内S旨、辛内醋、巴豆内醋、 5 -戊内酯、ά -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 8 200427795 造)己内酯類。 含羥基之聚酯樹脂具有玻璃轉換溫度(Tg)為4(rc至85 1且較佳為45°C至75X:。當玻璃轉換溫度(Tg)低於4〇。〇時 ,薄膜硬度減低。當Tg高於80°C時,耐切晶片效能減低。 5 脂肪族異氰酸S旨化合物例如包括六亞甲基二異氰酸西旨 、三甲基六亞曱基二異氰酸酯、環己烷-丨,‘二異氰酸酯、 一環己基甲烧-4,4-二異氰酸酯、甲基環己院二異氰酸酯及 異佛爾S同二異氰酸g旨。 特別由經塗覆之複合薄膜之耐切晶片效能及耐候性觀 10點,較佳使用六亞甲基二異氰酸酯或三甲基六亞甲基二異 氰酸酯。可使用雙縮脲、異氰尿酸酯及其加合物。 含經基聚自旨樹脂與脂肪族異氰酸g旨化合物之反應可經 由熟諳技藝人士已知方法進行。 經胺基曱酸酯改性之聚酯樹脂(a)具有數目平均分子量 15 (Mn)為150〇至3000且較佳為1700至2500。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 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。 20 經胺基甲酸酯改性之聚酯樹脂(a)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 之複合薄膜之防水性降低。當經基值小於3〇時,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K〇H/克。當酸價超過 9 200427795 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。 含於中間塗料之經胺基甲酸酯改性之聚酯樹脂(a)含量 5 ,以樹脂之固型物含量為基準,含量為5至30%重量比且較 佳10至30%重量比。當含量小於5%重量比時,耐切晶片效 能變不足。當含量超過30%重量比時,經塗覆之複合薄膜 硬度降低。 考慮經由含括以胺基甲酸酯改性之聚酯樹脂作為中間 10 塗料成分,經塗覆之複合薄膜之彈性改良,經塗覆之耐切 晶片性質也改良。 聚烯烴彈性體(b)通常為以聚烯烴為主之接枝聚合物。 聚烯烴彈性體(b)例如係經由以聚烯烴為主之巨單體與烯屬 不飽和化合物共聚合而製備。 15 以聚烯烴為主之巨單體表示於聚烯烴鏈以及於末端有 一個烯屬不飽和基團之高分子單體。以聚烯烴為主之巨單 體例如係經由具有羥基之聚烯烴與具有烯屬不飽和基團之 酸或酸酐反應獲得。 具有羥基之聚烯烴例如包括以聚烯烴為主之樹脂如聚 20 乙烯、聚丙烯、聚丁烯、氫化聚丁二烯、聚異戊間二烯、 氫化聚異戊間二烯、EPDM等,其餘兩端皆有羥基。較佳具 有數目平均分子量為200至5000,及更佳500至4000。 市售具有羥基之聚烯烴例如包括下列: 10 200427795 [表i] 商品名 製造商 化合物 Μη G-1000 曰本曹打公司 α,ω-聚丁二稀二醇 約 15,00 G-2000 曰本曹打公司 α,ω-聚丁二嫦二醇 約 2,000 G-3000 日本曹打公司 α,ω-聚丁二稀二醇 約 29,00 G-1000 曰本曹打公司 α,ω-氫化聚丁二稀二醇 約 15,00 G-2000 日本曹打公司 α,ω-氫化聚丁二烯二醇 約 21,00 G-3000 日本曹打公司 α,ω-氫化聚丁二婦二醇 約 3,000 R-15HT 出水石化公司 α聚丁二稀二醇 約 1,200 R-45HT 出水石化公司 α,ω-聚丁二稀二醇 約 2,800 LIR-506 庫拉雷(Kuraray)公司 聚異戊間二烯五醇 約 25,000 具有稀屬不飽和基團之酸酐例如包括順丁稀二酐、衣 康酐、丁二酐等。其中以使用順丁烯二酐為特佳。 5 具有羥基之聚烯烴與具有烯屬不飽和基團之酸或酸酐 之反應可經由熟諳技藝人士已知方法進行。 以聚烯烴為主之巨單體可經由具有羥基之聚烯烴、二 異氰酸酯化合物及具有烯屬不飽和基團之醇反應獲得。具 有烯屬不飽和基團之醇例如包括含羥基之丙烯酸系單體。 10 至於二異氰酸酯化合物,可使用用於製備以胺基甲酸 酯改性之聚酯樹脂之脂肪族二異氰酸酯。特佳為異佛爾酮 二異氰酸醋。 至於含羥基之丙烯酸系單體,例如可使用甲基丙烯酸 羥基乙酯(HEMA)、丙烯酸羥基乙酯(HEA)、甲基丙烯酸羥 15 基丙酯(HPMA)、丙烯酸羥基丙酯(ΗΡΑ)及丙烯酸羥基丁酯 (ΗΒΑ)。此等單體可單獨使用或經由混合兩種或兩種以上使 用。此等含羥基之丙烯酸系單體中,以使用(甲基)丙烯酸羥 基乙醋為特佳。 含羥基之聚烯烴、二異氰酸酯化合物、與具有烯屬不 11 200427795 飽和基團之醇之反應可經由熟諳技藝人士已知方法進行。 欲與以聚烯烴為主之巨單體共聚合之烯屬不飽和化合 物包括烯屬不飽和單體、不飽和丙烯酸系樹脂、不飽和聚 酯樹脂等。 5 烯屬不飽和單體例如包括丙烯酸系單體如丙稀酸甲g旨 、甲基丙烯酸甲酯、丙烯酸、甲基丙烯酸、丙烯酸羥基乙 酯、甲基丙稀酸經基乙酯、丙烯酸正丁酯及甲基丙烯酸正 丁酯等。此等丙烯酸系單體可單獨或混合兩種或兩種以上 使用。此外可使用其它可與丙烯酸系單體共聚合之單體, 10 如苯乙烯及乙酸乙烯酯。 不飽和丙烯酸系樹脂為不飽和鍵結被導入丙稀酸系樹 脂。例如不飽和丙烯酸系樹脂可經由加成曱基丙烯酸縮水 甘油酯至丙烯酸系樹脂之羧基獲得;經由加成具有不飽和 鍵之酸酐至丙烯酸系樹脂之羥基獲得;或經由加成具有不 15飽和鍵之羧酸至丙烯酸系樹脂之環氧乙烷基獲得。 至於不飽和丙烯酸系樹脂,較佳具有酸價〇至2〇〇毫克 KOH/克,及更佳0至150毫克KOH/克,Μ基值10至300且更 佳10至200,數目平均分子量1〇〇〇至50000且更佳為2〇〇〇至 5000,以及碘價為0.5至100及更佳為〇.5至70。 20 不飽和聚酯樹脂可經由習知方法例如多元醇化合物與 具有不飽和基團之多元酸化合物反應獲得。 於不飽和聚酯樹脂,較佳具有酸價〇至2〇〇毫克ΚΟΗ/ 克,及更佳0至150毫克ΚΟΗ/克,羥基值1〇至3〇〇且更佳1〇 至200,數目平均分子量1〇〇〇至5〇〇〇且更佳為1〇〇〇至4〇〇〇, 12 以及碘價為0.5至100及更佳為Ο 5至7〇。 以聚烯烴為主之巨單體與烯屬不飽和化合物之共聚合 可、,二由热,曰技藝人士已知方法進行。例如根據溶液聚合法 以承烯烴為主之巨單體溶解於適當溶劑,升高溫度,隨 後烯屬不飽和化合物與適當聚合引發劑逐滴添加至其中且 同時攪拌。 反應使用之適當溶劑例如包括脂肪族烴類如煤油、乙 基環己烷及薛卓(Shellzole)TH(商品名,日本殼牌公司製造 )、芳香族烴類如甲苯、二甲笨及史瓦卓(Swaz〇le)1〇〇(商品 名,丸#石化公司製造)、酯類如乙酸丁酯及優卡酯 Ester) EEP(商品名,永備公司製造)、及醇類如丁醇、異丁 醇及乙二醇一丁_。 聚合引發劑例如包括過氧化物如己酸第三丁基過氧基 -2-乙酯、過氧化笨甲醯及過氧化二苯二甲醯,及以偶氮為主 之引發劑如偶歧異丁歧2,2,·偶Mo二甲基戊腈)。 反應溫度通常調整為⑼它至丨⑼它,且較佳8〇。(:至14〇 C。反應終點係由反應溶液之黏度穩定而測定。 結果所彳于之聚烯烴彈性體具有數目平均分子量為 3,000至200,000,且較佳為1〇,〇〇〇至1〇〇 〇〇〇。當數目平均分 :量小於3,咖時,經塗覆之複合薄膜外觀低劣。相反地, 田數目平均分子ϊ超過2〇〇,〇〇〇時,聚烯烴彈性體於溶劑之 溶解度低劣。 此外,較佳?<稀烴彈性體具有經基及/或絲。更佳聚 稀L彈性體具有^基及羧基二者。經由使肖含—或多個官 200427795 能基之聚烯烴彈性體,可進一步改良結果所得之經塗覆之 複合薄膜的物理性質及耐切晶片性質。 聚烯烴彈性體之酸價較佳為1至50毫克KOH/克及更佳 為5至30毫克KOH/克。當酸價超過50毫克KOH/克時,所得 5 經塗覆之複合薄膜之防水性降低。此外,聚烯烴彈性體之 羥基值較佳為1至200,及更佳為50至150。當羥基值超過200 時,所得經塗覆之複合薄膜之防水性降低。 以樹脂固型物含量之重量為基準,聚烯烴彈性體(d)於 中間塗料之含量為30至60%重量比且較佳為30至40%重量 10 比。當含量小於30%時,未見所得經塗覆之複合薄膜之物 理性質及塗膜外觀改良。當含量超過60%時,塗料之可相 容性降低,結果導致不均勻。 經由含括聚烯烴彈性體作為中間塗料之成分,塗膜之 伸長率改良,塗膜之耐切晶片性質也改良。此外,因中間 15 塗膜與頂塗膜間之相容性降低且底塗膜或透明塗膜不會滲 透入濕中間塗膜,故可防止相的混合,以及外觀改善,特 別為光澤外觀改善。 嵌段異氰酸酯化合物(c)為用來硬化以胺基甲酸酯改性 之聚酯樹脂(a)及聚烯烴彈性體(b)之成分。 20 嵌段異氰酸酯化合物係經由添加嵌段劑至脂肪族異氰 酸酯或其衍生物獲得。當嵌段異氰酸酯化合物被加熱時, 嵌段劑解離,而產生異氰酸基,異氰酸基與以胺基甲酸酯 改性之聚酯樹脂之經基反應而硬化材料。 脂肪族異氰酸酯及其衍生物例如包括用於製備以胺基 14 200427795 甲酸酯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驢基丙酮、乙si基乙酸乙自旨及丙二 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。 5 嵌段異氰酸酯化合物例如由旭化學工業公司出售為 活性亞甲基型嵌段異氰酸酯「杜蘭内特(Duranate) MF-K60X」。 中間塗料之嵌段異氰酸酯化合物(c)之含量,以塗料之 樹脂固體重量含量為基準,為15至3〇%重量比且較佳為17 10 至25%重量比。當含量小於15%重量比時,硬化性不足;而 當含量超過30%重量比時,硬化後之薄膜太硬也太脆。 蜜胺樹脂(d)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-丁基混合性蜜胺樹脂。例如包括r 賽莫(Cymel)_303」、「賽莫254」、「優邦(U ban ) 128」及「優 15邦20N60」係由三井東壓公司出售,以及「蘇敏那(sumimar) 系列」由住友化學公司出售。 以樹脂固型物含量重量為基準,蜜胺樹脂(d)於中間塗 料之含量至多為20%重量比,及更佳為5至15%重量比。當 蜜胺樹脂之含量超過20%重量比時,硬化後之塗膜變太硬 2〇 也太脆。 具有芯-殼結構之非水性分散液樹脂(e)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脂粒子,該粒子不溶於 。亥合浴液。欲於为政液文疋樹脂存在下,共聚合來_得 15 200427795 非又叫脂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。 為了合成前述分錄安定樹脂及非水性分散液 ,較佳 使-有B此基之可聚合單體,原因在於具有官能基之非 刀政/夜可與硬化劑連同與含官能基之分散液安定樹脂 反應而形成一種三維交聯之經塗覆之薄膜。 分散液安定樹脂並無特殊限制,只要可於有機溶劑穩 水s日树月日、?炎醚樹脂、聚碳酸醋樹脂、聚胺基甲酸醋樹脂 〇等八/、有^工基值10至250且較佳20至180,酸值0至1〇〇毫 克KOH/克且較佳〇至5〇毫克K〇H/克以及數目平均分子量 800至100,000且較佳為1〇〇〇至2〇,〇〇〇。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 質也降低。當參數低於下限時,塗膜可能被解吸附,當調 15配成經塗覆之薄膜時,粒子穩定性降低。 月丨J述刀政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,用於獲得前述分散液安定樹脂之單體可依據樹脂性質 2〇適當逛用,但較佳使用具有官能基(如羥基、酸基等)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(容後詳述),·進-步若有所需,可使用具有官能基如縮水 甘油基、異氰酸基等之單體。 此外,前述分散液安定樹脂與可聚合單體之重量比可 16 427795 依據使用目的任意選用。例如以兩種成分總重為基準,前 述分散液安定樹脂為3至80%重量比,特別5至6〇%重量比, 可來合單體為97至20%重量比且特別為95至40%重量比。此 外,以總重為基準,分散液安定樹脂及可聚合單體於有機 /谷背彳之總濃度較佳為30至80%重量比,特別為40至60%重量 比。 前述非水性分散液可經由於分散液安定樹脂存在下, 來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KOH/ 1〇克且較佳為0至50毫克KOH/克以及平均粒子直徑(D5〇)為 〇·〇5至ίο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。 用來合成前述非水性分散液之具有官能基之可聚合單 15 體之代表例如後。具有羥基之單體例如包括(甲基)丙烯酸羥 基乙醋、(甲基)丙烯酸羥基丙酯、(甲基)丙烯酸羥基丁酯、 (甲基)丙烯酸羥基曱酯、丙烯醇,以及(曱基)丙烯酸羥基乙 酉旨與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 20基等之可聚合單體。具有羧基之單體例如包括(曱基)丙烯酸 巴豆酸、乙基丙烯酸、丙基丙烯酸、異丙基丙稀酸、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。當使用具有酸基 之可聚合單體時,較佳部分酸基為羧酸基。 17 200427795 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,α-二曱基嶋基異氰酸酯 、丙烯酸異氰酸基乙s旨等。 5 其它可聚合單體例如包括(甲基)丙烯酸烷基酯,例如( 曱基)丙烯酸甲酯、(甲基)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、(甲基)丙烯酸正辛酯、(甲基)丙烯酸月桂酯、(甲基)丙 10 烯酸硬脂酯及(曱基)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甲基丙烯酸酯單體之加成反應產物( 例如硬脂酸與曱基丙烯酸縮水甘油酯之加成反應產物等) ;含(:3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-甲基苯乙 15 烯、間-甲基苯乙烯、對-甲基苯乙烯、對-第三丁基苯乙烯 、(甲基)丙烯酸嶋酯、衣康酸酯(衣康酸二甲酯)、順丁烯二 酸酯(順丁稀二酸二曱酯)、反丁稀二酸酯(反丁烯二酸二甲 酯);以及其它可聚合單體例如丙烯腈、甲基丙烯腈、甲基 異丙烯基甲酮、乙酸乙烯酯、微巴(Veoba)單體(殼牌化學公 20 司製造,商品名)、丙酸乙烯酯、特戊酸乙烯酯、乙烯、丙 烯、丁二烯、丙烯酸N,N-二甲基胺基乙酯、甲基丙烯酸N,N-二甲基胺基乙酯、丙烯醯胺及乙烯基吡啶。 較佳用於獲得非水性分散液之聚合反應係於基團聚合 引發劑存在下進行。基團聚合引發劑例如包括以偶氮為主 18 200427795 之引發劑,例如2,2’-偶氮貳異丁腈及2,2’-偶氮貳(2,4-二甲 基戊腈)、過氧化苯甲醯、過氧化月桂醯、過辛酸第三丁酯 等。較佳相對於總量100份重量比可聚合單體,此種引發劑 用量為0.2至10份重量比且較佳為0.5至5份重量比。較佳用 5 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60°C至160°C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 10 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。 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 15 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(e)之含量為15%重量比且較佳為5至12%重量比。 當含量超過15%重量比時,耐切晶片效能降低。 經由使用非水性分散液樹脂(e),可防止各塗層間之溶 20 混且外觀改善。 至於片狀顏料⑴可使用雲母、鋁氧、滑石及矽氧,由 切晶片效能觀點,較佳使用滑石。 較佳片狀顏料⑴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 19 200427795 時,薄膜外觀低劣,無法獲得足夠耐切晶片效能。而當粒 子直徑於前述範圍以外時,同理,經塗覆之薄膜之外觀變 差,且無法獲得足夠耐切晶片效能。 以100份重量比樹脂固型物含量為基準,片狀顏料⑴ 5 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 獲得足夠而寸切晶片效能。 其它可包含之樹脂並無特殊限制,包括丙烯酸系樹脂 、聚酯樹脂、醇酸樹脂、環氧樹脂等。此等樹脂可單獨使 10 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 、以二氧己環為主之顏料、以喳吖啶酮為主之顏料、以異 15 吲哚啉酮為主之顏料、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,至於增量劑顏料,可使用碳酸妈、 硫酸鋇、鋁粉、高嶺土等。 使用含有碳黑及二氧化鈦之以灰色為主之著色顏料作 20 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 作能力,可添加流變劑至前述中間塗料。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 20 200427795 脂肪酸醯胺、醯脸昨 月曰肪I、長鏈多胺醯胺磷酸鹽等之溶脹 分散液;以聚乙馀么+ 冲為主之化學劑例如聚環氧乙烷等之膠體 溶齡錢;以有機4土為主之化學劑如有機酸綠土、蒙 脫土等…、機顏料如石夕酸紹、硫酸鎖等;片狀顏料顯示之 黏度雜據顏料形狀、交聯樹脂粒子等決定。 本毛月使用之中間塗料之固型物含量總量於施用時為 30至80%重里比且較佳為%至㈣重量比。當含量於此範圍 ίο 15200427795 发明 Description of the invention: The technical field of the invention is: 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 layer through a three-coat film drying method. Method for covering composite film. L Prior Art 3 Background of the Invention There are two ways to form a coated composite film. 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-A No. 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 promotes the appearance of the film. 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, the three-coat film drying method has the following problems, for example. In some cases, the peeling of the coating film occurs by a so-called dicing wafer, and the dicing wafer occurs when a moving vehicle hits a cobblestone and the cobblestone hits the coating film. In the conventional method of forming a coated composite film, for example, an individual baking method for each application of coating and a one-time baking method for two coating films, a base coating film and an intermediate coating film are respectively baked and hardened. Therefore, the strategy 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 degree of the top film and the brightness of the base coating film to form an intermediate coating film that has not yet been peeled off. 5 For example, Jp-A No. 2002 · 249699 and JP-A No. 9-208882 describe a wafer cutting primer coating composition, and the wafer coating film is cut only after the coated composite film is formed. In addition, in JP-A No. 6-256714 or JP-A No. 6-254482, the improvement of cut-resistance wafer properties is studied from the viewpoint of an intermediate coating composition, but the improvement degree of 10 degrees is not sufficient for a three-coat film baking method. In addition, the car body has many uneven parts. When the entire surface of the car body is coated by the three-coat film once, there is a problem that it is easy to cause the appearance to deteriorate. [Akimoto 3 15 Summary of the Invention The present invention can solve the aforementioned conventional problems, and the object of the present invention is to provide a method for forming a coated composite film with excellent cut-resistant wafer properties by a two-coat film and one-time baking method. The present invention provides the intermediate coating based on the resin solid content of 20, containing (a) 5 to 30% by weight of a urethane-modified polyester resin having a number average molecular weight of 1, 500 to 3,000, which is obtained by reacting an aliphatic isocyanate compound with a hydroxyl-containing polyester resin having a glass transition point (Tg) of 40 ° C to 80 ° C, and the polyester is obtained by containing 80 mol% or more 6 200427795 Obtained by polycondensation of phthalic acid and polyhydroxy alcohol, (b) 30 to 60% by weight of polyolefin elastomers having acid groups and / or hydroxyl groups, and 10 to 30% by weight of block isocyanate compounds . 5 [Embodiment] Detailed description of the preferred embodiment The intermediate coating film is formed in the coating film forming method of the present invention. The intermediate coating material for forming the intermediate coating film contains a urethane-modified polyester resin (a), Polyolefin elastomer 10 (b) and block isocyanate compound (c). If necessary, the intermediate coating may further contain a melamine resin (d), a non-aqueous dispersion resin (e) having a core-shell structure, and a flake pigment (f). The amino resin-modified polyester resin (a) can be obtained by reacting a hydroxyl-containing polyester resin with an aliphatic isocyanate compound. 15 In general, polyester resins are prepared by polycondensation of an acid component such as a carboxylic acid, an anhydride, and an acid gas with a monohydric alcohol or a polyhydric alcohol. The hydroxyl-containing polyester resin used in the present invention contains an acid component used in the polycondensation reaction of phthalic acid at 80 mol% or more based on the total molar number of acid components. When the content of isophthalic acid in the acid component is less than 80 mol%, the glass transition temperature (Tg) of the obtained hydroxyl-containing polyester resin 20 becomes lower than a desired range. Acid components other than isophthalic acid include, for example, phosphophthalic acid, phosphophthalic anhydride, tetrahydrophosphophthalic acid, tetrahydrophosphophthalic anhydride, hexahydrophosphophthalic acid, and hexahydrophosphoxylene Anhydride, methyltetrahydrophosphophthalic acid, methyltetrahydrophosphophthalic anhydride, himic acid anhydride, trimellitic acid, trimellitic anhydride 7 200427795, pyromellitic acid, pyromellitic acid Anhydride, terephthalic acid, maleic acid, maleic anhydride, fumaric acid, itaconic acid, adipic acid, azelaic acid, sebacic acid, succinic acid, succinic anhydride, ten Dicarbenyl succinic acid, dodecenyl succinic anhydride, and the like. In addition, as for the acid component, an acid other than polyvalent pentavalent acid and polyvalent retarding anhydride, which are commonly used in the preparation of polyester resins, may be contained. Such acids include, for example, monoweilic acid and hydroxycarboxylic acids. As the acid used for preparing the hydroxyl-containing polyester resin, isophthalic acid may be used alone, or other acids may be used in combination. Polyhydric alcohols include, for example, ethylene glycol, diethylene glycol, polyethylene glycol, propylene glycol, dipropylene glycol, polypropylene glycol, neopentyl glycol, 1,2-butanediol, 1,3-10 butanediol, 1 4,4-butanediol, 2,3-butanediol, 1,5-pentanediol, 1,6-hexanediol, 1,4-ammonium adipase, 2,2-dimethyl-3 -Technyl propyl-2,2-dimethyl-3 -caproyl propionate, 2,2,2-trimethylidene-1,3-pentanediol, polytetramethylene ether glycol, poly Caprolactone polyol, glycerol, sorbitol, annitol, trimethylolethane, trimethylolpropane, trimethylolbutane, hexanetriol, pentaerythritol 15 tetraol, Dipentaerythritol and so on. In the preparation of the hydroxyl-containing polyester resin, in addition to the acid component and the polyhydric alcohol, 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. The intrinsic moieties can form graft chains through ring-opening addition of polyester resins formed from 20 to polyvalent carboxylic acids and polyhydric alcohols. Lactones include, for example, cold-propiolactone, dimethylpropiolactone, butyrolactone, T-valerolide, ε-caprolactone, caprolactone, caprylic vinegar, crotonide, 5 -Valerolactone, ά -caprolactone, etc. Particularly, ε-caprolactone is most preferable. Specific examples include an epoxy compound such as Carjula E (manufactured by Shell Chemical Co., Ltd. 8 200427795) caprolactones. The hydroxyl-containing polyester resin has a glass transition temperature (Tg) of 4 (rc to 85 1 and preferably 45 ° C. to 75X :. When the glass transition temperature (Tg) is lower than 40.0, the film hardness decreases. When Tg is higher than 80 ° C, the chip-cutting resistance is reduced. 5 Aliphatic isocyanate S compounds include, for example, hexamethylene diisocyanate, trimethylhexamethylene diisocyanate, cyclohexane-丨, 'Diisocyanate, monocyclohexyl-4,4-diisocyanate, methylcyclohexyl diisocyanate, and isophor S with diisocyanate g. In particular, the chip-resistant performance of the coated composite film And 10 points of weather resistance, hexamethylene diisocyanate or trimethyl hexamethylene diisocyanate is preferably used. Biuret, isocyanurate, and adducts thereof can be used. The purpose of the polymer containing the radical The reaction between the resin and the aliphatic isocyanate g can be carried out by a method known to those skilled in the art. The amino resin modified polyester resin (a) has a number average molecular weight 15 (Mn) of 150 to 3000. And preferably from 1700 to 2500. When the molecular weight is less than 1500, workability and hardenability are insufficient. When the molecular weight is When it exceeds 3,000, the non-volatile content at the time of 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. 20 Carbamate The modified polyester resin (a) has a hydroxyl value (0HV) of preferably 30 to 180 and more preferably 40 to 160. When the hydroxyl value exceeds 180, the water resistance of the coated composite film decreases. When the value is less than 30, the hardenability of the coated composite film is reduced. 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 9 200427795 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. Contained in the intermediate coating The content of the urethane-modified polyester resin (a) is 5 based on the solid content of the resin, and the content is 5 to 30% by weight and preferably 10 to 30% by weight. When the content is less than When the weight ratio is 5%, the cut-resistant wafer performance becomes insufficient. When the content exceeds 30% by weight, the coated composite film The degree of reduction is considered. By including a polyester resin modified with urethane as an intermediate 10 coating component, the elasticity of the coated composite film is improved, and the properties of the coated cut-resistant wafer are also improved. Polyolefin elastomer ( b) Usually a polyolefin-based graft polymer. The polyolefin elastomer (b) is prepared, for example, by copolymerizing a polyolefin-based macromonomer with an ethylenically unsaturated compound. 15 Polyolefins are The main macromonomer means a polymer monomer having an ethylenically unsaturated group at the end of the polyolefin chain. The macromonomer mainly consisting of a polyolefin is, for example, via a polyolefin having a hydroxyl group and having an ethylenically unsaturated group. The acid or anhydride of the group is obtained by reaction. Polyolefins having a hydroxyl group include, for example, polyolefin-based resins such as polyethylene, polypropylene, polybutene, hydrogenated polybutadiene, polyisoprene, hydrogenated polyisoprene, EPDM, etc. The remaining ends have hydroxyl groups. It preferably has a number average molecular weight of 200 to 5000, and more preferably 500 to 4000. Commercially available polyolefins having a hydroxyl group include, for example, the following: 10 200427795 [Table i] Trade name manufacturer compound Mη G-1000 Saibon Soda Corporation α, ω-polybutadiene glycol about 15,00 G-2000 Yuan Caoda Corporation α, ω-polybutadiene glycol approximately 2,000 G-3000 Caoda Corporation Japan α, ω-polybutadiene glycol approximately 29,00 G-1000 Butadiene glycol approximately 15,00 G-2000 Alpha, omega-hydrogenated polybutadiene glycol from Japan's Soda Corporation approximately 21,000 G-3000 Alpha, omega-hydrogenated polybutadiene glycol from Japan's Soda Corporation 3,000 R-15HT α-polybutadiene glycol from effluent petrochemical company, about 1,200 R-45HT α, ω-polybutadiene glycol from effluent petrochemical company, about 2,800 LIR-506 polyisoprene from Kuraray Pentaol is about 25,000 acid anhydrides having a rare unsaturated group, and examples include maleic anhydride, itaconic anhydride, succinic anhydride, and the like. Among them, the use of maleic anhydride is particularly preferred. 5 The reaction of a polyolefin having a hydroxyl group with an acid or an anhydride having an ethylenically unsaturated group can be performed by a method known to those skilled in the art. Polyolefin-based macromonomers can be obtained by reacting a polyolefin having a hydroxyl group, a diisocyanate compound, and an alcohol having an ethylenically unsaturated group. The alcohol having an ethylenically unsaturated group includes, for example, a hydroxyl-containing acrylic monomer. 10 As for the diisocyanate compound, an aliphatic diisocyanate for preparing a urethane-modified polyester resin can be used. Particularly preferred is isophorone diisocyanate. As the hydroxyl-containing acrylic monomer, for example, hydroxyethyl methacrylate (HEMA), hydroxyethyl acrylate (HEA), hydroxy 15-propyl methacrylate (HPMA), hydroxypropyl acrylate (HPA), and Hydroxybutyl acrylate (BBA). These monomers can be used alone or by mixing two or more kinds. Among these hydroxyl-containing acrylic monomers, it is particularly preferable to use hydroxyethyl (meth) acrylate. The reaction of a hydroxyl-containing polyolefin, a diisocyanate compound, and an alcohol having an ethylenically unsaturated group can be performed by methods known to those skilled in the art. The ethylenically unsaturated compounds to be copolymerized with the polyolefin-based macromonomer include ethylenically unsaturated monomers, unsaturated acrylic resins, unsaturated polyester resins, and the like. 5 Ethylenically unsaturated monomers include, for example, acrylic monomers such as methyl acrylic acid, methyl methacrylate, acrylic acid, methacrylic acid, hydroxyethyl acrylate, methyl ethyl acrylate, Butyl and n-butyl methacrylate. These acrylic monomers may be used alone or in combination of two or more. In addition, other monomers copolymerizable with acrylic monomers, such as styrene and vinyl acetate, can be used. The unsaturated acrylic resin is introduced into the acrylic resin as an unsaturated bond. For example, unsaturated acrylic resins can be obtained by addition of glycidyl acrylate to carboxyl groups of acrylic resins; obtained by addition of anhydrides having unsaturated bonds to hydroxyl groups of acrylic resins; or additions having unsaturated bonds of 15 It is obtained from carboxylic acid to ethylene oxide group of acrylic resin. As for the unsaturated acrylic resin, it is preferable to have an acid value of 0 to 200 mg KOH / g, and more preferably 0 to 150 mg KOH / g, an M base value of 10 to 300 and more preferably 10 to 200, and a number average molecular weight of 1 0.00 to 50,000 and more preferably 2000 to 5000, and iodine value of 0.5 to 100 and more preferably 0.5 to 70. 20 The unsaturated polyester resin can be obtained by a conventional method such as the reaction of a polyol compound with a polyacid compound having an unsaturated group. For unsaturated polyester resins, it is preferred to have an acid value of 0 to 200 mg of KOH / g, and more preferably 0 to 150 mg of KOH / g, a hydroxyl value of 10 to 300, and more preferably 10 to 200. The number The average molecular weight is from 1,000 to 5,000 and more preferably from 1,000 to 40,000, 12 and the iodine value is from 0.5 to 100 and more preferably from 0 to 5 and 70. The copolymerization of polyolefin-based macromonomers and ethylenically unsaturated compounds can be carried out by a method known to those skilled in the art. For example, according to the solution polymerization method, the macromonomer mainly containing olefins is dissolved in an appropriate solvent, the temperature is increased, and then the ethylenically unsaturated compound and an appropriate polymerization initiator are added dropwise thereto while stirring. Suitable solvents for the reaction include, for example, aliphatic hydrocarbons such as kerosene, ethylcyclohexane, and Shellzole TH (trade name, manufactured by Shell Corporation of Japan), aromatic hydrocarbons such as toluene, dimethylbenzyl, and Swadzu. (Swazole) 100 (trade name, manufactured by Maru #Petrochemical Co., Ltd.), esters such as butyl acetate and eucalyptus Ester) EEP (trade name, manufactured by Yong Bei Corporation), and alcohols such as butanol, isopropyl Butanol and ethylene glycol monobutyrate. Polymerization initiators include, for example, peroxides such as tert-butylperoxy-2-ethylhexanoate, benzamidine peroxide and diphenylmethaneperoxide, and azo-based initiators such as azodiffusion Butyl 2,2 ,. Even Mo dimethylvaleronitrile). The reaction temperature is usually adjusted to ⑼ to ⑼, and is preferably 80. (: To 14 ° C. The reaction end point is determined by the stability of the viscosity of the reaction solution. As a result, the polyolefin elastomer having a number average molecular weight of 3,000 to 200,000, and preferably 10,000 to 1〇 〇〇〇〇〇. When the average number of points: the amount is less than 3, the appearance of the coated composite film is inferior. On the contrary, when the average molecular weight of the field number exceeds 20,000, the polyolefin elastomer in the solvent Its solubility is poor. In addition, it is preferred that the dilute hydrocarbon elastomer has a warp group and / or a silk. A better polylean L elastomer has both a carboxyl group and a carboxyl group. By making Xiaohan—or multiple official 200427795 energy groups The polyolefin elastomer can further improve the physical properties and chip-resistant properties of the resulting coated composite film. The acid value of the polyolefin elastomer is preferably 1 to 50 mgKOH / g and more preferably 5 to 30. Mg KOH / g. When the acid value exceeds 50 mg KOH / g, the water resistance of the obtained 5 coated composite film decreases. In addition, the hydroxyl value of the polyolefin elastomer is preferably 1 to 200, and more preferably 50. To 150. When the hydroxyl value exceeds 200, the obtained coated composite film Water resistance is reduced. Based on the weight of the resin solid content, the content of the polyolefin elastomer (d) in the intermediate coating is 30 to 60% by weight and preferably 30 to 40% by weight. When the content is less than 30 %, The physical properties of the obtained coated composite film and the appearance of the coating film are not improved. When the content exceeds 60%, the compatibility of the coating is reduced, resulting in non-uniformity. By including a polyolefin elastomer as an intermediate The composition of the coating, the elongation of the coating film is improved, and the chip resistance of the coating film is also improved. In addition, the compatibility between the middle 15 coating film and the top coating film is reduced, and the base coating film or the transparent coating film will not penetrate into the wet The intermediate coating film can prevent the mixing of phases and improve the appearance, especially the gloss appearance. The block isocyanate compound (c) is used to harden the urethane-modified polyester resin (a) and polyolefin. The component of the elastomer (b). 20 The block isocyanate compound is obtained by adding a block agent to an aliphatic isocyanate or a derivative thereof. When the block isocyanate compound is heated, the block agent dissociates to generate an isocyanate group, different Cyanate groups harden materials by radical reaction with polyester resins modified with urethanes. Aliphatic isocyanates and their derivatives include, for example, those used to prepare polyester resins modified with amine 14 200427795 formate. Blocking agents include, for example, compounds having active methylene groups such as ethoxylated acetone, ethoxylated ethyl acetate, and ethyl malonate. By using a blocking agent, the elasticity of the coated composite film is improved The chip resistance of the coated composite film is also improved. 5 Block isocyanate compounds are sold, for example, by Asahi Chemical Industry Co., Ltd. as active methylene-type block isocyanates "Duranate MF-K60X". Intermediate paint The content of the block isocyanate compound (c) is 15 to 30% by weight and preferably 17 10 to 25% by weight based on the resin solid weight content of the coating. When the content is less than 15% by weight, the hardenability is insufficient; and when the content exceeds 30% by weight, the hardened film is too hard and brittle. The melamine resin (d) is not particularly limited, but includes a methylated melamine resin, a butylated melamine resin, or a methyl-butyl mixed melamine resin. Examples include r Cymel_303 ”,“ Symo 254 ”,“ U ban 128 ”and“ U 15 State 20N60 ”are sold by Mitsui Toyo Co., and the“ Sumimar ”series "Sold by Sumitomo Chemical. The content of the melamine resin (d) in the intermediate coating is at most 20% by weight, and more preferably 5 to 15% by weight based on the content of the resin solid content. When the content of the melamine resin exceeds 20% by weight, the hardened coating film becomes too hard and too brittle. The non-aqueous dispersion liquid resin (e) having a core-shell structure can be prepared by copolymerizing a dispersion stabilizer resin and a copolymerizable monomer in a mixed solution containing an organic solvent, and the copolymer is obtained to obtain non-crosslinked resin particles. Insoluble. Haihe bath. Copolymerization in the presence of political liquid resins is not particularly limited, as long as it is a group-polymerizable unsaturated monomer. In order to synthesize the above-mentioned entry stable resin and non-aqueous dispersion liquid, it is preferable to use a polymerizable monomer having a B group because the non-knife / night with functional group can be combined with a hardener and a dispersion liquid containing a functional group. The stabilization resin reacts to form a three-dimensionally cross-linked coated film. There is no special restriction on dispersion stabilizer resin, as long as it can be stabilized in organic solvents Inflammable ether resins, polycarbonate resins, polyurethane resins, etc., have a base value of 10 to 250 and preferably 20 to 180, and an acid value of 0 to 100 mg KOH / g and preferably. To 50 mg KOH / g and a number average molecular weight of 800 to 100,000 and preferably 1,000 to 20,000. 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. When formulated into a coated film, the particle stability is reduced. The method for synthesizing stable resins of the knife solution 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, the monomers used to obtain the stable resin of the dispersion can be appropriately used according to the properties of the resin, but it is preferable to use monomers having functional groups (such as hydroxyl groups, acid groups, etc.), which are used for synthesis Possibility of polymerizable monomers in non-aqueous dispersion (described later in detail).-If necessary, monomers having functional groups such as glycidyl, isocyanate, etc. can be used. In addition, the weight ratio of the dispersion resin and the polymerizable monomer may 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 blendable monomer is 97 to 20% by weight and particularly 95 to 40. %weight ratio. In addition, based on the total weight, the total concentration of the dispersion stabilizer resin and the polymerizable monomer in the organic / glutarium is preferably 30 to 80% by weight, and particularly 40 to 60% by weight. The non-aqueous dispersion can be obtained by polymerizing a 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 / 10 g and preferably 0 to 50 mg KOH / g and the average particle diameter (D50) is from 0.05 to 1 μm and preferably from 0 to 2 μm. When the parameter is below the lower limit, the particle shape cannot be maintained. When the parameter exceeds the upper limit, the stability of dispersion in the coating decreases. Representative examples of polymerizable monomers having a functional group used to synthesize the aforementioned non-aqueous dispersion are as follows. The monomer having a hydroxyl group includes, for example, hydroxyethyl (meth) acrylate, hydroxypropyl (meth) acrylate, hydroxybutyl (meth) acrylate, hydroxymethyl (meth) acrylate, allyl alcohol, and (fluorenyl) ) Adduct of hydroxyethyl 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 group, or the like. Examples of the monomer having a carboxyl group include (fluorenyl) acrylic acid, crotonic acid, ethacrylic acid, propylacrylic acid, isopropylacrylic 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. 17 200427795 In addition, polymerizable monomers having functional groups include, for example, unsaturated monomers containing glycidyl groups such as glycidyl (meth) acrylate; and unsaturated monomers containing isocyanate groups such as m-isopropenyl , Α-Difluorenylfluorenyl isocyanate, acrylic isocyanatoethyl s, etc. 5 Other polymerizable monomers include, for example, alkyl (meth) acrylates, such as methyl (fluorenyl) acrylate, ethyl (meth) acrylate, isopropyl (meth) acrylate, n-propyl (meth) acrylate Ester, n-butyl (meth) acrylate, third butyl (meth) acrylate, isobutyl (meth) acrylate, 2-ethylhexyl (meth) acrylate, n-octyl (meth) acrylate , Lauryl (meth) acrylate, stearyl (meth) propenoate, and tridecyl (fluorenyl) acrylate; oil fatty acids and acrylic or methacrylate monomers with ethylene oxide structures Addition reaction products (such as the addition reaction products of stearic acid and glycidyl methacrylate, etc.); addition reaction products of ethylene oxide compounds containing (: 3 or more alkyl groups and acrylic acid or methacrylic acid, Styrene, α-methylstyrene, o-methylstyrene 15ene, m-methylstyrene, p-methylstyrene, p-third butylstyrene, methacrylate (meth) acrylate, Itaconic acid ester (dimethyl itaconate), maleic acid ester (maleic acid) Acid dimethyl ester), fumarate (dimethyl fumarate); and other polymerizable monomers such as acrylonitrile, methacrylonitrile, methisopropenone, vinyl acetate, Veoba monomer (manufactured by Shell Chemical Company 20, trade name), vinyl propionate, vinyl pivalate, ethylene, propylene, butadiene, N, N-dimethylaminoethyl acrylate , N, N-dimethylaminoethyl methacrylate, acrylamide and vinylpyridine. The polymerization reaction preferably used to obtain a non-aqueous dispersion is carried out in the presence of a group polymerization initiator. Group polymerization Initiators include, for example, azo-based initiators 18 200427795, such as 2,2'-azobisisobutyronitrile and 2,2'-azobis (2,4-dimethylvaleronitrile), peroxide Benzamidine, lauryl peroxide, tert-butyl peroctoate, etc. The amount of such initiator is preferably 0.2 to 10 parts by weight and preferably 0.5 to 100 parts by weight based on the total amount of polymerizable monomers. 5 parts by weight. It is preferred to use 5 for the polymerization of a non-aqueous dispersion obtained from an organic solvent containing a dispersion stabilizer resin. It is usually carried out at a temperature range of about 60 ° C to 160 ° C for 1 to 15 hours. In addition, the non-aqueous dispersion is a particle component in a coating different from the cross-linked polymer particles, but it has a coating composition The film does not form the characteristics of the particle structure. In other words, the difference between the non-aqueous dispersion and the crosslinked polymer particles is that since the particles do not have crosslinked sites, the shape of the particles changes during the baking process and can be a resin component. For example, it is also possible to use resin particles called NAD (non-aqueous dispersion), which is described in Coloring Material No. 48 (1975), pages 28-34, and is used for NAD 15 coatings. Based on the weight of the resin solid content The content of the non-aqueous dispersion resin (e) of the intermediate coating is 15% by weight and preferably 5 to 12% by weight. When the content exceeds 15% by weight, the cut-resistant chip performance decreases. By using the non-aqueous dispersion resin (e), it is possible to prevent miscibility between the coating layers and improve the appearance. As for flake pigments, mica, alumina, talc, and silica can be used. From the viewpoint of chip performance, talc is preferred. Preferred flake pigments ⑴ have 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 out of this range, 19 200427795, the appearance of the film is inferior, and sufficient cut-resistant wafer performance cannot be obtained. When the diameter of the particles is outside the foregoing range, the appearance of the coated film is deteriorated, and sufficient chip-cutting resistance cannot be obtained. The content of the flake pigment ⑴ 5 is 0.4 to 2 parts by weight based on 100 parts by weight of the resin solid content. It is more preferably 0.5 to 1.5 parts by weight. When the content is outside this range, the adhesiveness with the undercoat film is reduced, and sufficient chip-cutting performance cannot be obtained. Other resins that can be included are not particularly limited, including acrylic resins, polyester resins, alkyd resins, epoxy resins, and the like. These resins can 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 dinaphthol, pigments based on dioxane, pigments based on fluoracridone, pigments based on iso 15 indololinone, metal complex pigments, etc. As an 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, as for the extender pigment, carbon monoxide, barium sulfate, aluminum powder, kaolin, and the like can be used. As the main pigment, a gray-based coloring pigment containing carbon black and titanium dioxide is used. 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 each layer from being compatible with the top coating film and maintain the coating workability, a rheological agent may be added to the aforementioned intermediate coating. Rheological agents include, for example, materials that generally have thixotropic properties, such as polyamine-based chemicals such as 20 200427795 fatty acid amidoamine, fatty acid amidine, long-chain polyamine ammonium phosphate, and swelling dispersions ; Chemical agents mainly based on polyethylenimine + red, such as polyethylene oxide, etc .; Chemical agents based on organic 4 soil such as organic acid smectite, montmorillonite, etc., organic pigments such as Shixi acid shao, sulfuric acid lock, etc .; the viscosity of flake pigments is determined by the shape of the pigment, crosslinked resin particles, etc. The total solid content of the intermediate coating used in this hair month is 30 to 80% by weight and preferably% to ㈣ by weight when applied. When the content is within this range ίο 15
卜才、主料私定度降低。當含量超過上限時,黏度過高 ’經塗覆之_外觀下降。當含量低於下限時,黏度過低 出現如各層〉谷混以及不均勻等劣化外觀。 除了 4等分外’其它通常添加至塗料之添加劑例如表 面調整劑' Μ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。 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,反而包括丙稀酸系樹脂 、聚酯Bu Cai, the main ingredients of the private degree decreased. When the content exceeds the upper limit, the viscosity is too high. When the content is lower than the lower limit, the viscosity is too low, and appearances such as various layers> valley mixing and unevenness appear. In addition to 4 aliquots, other additives commonly added to coatings, such as surface modifiers, defoamers, and defoamers, 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. In addition, other resins may be contained in the urethane-modified polyester resin. There are no special restrictions on this resin, but it includes acrylic resins, polyesters
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 去並揲彳寸殊限制,熟諳技藝人士眾所周知之方法例如使 2〇用混練機、輥及SG磨機混練且分散顏料攙合物之任一種方 法皆可使用。 底塗膜 用於本發明之塗膜形成方法之底塗料係用來使用透明 塗料形成頂塗膜。此種底塗料含有成膜樹脂、硬化劑、著 21 200427795 色顏以及若有所需含有光澤彩色顏料等。 前述底塗料所含之成膜樹脂並無特殊限制,其範例包 括丙烯酸系樹脂、聚_脂、醇酸樹脂、環氧樹脂、胺基 甲酸醋樹脂等。此等樹脂可單獨使用或組合兩種或兩種以 上使用。 前述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’較錢用絲樹毅/或嵌段異氛酸 酯樹脂。Resin, alkyd resin, epoxy resin, etc. The resin may be used alone or in combination of two or more. A method for preparing the coating composition used in the present invention includes the methods described below and is not limited. Any method well known to those skilled in the art, such as mixing and dispersing pigment compounds with a kneader, roller, and SG mill, is used. Either method can be used. Undercoating film The undercoating film used in the coating film forming method of the present invention is used to form a topcoating film using a clear coating. This primer contains film-forming resins, hardeners, pigments, and pigments, etc., if necessary. The film-forming resin contained in the aforementioned primer is not particularly limited, and examples thereof include acrylic resins, polyesters, alkyd resins, epoxy resins, and urethane resins. These resins may be used alone or in combination of two or more. The aforementioned film-forming resin can be used in combination with a hardener. From various viewpoints of the effectiveness and the cost of the resulting coating film, it is more economical to use silk tree // block isocyanate resin.
以成膜樹脂之固型物含量重量為基準,前述硬化劑含 H)量較佳為20至60%重量比及更佳物至鄕重量比。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,至於前述著色顏料,例如可含有對前述中間塗 料舉例說明之著色顏料。 15 冑述底塗料選擇性含有之金屬顏料的形狀並無特殊限Based on the solid content and weight of the film-forming resin, the hardener contains H) in an amount of preferably from 20 to 60% by weight and more preferably from 鄕 to 鄕 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. The coloring pigment may include, for example, a coloring pigment exemplified for the intermediate coating material. 15 There is no particular limitation on the shape of the metallic pigments optionally contained in the primer
制。金屬顏料可經著色。例如以具有平均粒子直徑(D一為2 至50微米,厚度0.1至5微米之金屬顏料為佳。此外,具有 平均粒子直徑於1〇至35微米範圍之金屬顏料之光澤外觀絕 佳故適合使用。前述塗料中金屬顏料之顏料濃度(pwc)通 20常為20.0%重量比或以下。濃度較佳為〇.〇1至18.0%重量比 ,以及更佳為0.1至15.0%重量比。當金屬顏料之含量Z過 20·〇%重量比時,塗膜外觀下降。 前述金屬顏料例如包括金屬或合金如鋁、銅、辞、鐵 、鎳、錫及氧化銘及其混合物等金屬或合金之纟經著色或 22 200427795 經著色之金屬金屬顏料。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結 合使用。 塗料中,金屬顏料及全部其它顏料之總顏料濃度(PWC) 5 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。 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 10 劑,可含有對前述中間塗料舉例說明之流變劑。 除了前述成分外,通常添加於塗料之添加劑例如表面 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。其攙混量係於熟諳技藝 人士已知之範圍。 15 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 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。 20 透明塗膜 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。 23 200427795 由透明度及對酸蝕刻之耐性而言,溶液型透明塗料較 佳例如包括丙稀酸系樹脂及/或聚醋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 5 樹脂。 此外,水性型透明塗料例如包括含有樹脂之塗料,該 塗料係經由使用鹼中和前述範例溶液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。 10 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 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 15 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 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 20 添加流變劑至透明塗料。至於流變劑,通常含有具觸變性 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 24 200427795 本發明之經塗覆之薄膜形成方法較佳用於各種基材, 例如金屬、塑膠、發泡材料等,特別金屬表面及鑄造物件 。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。 5 前述金屬產物例如包括鐵、銅、铭、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 等預先接受化學處理之金屬。 此外,於用於本發明之金屬塗覆膜形成方法之基材, 10 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,該塗料可獲得絕佳防蝕性 之塗膜。 塗覆膜形成方法 15 於本發明之經塗覆之薄膜形成方法,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基材 上。 當汽車車體塗覆以根據本發明之中間塗料時,為了提 20 升外觀,薄膜可經由多階段式塗覆較佳為藉空氣靜電喷塗 之2階段式塗覆形成;或經由使用旋轉霧化靜電塗覆機[稱 作為「微微貝機(// // (micro micro) bel)」、「微貝機(// (micro) bel)」或「美它貝機(metabel」]形成。 本發明之中間塗料所形成之乾塗膜厚度依據預定用途 25 200427795 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 如不均勻及凹陷等缺點;而當厚度低於下限時,表面可能 被遮蓋而發生不均勻塗層。 5 於本發明之經塗覆之薄膜形成方法,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。 用以於本發明方法形成底塗膜之底塗料可藉靜電噴塗 ,或使用如美它貝機、微微貝機、微貝機等旋轉霧化靜電 10塗覆機塗覆。塗膜之乾厚度設定為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)。 於本發明之塗膜形成方法,當底塗膜形成後,含有底 15塗膜及金屬顏料所致之不規則時,形成透明塗膜, 經由遮 蓋由不規則所產生之凸部來保護塗膜。至於塗覆方法,較 传係使用刚述疑轉霧化靜電塗覆機如微微貝機、微貝機等 形成薄膜。 由透明塗料形成之透明塗膜之乾厚度較佳為約1〇微米 ^矣8〇微米,及更佳為約20微米至6G微米。當厚度超過上限 時,某些惝况下出現爆開及凹陷等缺陷 。當厚度低於下限 0彳,影像銳度降低。 如此所付經塗覆之複合薄膜藉同時硬化接受塗膜的形 成’亦即所明之二塗膜_次烤乾。此種情況下,可刪除中 26 ^υυ427795 < 、二用之烤爐及乾燥爐,故由經濟與環保觀點為較佳。 仁。亥方法要求所謂之賴,預熱步驟為介於塗覆步驟間以 …、及風去除濕膜之揮發性材料之步驟。例如可於40°C至 1〇〇 c加熱約1至5分鐘時間。 、、二由將經塗覆之複合薄膜硬化溫度設定於10 0 °c至18 0 C ’且較佳13(rc至160°C,可獲得有高度交聯度之硬化塗 膜。當溫度高於上限時,塗膜變硬及變脆。#溫度低於下 限呤’硬化不足。硬化時間隨硬化溫度改變,但適合於130 °C至160。(:硬化1〇至30分鐘。 本發明形成之經塗覆之複合薄膜之膜厚度通常為3〇至 300微米,且較佳為5〇至25〇微米。當超過上限時,薄膜性 質(如溫度週期試驗等性質)降低。當低於下限時,薄膜強度 降低。 根據本發明,即使經塗覆之複合薄膜係藉三塗膜一次 15烤乾方法形成,該方法包含依次以濕於濕方式形成中間塗 膜、底塗膜及透明塗膜,以及隨後一次硬化塗膜,仍可獲 得耐切晶片效能及塗膜外觀絕佳之經塗覆之複合薄膜。 本發明之中間塗覆塗料組成可對切晶片時的衝擊提供 斥力,且具有可將衝擊能轉換成為熱能給塗層之性質。如 2〇 此,經由本發明所得之經塗覆之複合薄膜具有絕佳耐切晶 片性質,即使於接受到嚴重衝擊時只顯示小的剝離區且較 少出現剝離。 本發明之經塗覆之複合薄膜形成方法包括以濕於濕方 式依次形成中間塗膜、底塗膜及透明塗膜,由於可免除中 27 200427795 間塗膜之烤乾烘箱步驟,故就麟與環㈣㈣言為絕佳 。如此’本發明對所得經塗覆之複合薄膜提供多項優點, 例如对切晶片性質絕佳,物理性質加強以及外觀良好。 實施例 5 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 以胺基甲酸酯改性之聚酯樹脂(a)之製備 10 440份間苯二甲酸,20份六氫鄰笨二甲酸,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、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0.2份二丁基氧化錫,開始攪拌,反應 15層溫度由180°C徐緩升高至220°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行縮 合反應。當樹脂酸價達1〇毫克KOH/克時,材料冷卻至100 °C,以30分鐘時間徐緩添加1〇〇份六亞甲基二異氰酸酯。此 20 外,溫度維持1小時,添加200份二甲苯及200份乙酸丁酯, 獲得以胺基甲酸酯改性之聚酯樹脂,具有固型物含量70% ,平均分子量2〇〇〇,酸價8毫克KOH/克’ Μ基值120及樹脂 Tg 60〇C。 製備例2 28 200427795 聚烯烴彈性體(b-l)之製備 650份α,ω-氫化聚丁二烯二醇(「Gi-i〇〇〇」,日本曹打 公司製造)及650份甲苯置於適當反應容器内,反應容器裝 配有溫度計、攪拌器、冷卻管、氮氣導入管及添加漏斗, 5 溫度升向至5 〇 C。反應谷器内以1小時時間逐滴加入%份異 佛爾酮二異氰酸酯及96份甲苯溶液,溫度維持於5〇。〇 1小時 。然後反應容器溫度升高至85°C,以1小時時間逐滴加入56份 甲基丙沐酸經基乙S曰及56份甲笨溶液,於8維持1小時,冷 卻獲得以聚烯烴為主之巨單體溶液(固型物含量5〇%)。 10 25.6份以聚稀烴為主之聚單體溶液及83.2份曱苯置於 適當反應容器’溫度升高至110°C。另外,將20.0份丙烯酸 丁酯、29.0份甲基丙烯酸丁酯、2.2份甲基丙烯酸經基丁酯 及1.5份己酸第三丁基過氧基-2-乙酯混合獲得溶液,以3小 時時間逐滴添加至反應容器,同時授拌其内部。隨後反應 15 容器於110°C維持30分鐘。以30分鐘時間逐滴加入0.5份己酸 第三丁基過氧基-2-乙酯及5.0份甲苯之溶液。持續擾拌90分 鐘後,材料經冷卻獲得聚烯烴彈性體(b-l)溶液(固型物含量 40%) 所得聚烯烴彈性體(M)具有物理性質數據:數目平均 20 分子量20,000及羥基值20。 製備例3 聚烯烴彈性體(b-2)之製備 650份α,ω-氫化聚丁二烯二醇(「GI-i〇〇〇」,日本曹打 公司製造),692.1份甲苯及42.1份順丁烯二酐置於適當反應 29 200427795system. Metal pigments can be colored. For example, a metal pigment having an average particle diameter (D1 is 2 to 50 micrometers and a thickness of 0.1 to 5 micrometers is preferred. In addition, a metal pigment having an average particle diameter in the range of 10 to 35 micrometers is excellent in gloss appearance and is suitable for use. The pigment concentration (pwc) of the metallic pigment in the aforementioned coating is usually 20% by weight or less. The concentration is preferably from 0.01 to 18.0% by weight, and more preferably from 0.1 to 15.0% by weight. When metal When the content of the pigment Z exceeds 20.0% by weight, the appearance of the coating film decreases. The aforementioned metallic pigments include, for example, metals or alloys such as aluminum, copper, copper, iron, nickel, tin, and oxides and mixtures thereof. Tinted or 22 200427795 Tinted metallic pigments. In addition, interference mica pigments, muscovite pigments, graphite pigments, and other pigmented or uncolored flake pigments can also be used in combination. In coatings, metallic pigments and all other pigments The total pigment concentration (PWC) 5 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. Besides As in the intermediate coating, in order to maintain the coating workability, it is preferable to add a rheological agent to the base coating. The rheological agent is used to form a coating film without unevenness and depression, and usually contains a chemical agent having thixotropic properties. 10 kinds of rheological agent, which may contain the rheological agent exemplified for the aforementioned intermediate coating. In addition to the foregoing components, additives such as surface modifiers, rheological agents, antioxidants, ultraviolet light inhibitors and defoaming agents usually added to coatings It can also be blended with the primer used in the present invention. The blending amount is within the range known to those skilled in the art. 15 The base coating used in the present invention has a total solid content of 10 to 60% by weight when applied. It is preferably 15 to 50% by weight. When the content is higher than the upper limit or lower than the lower limit, 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 In order to form a transparent coating film, a transparent coating is used. The transparent coating is not particularly limited, but it can be used with film-forming heat. Transparent coatings for resins and hardeners. As for transparent coatings, such as solution type, water-based type and powder type. 23 200427795 In terms of transparency and resistance to acid etching, solution type transparent coatings preferably include acrylic resins. And / or a combination of a polyester resin and an amine resin, an acrylic resin and / or a combination of a polyester resin and an isocyanate compound, and an acrylic resin and / or a polyester 5 resin having a carboxylic acid-epoxy curing system. Water-based transparent coatings include, for example, resin-containing coatings, which are obtained by neutralizing the film-forming resin of the aforementioned exemplary solution-type transparent coatings with an alkali, and are not easily water-based. Neutralization can be added before or after polymerization by adding Tertiary amines such as dimethylethanolamine and triethylamine are carried out. 10 Conversely, as the powder type clear coating, conventional powder coatings such as thermoplastic powder coatings and thermosetting powder coatings 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, powder transparent coatings mainly composed of epoxy resins, acrylics and polyester resins, but powder transparent coatings based on acrylics 15 which have better weather resistance are special good. As for the powder-type transparent coating used in the present invention, since it does not contain volatile substances when hardened, it can obtain better appearance and rarely yellowing, so it is based on epoxy resin containing acrylic resin / polyvalent carboxylic acid-based powder coating. Especially good. In addition, as with intermediate coatings, in order to maintain coating workability, it is preferred to add a rheological agent to the clear coating. As for rheological agents, they usually contain chemicals with thixotropic properties. 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 24 200427795 The coated film forming method of the present invention is preferably used for various substrates, such as metal, plastic, foamed materials, etc., especially metal surfaces and castings. Metals and shaped articles are preferred. This method is particularly suitable for metal products that can be coated with cations. 5 The aforementioned metal products include, for example, iron, copper, metal, 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 in advance with phosphates, chromates, and the like. In addition, in the substrate used in the method for forming a metal coating film of the present invention, the electrodeposition coating film can be formed on a chemically-treated steel sheet. As for the electrodeposition coating for forming an electrodeposition coating film, a cationic or anionic type can be used, and a cationic electrodeposition coating composition is preferable, and the coating can obtain a coating film with excellent corrosion resistance. Coating film forming method 15 In the coated thin film forming method of the present invention, the intermediate coating film is formed by the intermediate coating, the base coating film is formed by the base coating, and the transparent coating film is formed by the transparent coating. Formed successively on a substrate in a wet-on-wet manner. When the car body is coated with the intermediate coating according to the present invention, in order to improve the appearance of 20 liters, the film may be formed by multi-stage coating, preferably 2-stage coating by air electrostatic spraying; or by using a rotating mist Electrostatic coating machine [referred to as "micro micro-belt machine (// // (micro micro) bel)", "micro-belt machine (/ (micro) bel)" or "metabel machine (metabel") is formed. The thickness of the dry coating film formed by the intermediate coating of the present invention varies according to the intended use 25 200427795. In many cases, a thickness of 10 microns to 60 microns can be used. When the thickness exceeds the upper limit, the sharpness of the image decreases, and in some cases the Layers have disadvantages such as unevenness and depression; and when the thickness is below the lower limit, the surface may be covered and uneven coating may occur. 5 In the coated film forming method of the present invention, the primer and transparent coating are wet The application method is applied on the unhardened intermediate coating film to form a base coating film and a transparent coating film. The base coating used to form the base coating film in the method of the present invention can be electrostatic sprayed, or a Rutabex machine can be used. , Pico shell machine, pico shell machine, etc. Rotary atomizing electrostatic 10 coater coating. The dry thickness of the coating film is set to 5 to 35 micrometers, and preferably 7 to 25 micrometers. When the thickness of the base coating film exceeds 35 micrometers, the sharpness of the image decreases, in some cases Unevenness or dents appear under the surface. When the thickness is less than 5 micrometers, the surface covering properties are insufficient, and occasionally a non-uniform coating (discontinuous film state) appears. In the coating film forming method of the present invention, when the base coating film is formed, it contains a base 15 When the coating film and the metal pigment are irregular, a transparent coating film is formed, and the coating film is protected by covering the raised portions caused by the irregularity. As for the coating method, the newly described suspicious atomization electrostatic coating is more widely used. Coating machines such as picoshell machines, microshell machines, etc. form thin films. The dry thickness of the transparent coating film formed by the transparent coating is preferably about 10 microns to about 80 microns, and more preferably about 20 microns to 6G microns. When When the thickness exceeds the upper limit, defects such as bursting and dents appear under certain conditions. When the thickness is lower than the lower limit of 0 °, the sharpness of the image is reduced. The coated composite film thus paid receives the formation of the coating film by hardening at the same time. That is the second coating film In this case, 26 ^ υυ427795 < and two-use ovens and drying ovens can be deleted, so it is better from an economic and environmental perspective. Ren. Hai method requires the so-called reliance, the preheating step is between coating The step of removing the volatile material of the wet film with wind between the steps. For example, it can be heated at 40 ° C to 100c for about 1 to 5 minutes. The hardening temperature of the coated composite film Set at 10 0 ° C to 18 0 C 'and preferably 13 (rc to 160 ° C, a hardened coating film with a high degree of crosslinking can be obtained. When the temperature is higher than the upper limit, the coating film becomes hard and brittle. # The temperature is below the lower limit, the sclerosis is insufficient. The hardening time varies with the hardening temperature, but is suitable for 130 ° C to 160. (: Hardened for 10 to 30 minutes. The film thickness of the coated composite film formed by the present invention is usually 30 to 300 microns, and preferably 50 to 25 microns. When the upper limit is exceeded, the film properties (such as Properties such as temperature cycle test) decrease. When the lower limit is lowered, the film strength decreases. According to the present invention, even if the coated composite film is formed by the three coating film drying method at a time, the method includes sequentially wet-wet method Forming the intermediate coating film, the base coating film and the transparent coating film, and then curing the coating film once, can still obtain a coated composite film with excellent chip resistance and coating film appearance. The intermediate coating coating composition of the present invention can The impact when dicing the wafer provides repulsive force and has the property of converting the impact energy into thermal energy to the coating. As such, the coated composite film obtained by the present invention has excellent dicing wafer resistance properties, even after receiving Under severe impact, only a small peeling area is displayed and peeling is less likely to occur. The coated composite film forming method of the present invention includes sequentially forming an intermediate coating film, a base coating film, and Bright coating film, because the baking drying oven step of 27 200427795 coating films can be eliminated, it is very good to say Lin and Huan. In this way, the present invention provides a number of advantages for the obtained coated composite film, such as dicing wafers Excellent properties, enhanced physical properties and good appearance. Example 5 The present invention will be described in detail in the following examples, but the present invention is by no means limited to these examples. The "parts" and "percentages" in the following are based on Preparation Example 1 Preparation of urethane-modified polyester resin (a) 10 440 parts of isophthalic acid, 20 parts of hexahydroophthalic acid, 40 parts of azelaic acid, 300 parts of trihydroxy Methylpropane and 200 parts of neopentyl glycol are placed in a 2 liter reaction vessel; the reaction vessel is equipped with a nitrogen introduction tube, a stirrer, a temperature regulator, an addition funnel, and a cooling tube equipped with a decanter; when the raw materials are dissolved by heating When it becomes stirable, add 0.2 parts of dibutyltin oxide and start stirring. The temperature of the 15 layers of reaction is gradually increased from 180 ° C to 220 ° C for 3 hours. The condensation water produced is removed by distillation of the system. When the temperature reaches 220 ° C, maintain this temperature 1 hour, slowly add 20 parts of xylene to the reaction layer, allowing the condensation reaction in the presence of a solvent. When the resin acid value reaches 10 mg KOH / g, the material is cooled to 100 ° C, and slowly added 1 in 30 minutes. 〇part of hexamethylene diisocyanate. In addition, the temperature was maintained for 1 hour, 200 parts of xylene and 200 parts of butyl acetate were added to obtain a urethane-modified polyester resin having a solid content of 70. %, Average molecular weight 2000, acid value 8 mg KOH / g 'M group value 120 and resin Tg 60 ° C. Preparation Example 2 28 200427795 Preparation of polyolefin elastomer (bl) 650 parts of α, ω-hydrogenated polymer Butadiene glycol ("Gi-io00", manufactured by Soda Corporation, Japan) and 650 parts of toluene were placed in a suitable reaction vessel. The reaction vessel was equipped with a thermometer, stirrer, cooling tube, nitrogen introduction tube, and addition funnel. , 5 The temperature rose to 50 ° C. In the reaction trough, 1% of isophorone diisocyanate and 96 parts of toluene solution were added dropwise over a period of 1 hour, and the temperature was maintained at 50. 〇 1 hour. Then the temperature of the reaction vessel was raised to 85 ° C, 56 parts of methyl propionate and 56 parts of methylbenzyl solution were added dropwise over 1 hour, and maintained at 8 for 1 hour. Cooling to obtain mainly polyolefin Macromonomer solution (solid content 50%). 10 25.6 parts of a monomer solution mainly composed of polyhydrocarbons and 83.2 parts of toluene were placed in a suitable reaction vessel 'and the temperature was raised to 110 ° C. In addition, 20.0 parts of butyl acrylate, 29.0 parts of butyl methacrylate, 2.2 parts of methacrylic acid via butyl acrylate, and 1.5 parts of butyl peroxy-2-ethylhexanoate were mixed to obtain a solution, and the solution was allowed to stand for 3 hours. Time was added dropwise to the reaction vessel while stirring the inside thereof. Subsequently, the reaction vessel was maintained at 110 ° C for 30 minutes. A solution of 0.5 part of tert-butylperoxy-2-ethylhexanoate and 5.0 parts of toluene was added dropwise over a period of 30 minutes. After continuous stirring for 90 minutes, the material was cooled to obtain a polyolefin elastomer (b-1) solution (solid content 40%). The obtained polyolefin elastomer (M) had physical property data: number average 20, molecular weight 20,000, and hydroxyl value 20. Preparation Example 3 Preparation of Polyolefin Elastomer (b-2) 650 parts of α, ω-hydrogenated polybutadiene glycol ("GI-i0000", manufactured by Soda Corporation, Japan), 692.1 parts of toluene and 42.1 parts Maleic anhydride placed in the appropriate reaction 29 200427795
容器’反應容器裝配有溫度計、攪拌器、冷卻管、 入管及添加漏斗。反應容器經加壓,升高至130°C。 度至FT-IR測得酸酐之畸峰(1780厘米-1)消失為止; ’材料經冷卻獲得以聚烯烴為主之巨單體溶液(固型物含量 50%) 〇Vessel 'The reaction vessel is equipped with a thermometer, a stirrer, a cooling tube, an inlet tube and an addition funnel. The reaction vessel was pressurized and raised to 130 ° C. Degree until the abnormal peak of acid anhydride (1780 cm-1) measured by FT-IR disappears; ′ The material is cooled to obtain a polyolefin-based macromonomer solution (solid content 50%).
102.9份以聚烯烴為主之聚單體及丨〇3.〇份甲笨置於適 當反應容器’溫度升高至ll〇°C。另外,將9.3份丙烯酸丁酉旨 、10.0份甲基丙烯酸丁酯、10.0份順丁烯二酸、9.0份丙稀 酸羥基乙酯、10.0甲基丙烯酸羥基丁酯、3.2份甲基丙稀酸 10 及1·5份己酸第三丁基過氧基-2-乙酯混合獲得溶液,以3小 時時間逐滴添加至反應容器,同時攪拌其内部。隨後反應 容器於110°C維持30分鐘。於其中以30分鐘時間逐滴添加〇 5 份己酸第三丁基過氧基-2-乙酯及5.0份甲苯之溶液。持續搜 拌90分鐘後,材料經冷卻獲得聚烯烴彈性體(b-2)溶液(固型 15 物含量40%)102.9 parts of polyolefin-based comonomer and 0.30 parts of methylbenzyl were placed in a suitable reaction vessel 'and the temperature was raised to 110 ° C. In addition, 9.3 parts of butyl acrylate, 10.0 parts of butyl methacrylate, 10.0 parts of maleic acid, 9.0 parts of hydroxyethyl acrylate, 10.0 hydroxybutyl methacrylate, 3.2 parts of methacrylic acid 10 It was mixed with 1.5 parts of tert-butylperoxy-2-ethyl hexanoate to obtain a solution, which was added dropwise to the reaction container over a period of 3 hours while stirring the inside. The reaction vessel was then maintained at 110 ° C for 30 minutes. A solution of 05 parts of tert-butylperoxy-2-ethylhexanoate and 5.0 parts of toluene was added dropwise thereto over a period of 30 minutes. After continued searching for 90 minutes, the material was cooled to obtain a polyolefin elastomer (b-2) solution (solid content: 40%)
所得聚烯烴彈性體(b-2)具有下列性質··數目平均分子 量40000,經基值1〇〇及酸價2〇毫克κοΗ/克。 製備例4 非水性分散液之製備 20 (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 冷凝器之容器。然後20份溶液具組成如後: 30 200427795 [表2] 甲基丙烯酸甲酯 38.9 份 甲基丙烯酸硬脂酯 38.8 份 丙烯酸2-羥基乙酯 22.3 份 偶氮貳異丁腈 5.0份 添加至其中,藉加熱、攪拌升高溫度。85份其餘混合 溶液於110°C逐滴添加3小時,然後以30分鐘時間逐滴添加 5 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 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 10 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 及控溫器。然後具如下組成之溶液: [表3] 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 15 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 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 31 200427795 徑180奈米。此種非水性分散液樹脂具有Tg 23°C,經基值 162及SP值11·8 ;殼部為分散液穩定樹脂與本全體非水性分 散液樹脂之SP值差異為2.3。 實施例1 5 中間塗料1 14_3份先前製備例1所得之以胺基甲酸酯改性之聚酯 樹脂,1,500份BOR-904(聚烯烴彈性體,沙凱(sakai)化學工 業公司製造,乙烯/丙烯共聚物,固型物含量10%,酸價4 毫克KOH/克),66.7份杜蘭内特(Duranate) MF-K60X(嵌段異 10 氫酸酯,旭化學工業公司製造,固型物含量60%,95份 CR-97(氧化鈦,石原產業公司製造),5份MA-100(碳黑顏料 ,三菱化學公司製造)及〇·1份迪斯巴隆(Disparon) 4200-20( 抗沉降劑,楠本(Kusumoto)化學公司製造)置於1升容器,使 用分散機混合,加入與混合物等重之GB503M(粒子直徑1.6 15 毫米之玻璃珠),使用桌上型SG磨機於室溫分散2小時。分 散完成時使用研磨計測得粒徑為5微米或以下。過濾去除玻 璃珠,獲得中間塗料。此塗料使用4號福特杯,以甲苯/史 瓦卓(Swazole)-100(芳香族烴溶劑,艾克森公司製造)=1/1混 合溶劑稀釋成20秒/20°C。稀釋後塗料之固型物含量為25% 20 ,顏料濃度(PWC)為50%。 底塗料 以丙烯醯基蜜胺為主之金屬底顏料「歐加(Orga) TO H600 1幻綠金屬」(日本塗料公司製造)使用3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)之 32 匕。口稀釋至17#、/2(rc。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 5 、酉文〖生^氧樹月曰硬化為主之透明塗料「馬克(Mack) ^ 〇〇透明」(日本塗料公司製造)使用4號福特杯,以丙酸 氧基乙酉曰/S」〇〇(芳香族烴溶劑,艾克森公司製造)稀釋成 %秒/2〇t。塗料施用時之非揮發物含量為鄕。此外,沉 積時之非揮發物含量為61〇/〇。 經塗覆之薄膜形成方法 1〇 陽離子性電沉積塗料「包爾托普(Power Top) V-20」( 曰,本塗料公司製造)電沉積塗覆於SPC鋼板上,鋼板厚0 8毫 只長3〇厘米,覓10厘米,已經使用鱗酸辞處理,經電沉 積塗覆而形成塗膜,具有乾膜厚度2〇微米,接著於⑽。◦烤 乾3〇刀4里。然後此塗覆板黏著至移動本體,於移動當中, 15使用「微貝機」(旋轉霧化型靜電塗覆機)塗覆以前述中間塗 料。乾膜厚度變成20微米,於施用後以1〇分鐘時間固化。 然後,前述底塗料分二階段使用「微貝機」及「美它 貝機」於2階段施用,乾膜厚度變成15微米。兩次施用間間 隔時間2.5分鐘。第二次施用後,固化8分鐘。然後前述透 20明塗料於1階段使用「微貝機」塗覆,乾膜厚度變成35微米 ’進行7分鐘固化。然後所得塗覆板於140°C乾燥器内烤乾 3 0分鐘。 薄膜評比方法 有關所得塗覆板,使用WS-DOI(薄膜外觀測量裝置, 33 200427795 別克(Bick)化學公司製造)。評比經塗覆之複八 双。磚膜外觀。 藉WS-DOI,評比塗膜外觀,特別光澤外觀之評比以^值 表示。隨著Wa值的變小,出現光澤外觀,而外 I規較佳。 此外,所得塗覆板之耐切晶片性質評比如後使用葛 拉貝羅(glabero)測試器(蘇加(Suga)測試儀器公司制生)3⑼ 塊7號碎石由35厘米距離,以空氣壓力3.0千克力/平方厘米 以45度角度碰撞薄膜。以水洗滌及乾燥後,使用尸大委 (Nichiban)公司製造之工業用黏膠帶進行剝離气 4驗,隨後就 玻璃直徑及玻璃數以肉眼觀察及評比剝離程度。 ίο 中間塗膜之伸長率評比如後:中間塗料施用 也用於厚3毫米 之聚丙烯板,乾膜厚度變成40至60微米,進耔m 咬仃固化約2〇分 鐘,接著於140°C烤乾20分鐘。所得薄膜切割成有饮部、 成長5厘米X寬1厘米,由聚丙烯板上剝離來形成〜種刀又 承體之自由態薄膜。有關此自由態薄膜,使用知丄、S支 15 力須彳試器( 「Tensilon」,妥有伯温(Toyo Boldwin)公司製造)以杈 、 率10毫米/分鐘於20°C環境下測定伸長率。 ^ 前述結果顯示於表4 實施例2 中間塗料2 20 28.6份先前製備例1所得之以胺基甲酸酯改性之^ 樹脂,148份PP-2001(以聚丙烯為主之彈性體,3 A , 曰 一开化學公 司製造,固型物含量27%、酸價6.6毫克KOH/克,輕基值13 ,16.7份U-128(蜜胺樹脂,三井西鐵克(Sitec)公司製& 型物含量60%),33·3份MF-K60X(活性亞甲基型嵌段里& 34 200427795 酯’旭化學工業公司製造,固型物含量60%),25份先前製 備例4所得之非水性分散液,39.2份CR-97(氧化鈦,石原產 業公司製造),2.9份MA-100(碳黑顏料,三菱化學公司製造 )’ 〇·1份迪斯巴隆4200-20(抗沉降劑,楠本化學公司製造) 5 及0.W*LMS-300(滑石,富士滑石公司製造)置於1升容器内 ’使用分散機混合,加入與混合物等重之GB503M(具有粒 子直徑1.6毫米之玻璃珠),使用桌上型sG磨機於室溫分散2 小0寸°分散完成時使用研磨計測得粒徑為5微米或以下。過 濾去除玻璃珠,獲得中間塗料。此塗料使用4號福特杯,以 10曱笨/史瓦卓-100(芳香族烴溶劑,艾克森公司製造)=1/i混合 /谷劑稀釋成20秒/20。(3。稀釋後塗料之固型物含量為46%, 顏料濃度(PWC)為30%。 根據實施例1之相同方式,但使用前述中間塗料2來替 代中間塗料1,製備經塗覆之複合薄膜且如前文說明評比。 15 結果顯不於表4。 實施例3 中間塗料3 4.3份先前製備例丨所得之以胺基甲酸酯改性之聚酯樹 脂,125份先前製備例2所得之聚烯烴彈性體(bj),66.7份 20 MF_K6〇x(嵌段異氰酸酯,旭化學工業公司製造),固型物 60/。)’ 95伤CR-97(氧化鈦,石原產業公司製造),9份嫩_1〇〇( 碳黑顏料,三菱化學公司製造)及W份迪斯巴隆4跡2〇(抗 沉降劑,楠本化學公司製造)置於咔容㈣,以類似實施 例1中間塗料1之方式製備顏料。所得稀釋後塗料之固型物 35 200427795 含量為51%,以及塗料之顏料濃度(PWC)為5〇%。 根據實施例1之相同方式’但使用前述中間塗料3來替 代中間塗料3,製備經塗覆之複合薄膜且以類似方式評比。 結果顯示於表4。 5 實施例4 中間塗料4 28.6份先前製備例1所得之以胺基甲酸酯改性之聚酯 樹脂,99.9份先前製備例3所得之聚稀烴彈性體(b-2),16.7 份U-128(蜜胺樹脂,三井西鐵克公司製造,固型物含量60%) 1〇 ,33.3份MF-K60X(活性亞甲基型嵌段異氰酸酯,旭化學工 業公司製造,固型物含量60%) ’ 25份先前製備例4所得之非 水性分散液,39.2份CR-97(氧化鈦,石原產業公司製造), 2.9份MA-100(碳黑顏料,三菱化學公司製造),0.1份迪斯巴 隆4200-20(抗沉降劑,楠本化學公司製造)及0.8份LMS-300( 15 滑石,富士滑石公司製造)置於1升容器内,以類似實施2中 間塗料2之方式製備塗料。稀釋後塗料之固型物含量為45% ,顏料濃度(PWC)為30%。 根據實施例1之相同方式,但使用前述中間塗料2來替 代中間塗料4,製備經塗覆之複合薄膜且以類似方式評比。 2〇 結果顯示於表4。 比較例1 中間塗料5 107份先前製備例1所得之以胺基甲酸酯改性之聚酯樹 脂清漆,280份CR-97(石原產業公司製造之氧化鈦),13份 36 200427795 MA-100(碳黑顏料,三菱化學公司製造),7份MS-100(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升容器及使用分散器混合,放置與進料總量等量之 GB503M(粒子直徑1·6毫米之玻璃珠),材料於室溫使用桌上 5 型SG磨機分散3小時獲得灰色顏料糊。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 。於100份此顏料糊内加入24份製備例1之以胺基甲酸酯改 性之聚醋樹脂⑷,24份MF-K60X(活性亞甲基型嵌段異氰酸 酯,旭化學工業公司製造,固型物含量60%),及24份 10 U-20N60(蜜胺樹脂,三井西鐵克公司製造,固型物含量60%) 。於其中加入丙酸乙氧基乙酯/S-100(芳香族烴溶劑,艾克 森公司製造)=1/1之混合溶劑,材料使用4號福特杯稀釋成19 秒/20°C。稀釋後塗料之固型物含量為49%,以及塗料之顏 料濃度(PWC)為30%。 15 根據實施例1之相同方式,但使用前述中間塗料2來替 代中間塗料5,製備經塗覆之複合薄膜且以類似方式評比。 結果顯示於表4。 比較例2 CP-101(切晶片底劑,日本塗料公司製造)喷塗於已經 20經過電沉積塗覆及烤乾硬化的鋼板上,具有薄膜厚度5微米 ,隨後使用比較例1使用中間塗料5形成塗覆膜。固化5分鐘 後,使用比較例1所述之中間塗料5形成中間塗膜。然後使用 實施例冰述之相同底塗料及透明塗料,如同實施例i製備經 塗覆之複合賴’且以類似方式評比。結果顯示於表4。 37 200427795 [表4] 實施例1 實施例2 實施例3 實施例4 比較例1 比較例2 外觀之評比(Wa值) 25 21 21 19 21 29 而于切晶片 剝離直徑 (毫米) 1.5 1.5 1.2 1.2 2.0 1.5 剝離數目 (塊) 10 8 10 9 20 10 中間塗膜 伸長率(%) 70 100 80 100 30 30 I:圖式簡單說明】 (無) 鲁 5 【圖式之主要元件代表符號表】 (無)The obtained polyolefin elastomer (b-2) had the following properties: a number average molecular weight of 40,000, a base value of 100, and an acid value of 20 mg κοκ / g. Preparation Example 4 Preparation of Non-Aqueous Dispersion Liquid 20 (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 condenser. Then 20 parts of the solution had the following composition: 30 200427795 [Table 2] 38.9 parts of methyl methacrylate, 38.8 parts of stearyl methacrylate, 38.8 parts of 2-hydroxyethyl acrylate, 22.3 parts of azoisobutyronitrile, 5.0 parts were added thereto, Increase the temperature by heating and stirring. 85 parts of the remaining mixed solution was added dropwise at 110 ° C for 3 hours, and then 5 0.5 parts 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 10 90 parts of butyl acetate and 60 parts (a) Preparation of dispersion resin stabilized acrylic resin, placed in a container, the container is equipped with a stirrer, condenser and temperature controller . Then a solution with the following composition: [Table 3] 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 15 Add dropwise at 100 ° C for 3 hours, and then add 0.1 part of azobisisobutyronitrile and 1 part of butyl acetate solution dropwise over 30 minutes. The reaction solution was continuously stirred for 1 hour to obtain an emulsion having 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 particles with a diameter of 31 200427795 and a diameter of 180 nm. This non-aqueous dispersion resin has a Tg of 23 ° C, a base 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 overall non-aqueous dispersion resin is 2.3. Example 1 5 Intermediate paint 1 14-3 parts of urethane-modified polyester resin obtained in the previous Preparation Example 1, 1,500 parts of BOR-904 (polyolefin elastomer, manufactured by Sakai Chemical Industry Company) , Ethylene / propylene copolymer, solid content 10%, acid value 4 mg KOH / g), 66.7 parts Duranate MF-K60X (block iso 10 hydrochloride, manufactured by Asahi Chemical Industry Co., Ltd., 60% solid content, 95 parts CR-97 (titanium oxide, manufactured by Ishihara Industries), 5 parts MA-100 (carbon black pigment, manufactured by Mitsubishi Chemical Corporation), and 0.1 part Disparon 4200 -20 (anti-settling agent, manufactured by Kusumoto Chemical Co., Ltd.) was placed in a 1 liter container, mixed with a disperser, and GB503M (glass beads with a particle diameter of 1.6 15 mm) equal to the weight of the mixture was added, and a desktop SG mill was used. The machine disperses at room temperature for 2 hours. When the dispersion is completed, the particle size measured by a grinder is 5 microns or less. The glass beads are filtered to remove the intermediate coating. This coating uses a No. 4 Ford cup with toluene / Swazole- 100 (aromatic hydrocarbon solvent, manufactured by Exxon) = 1/1 mixed solvent diluted to 20 seconds / 20 ° C The solid content of the diluted coating is 25% 20 and the pigment concentration (PWC) is 50%. The base coating is based on acryl melamine-based metal base pigment "Orga TO H600 1 Magic Green Metal" ( Nihon Paint Co., Ltd.) uses a No. 3 Ford cup with 32 daggers of ethoxyethyl propionate / S-100 (aromatic hydrocarbon solvent, manufactured by Exxon Corporation). The mouth is diluted to 17 #, / 2 (rc. The non-volatile content when the coating is applied is 31%. The non-volatile content when it is deposited is 65%. Transparent coatings 5, transparent text [Original ^ oxygen tree month hardening-based transparent coating "Mack" ^ 〇〇 "Transparency" (manufactured by Japan Coatings Co., Ltd.) uses No. 4 Ford Cup, diluted with acetoxy propionate / S "00 (aromatic hydrocarbon solvent, manufactured by Exxon Corporation) to% sec / 20t. When coating is applied The non-volatile matter content is 此外. In addition, the non-volatile matter content at the time of deposition is 61/0. Coated film formation method 10 Cationic electrodeposition coating "Power Top V-20" (Say, manufactured by this coating company) Electrodeposition coating on SPC steel plate, the thickness of the steel plate is 0.8 mm, the length is 30 cm, and the length is 10 cm. It is treated with scaly acid, and is coated by electrodeposition to form a coating film with a dry film thickness of 20 micrometers, followed by ⑽. ◦ Bake and dry for 30 knives and 4 miles. Then the coating plate is adhered to the moving body and is moving. 15 Using a "micro-shell machine" (rotary atomizing electrostatic coating machine) to coat the aforementioned intermediate coating. The dry film thickness became 20 microns, and it was cured in 10 minutes after application. Then, the aforementioned primer was divided into two stages Using the "micro shell machine" and "meta shell machine" in two stages, the dry film thickness became 15 microns. The interval between the two applications was 2.5 minutes. After the second application, it was cured for 8 minutes. Then, the above-mentioned transparent coating was coated with a "micro-shell machine" in one stage, and the dry film thickness was changed to 35 micrometers' for 7 minutes for curing. The resulting coated plate was then dried in a dryer at 140 ° C for 30 minutes. Thin film evaluation method For the obtained coated plate, WS-DOI (thin film appearance measuring device, 33 200427795 manufactured by Bick Chemical Co., Ltd.) was used. Compare the coated eight pairs. Brick film appearance. By WS-DOI, the evaluation of the appearance of the coating film, especially the appearance of the gloss, is expressed by ^ value. As the Wa value becomes smaller, a glossy appearance appears, and the outer I gauge is better. In addition, the cut-resistant wafer properties of the obtained coated plate were evaluated by using a glabero tester (produced by Suga Testing Instrument Co., Ltd.) 3⑼ pieces of No. 7 crushed stone from a distance of 35 cm and an air pressure of 3.0 Kgf / cm2 impacted the film at an angle of 45 degrees. After washing with water and drying, peeling gas was examined using an industrial adhesive tape manufactured by Nichiban, and then the diameter and number of glass were visually observed and evaluated for the degree of peeling. ίο The evaluation of the elongation of the intermediate coating film is as follows: the application of the intermediate coating is also used for polypropylene plates with a thickness of 3 mm. The dry film thickness becomes 40 to 60 microns, and it is cured by biting for about 20 minutes, and then at 140 ° C. Bake for 20 minutes. The obtained film was cut into a free-state film having a drinking part, 5 cm in length and 1 cm in width, and peeled from a polypropylene plate to form a seed and a carrier. For this free-state film, the elongation was measured at a rate of 10 mm / min at 20 ° C using a 15-force tester ("Tensilon", manufactured by Toyo Boldwin Co., Ltd.) at a rate of 10 mm / min. rate. ^ The foregoing results are shown in Table 4. Example 2 Intermediate Coating 2 20 28.6 parts of the urethane-modified resin obtained in the previous Preparation Example 1, 148 parts of PP-2001 (polypropylene-based elastomer, 3 A, manufactured by Yuekai Chemical Co., Ltd., with a solid content of 27%, an acid value of 6.6 mgKOH / g, a light base value of 13,16.7 parts U-128 (melamine resin, made by Mitsui & Sitec Corporation & 60% of content), 33.3 parts of MF-K60X (active methylene block & 34 200427795 ester manufactured by Asahi Chemical Industry Co., solid content of 60%), 25 parts obtained from the previous Preparation Example 4 Non-aqueous dispersion, 39.2 parts of CR-97 (titanium oxide, manufactured by Ishihara Sangyo Co., Ltd.), 2.9 parts of MA-100 (carbon black pigment, manufactured by Mitsubishi Chemical Co., Ltd.) '0.1 part of Desbaron 4200-20 (anti- Settling agent, manufactured by Kusumoto Chemical Co., Ltd.) 5 and 0.W * LMS-300 (talc, manufactured by Fuji Talc) placed in a 1 liter container. 'Mix with a disperser, add GB503M (having a particle diameter of 1.6 mm) Glass beads), using a desktop sG mill to disperse at room temperature for 2 hours and 0 inches. When the dispersion is complete, use a grinder to measure a particle size of 5 microns or Below. The glass beads were removed by filtration to obtain an intermediate coating. This coating used No. 4 Ford cup and was diluted with 10 曱 ben / Swadzu-100 (aromatic hydrocarbon solvent, manufactured by Exxon) = 1 / i mixed / cereal dilution 20 seconds / 20. (3. The solid content of the coating after dilution is 46% and the pigment concentration (PWC) is 30%. In the same manner as in Example 1, but using the aforementioned intermediate coating 2 instead of the intermediate coating 1, The coated composite film was prepared and evaluated as described above. 15 The results are not shown in Table 4. Example 3 Intermediate coating 3 4.3 parts of the urethane-modified polyester resin obtained in the previous preparation example, 125 parts Polyolefin elastomer (bj) obtained in the previous Preparation Example 2, 66.7 parts of 20 MF_K60x (block isocyanate, manufactured by Asahi Chemical Industry Co., Ltd.), solid matter 60 /. '95 wound CR-97 (titanium oxide, Ishihara Industry Co., Ltd.), 9 parts of Ten-100 (Carbon black pigment, manufactured by Mitsubishi Chemical Corporation) and 4 parts of Disparon 4 Trace 20 (Anti-settling agent, manufactured by Kusumoto Chemical Co., Ltd.) Pigments were prepared in a similar manner to the intermediate coating 1 of Example 1. The solids of the resulting diluted coating 35 200427795 contained The amount was 51%, and the pigment concentration (PWC) of the coating was 50%. According to the same manner as in Example 1 but using the aforementioned intermediate coating 3 instead of the intermediate coating 3, a coated composite film was prepared and evaluated in a similar manner. The results are shown in Table 4. 5 Example 4 Intermediate Coating 4 28.6 parts of the urethane-modified polyester resin obtained in the previous Preparation Example 1 and 99.9 parts of the polyolefin elastomer obtained in the previous Preparation Example 3 (b -2), 16.7 parts U-128 (melamine resin, manufactured by Mitsui Citigroup, solid content 60%) 10, 33.3 parts MF-K60X (reactive methylene block isocyanate, Asahi Chemical Industry Co., Ltd. Manufacturing, solid content 60%) '25 parts of the non-aqueous dispersion obtained in the previous Preparation Example 4, 39.2 parts of CR-97 (titanium oxide, manufactured by Ishihara Industries), 2.9 parts of MA-100 (carbon black pigment, Mitsubishi Chemical (Manufactured by the company), 0.1 parts of Desbaron 4200-20 (anti-settling agent, manufactured by Nanbu Chemical Co., Ltd.) and 0.8 parts of LMS-300 (15 talc, manufactured by Fuji Talc) were placed in a 1 liter container, similar to the implementation of 2 Coating 2 was prepared as a coating method. After dilution, the solid content of the coating is 45%, and the pigment concentration (PWC) is 30%. According to the same manner as in Example 1, but using the aforementioned intermediate coating 2 instead of the intermediate coating 4, a coated composite film was prepared and evaluated in a similar manner. The results are shown in Table 4. Comparative Example 1 Intermediate paint 5 107 parts of urethane-modified polyester resin varnish obtained in the previous Preparation Example 1, 280 parts of CR-97 (titanium oxide manufactured by Ishihara Industries), 13 parts of 36 200427795 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 container and mixed with a disperser, and placed with The total amount of feed was GB503M (glass beads with a diameter of 1.6 mm), and the material was dispersed at room temperature for 3 hours using a table-type SG mill for 3 hours to obtain a gray pigment paste. When the dispersion was completed, the particle diameter was 5 micrometers or less as measured using a grind meter. The glass beads are filtered to obtain a pigment paste. To 100 parts of this pigment paste, 24 parts of urethane modified urethane resin prepared in Preparation Example 1 and 24 parts of MF-K60X (reactive methylene block isocyanate, manufactured by Asahi Chemical Industry Co., Ltd., solid 60% of content), and 24 parts of 10 U-20N60 (melamine resin, manufactured by Mitsui & Citigroup, solid content of 60%). A mixed solvent of ethoxyethyl propionate / S-100 (aromatic hydrocarbon solvent, manufactured by Exxon) = 1/1 was added thereto, and the material was diluted to 19 seconds / 20 ° C using a No. 4 Ford cup. The solids content of the paint after dilution was 49% and the pigment concentration (PWC) of the paint was 30%. 15 In the same manner as in Example 1, but using the aforementioned intermediate coating 2 instead of the intermediate coating 5, a coated composite film was prepared and evaluated in a similar manner. The results are shown in Table 4. Comparative Example 2 CP-101 (cut wafer primer, manufactured by Japan Coatings Co., Ltd.) was spray-coated on a steel plate that had been subjected to electrodeposition coating and baking hardening, and had a film thickness of 5 micrometers, followed by using Comparative Example 1 with an intermediate coating 5 A coating film is formed. After being cured for 5 minutes, the intermediate coating film 5 described in Comparative Example 1 was used to form an intermediate coating film. Then, the same base coating and clear coating described in the example were used, and the coated composite coating was prepared as in Example i and evaluated in a similar manner. The results are shown in Table 4. 37 200427795 [Table 4] Example 1 Example 2 Example 3 Example 4 Comparative example 1 Comparative example 2 Appearance ratio (Wa value) 25 21 21 19 21 29 The peeling diameter (mm) of the cut wafer 1.5 1.5 1.2 1.2 2.0 1.5 Number of peelings (block) 10 8 10 9 20 10 Elongation of intermediate coating film (%) 70 100 80 100 30 30 I: Simple explanation of the drawing] (None) Lu 5 [The main components of the drawing represent the symbol table] ( no)
3838
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US9095878B2 (en) | 2006-08-02 | 2015-08-04 | Ford Motor Company | Coating compositions and methods of applying the same |
JP5446222B2 (en) * | 2008-11-14 | 2014-03-19 | 住友電気工業株式会社 | Conductive paste, electromagnetic shielding film using the same, and electromagnetic shielding flexible printed wiring board |
KR101491779B1 (en) * | 2012-05-16 | 2015-02-11 | 주식회사 엘지화학 | Self-healable barrier substrate for flexible organic electronic device and method for manufacturing the same |
JP6028129B1 (en) * | 2015-03-27 | 2016-11-16 | 帝人株式会社 | Method for producing composite membrane |
US20210009848A1 (en) * | 2018-03-21 | 2021-01-14 | Kansai Paint Co., Ltd. | Multi-layer coating film formation method |
JP6630416B2 (en) * | 2018-09-13 | 2020-01-15 | 三井化学株式会社 | Curable composition |
CN109517512B (en) * | 2018-11-21 | 2021-07-20 | 邦弗特新材料股份有限公司 | High-solid-content two-component coating and application thereof |
CN110330619B (en) * | 2019-07-30 | 2020-07-28 | 中国科学院长春应用化学研究所 | Medical polyurethane material containing lactone group, preparation method thereof and medical catheter |
CN110499673A (en) * | 2019-08-27 | 2019-11-26 | 江苏美新建材科技有限公司 | A kind of decoration composite faced plywood bent |
CN113214697A (en) * | 2021-06-18 | 2021-08-06 | 中国船舶重工集团公司第七二五研究所 | Organic silicon foaming connection coating and preparation method thereof |
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