TW201236867A - Laminate - Google Patents

Laminate Download PDF

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Publication number
TW201236867A
TW201236867A TW100139155A TW100139155A TW201236867A TW 201236867 A TW201236867 A TW 201236867A TW 100139155 A TW100139155 A TW 100139155A TW 100139155 A TW100139155 A TW 100139155A TW 201236867 A TW201236867 A TW 201236867A
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TW
Taiwan
Prior art keywords
group
layer
functional group
laminate
adhesive functional
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TW100139155A
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Chinese (zh)
Inventor
Yumi Nakano
Yasuko Kouketsu
Shigehito Sagisaka
Shinya Murakami
Masaji Komori
Takayuki Hirao
Takeshi Inaba
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Daikin Ind Ltd
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Publication of TW201236867A publication Critical patent/TW201236867A/en

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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F16ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
    • F16LPIPES; JOINTS OR FITTINGS FOR PIPES; SUPPORTS FOR PIPES, CABLES OR PROTECTIVE TUBING; MEANS FOR THERMAL INSULATION IN GENERAL
    • F16L11/00Hoses, i.e. flexible pipes
    • F16L11/04Hoses, i.e. flexible pipes made of rubber or flexible plastics
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B1/00Layered products having a general shape other than plane
    • B32B1/08Tubular products
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/06Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material
    • B32B27/08Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material of synthetic resin
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/28Layered products comprising a layer of synthetic resin comprising synthetic resins not wholly covered by any one of the sub-groups B32B27/30 - B32B27/42
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/32Layered products comprising a layer of synthetic resin comprising polyolefins
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B7/00Layered products characterised by the relation between layers; Layered products characterised by the relative orientation of features between layers, or by the relative values of a measurable parameter between layers, i.e. products comprising layers having different physical, chemical or physicochemical properties; Layered products characterised by the interconnection of layers
    • B32B7/04Interconnection of layers
    • B32B7/10Interconnection of layers at least one layer having inter-reactive properties
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2439/00Containers; Receptacles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2597/00Tubular articles, e.g. hoses, pipes

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Laminated Bodies (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Wrappers (AREA)
  • Rigid Pipes And Flexible Pipes (AREA)

Abstract

Provided is a laminate in which a layer composed of a fluororesin containing an adhesive functional group and a layer composed of a modified polyolefin resin can be adhered to each other directly and strongly even when a molding method such as a multilayer blow molding method or a multicolor injection molding method is employed, and which has excellent initial adhesion properties, excellent uniformity of initial adhesion properties and excellent retained adhesion properties. The laminate comprises a layer (B-1) composed of a modified polyolefin resin and a layer (C) formed on the layer (B-1) and composed of a fluororesin containing an adhesive functional group, and is characterized in that the modified polyolefin resin which constitutes the layer (B-1) is a modified polyolefin having an imino group or a carbodiimide group and the fluororesin containing an adhesive functional group which constitutes the layer (C) has an adhesive functional group having reactivity with the functional group contained in the modified polyolefin resin that constitutes the layer (B-1) at the terminal of the main chain thereof and/or the terminal of a side chain thereof.

Description

201236867 六、發明說明: 【發明所屬之技術領域】 本發明係有關一種層合物。 【先前技術】 以往,含氟聚合物由於耐熱性、耐藥品性、耐候性、 表面特性(低摩擦特性等)、電絕緣性優異,故已用於各種 用途。 另一方面’含氟聚合物一般機械強度或尺寸安定性不 充分,且價格昂貴。 因此爲了最大限度地活性含氟聚合物之優點並使缺點 最小化’已封含氟聚合物與其他有機材料之黏著、層合化 、與無機材料之黏著、層合化等進行各種探討。 例如,於專利文獻1中,提案有含官能基之含氟聚合 物與非氟系之熱可塑性樹脂例如聚醯亞胺樹脂之層合物0 於專利文獻2中,則記載一種中空成形體,其具有聚 烯烴樹脂所形成之層(A) '改質聚烯烴樹脂所形成之層(B) 、及氟樹脂所形成之層(C),前述氟樹脂所形成之層(C)爲 最內層或最外層之至少任一側之層。 [先前技術文獻] [專利文獻1]國際公開第9 8/5 5 5 5 7號說明書 [專利文獻2]國際公開第2008-04 1 643號說明書 201236867 【發明內容】 [發明欲解決之課題] 然而,專利文獻2中記載之中空成形體’於一般用以 製作大型槽形狀而使用之多層吹塑成形時,由於構成2層 之2種類之樹脂以熔融狀態接觸之時間短,且於進行多色 射出成形時,因先射出之樹脂溫度降低,故使層(B)與層 (C)之黏著性不充分,而仍有改善之餘地。 本發明之目的係提供一種即使使用多層吹塑成形或多 色射出成形等之成形方法時,亦可使含有黏著性官能基之 氟樹脂所形成之層與改質聚烯烴樹脂所形成之層直接且強 固地黏著,且初期黏著性及初期黏著性之均一性、進而燃 料浸漬後之黏著性(保持黏著性)優異之層合物。 [解決課題之手段] 本發明人等經積極探討後,發現具有特定官能基之改 質聚烯烴與具有黏著性官能基之氟樹脂可非常強固地黏著 ,因而完成本發明。 亦即,本發明係一種層合物(本說明書中,有時稱爲 第1層合物),其特徵爲具有改質聚烯烴樹脂所形成之層 (B-1)及於前述層(B-1)上所形成之含有黏著性官能基之氟 樹脂所形成之層(C),構成層(B-1)之改質聚烯烴樹脂爲具 有亞胺基或碳二醯亞胺基之改質聚烯烴,構成前述層(C) 之含有黏著性官能基之氟樹脂於主鏈末端及/或側鏈末端 具有對前述構成層(B-1)之改質聚烯烴樹脂所具有之官能 6 _ 201236867 基顯示出反應性之黏著性官能基》 該具有亞胺基之改質聚烯烴較好爲在自由基產生劑存 在下’使聚烯烴與含有多數亞胺基之聚亞胺化合物經接枝 處理而得之亞胺改質聚烯烴,具有碳二醯亞胺基之改質聚 烯烴係在未改質聚烯烴存在下,使具有可與碳二醯亞胺基 反應之聚烯烴與含有碳二醯亞胺基之化合物進行反應而得 之碳二醯亞胺改質聚烯烴。 較好尙具有於層(B-1)上所形成之聚烯烴樹脂所形成 之層(A) 〇 本發明亦係一種層合物(本說明書中,有時稱爲第2 層合物),其特徵爲具有聚烯烴樹脂所形成之層(A)、改質 聚烯烴樹脂所形成之層(B-2)及含有黏著性官能基之氟樹 脂所形成之層(C),前述含有黏著性官能基之氟樹脂所形 成之層(C)爲最內層或最外層中之至少任一側之層,構成 前述層(C)之含有黏著性官能基之氟樹脂於主鏈末端及/或 側鏈末端具有對前述構成層(B-2)之改質聚烯烴樹脂所具 有之官能基顯示出反應性之黏著性官能基,前述黏著性官 能基相對於構成含有黏著性官能基之氟樹脂之全聚合單位 1 0 0莫耳%,爲〇 · 2 ~ 1 0莫耳%。 上述黏著性官能基相對於構成含黏著性官能基之氟樹 脂之全部聚合單位100莫耳%,較好爲0.2〜5莫耳%。 上述黏著性官能基相對於構成含黏著性官能基之氟樹 脂之全部聚合單位100莫耳%,較好爲0.2〜2莫耳%。 上述黏著性官能基較好爲由胺基、醯胺基、胺甲醯基 201236867 、羥基、羧基、羧酸鹵化物基、酯基、酸酐基、碳酸酯基 、環氧基、腈基及異氰酸酯基所組成群組選出之至少一種 〇 上述含黏著性官能基之氟樹脂之融點較好爲 120〜240〇C ° 上述含黏著性官能基之氟樹脂之融點較好爲所含有之 黏著性官能基之分解溫度以下。 構成上述層(B-2)之改質聚烯烴樹脂具有之官能基較 好爲由胺基、醯胺基、胺甲醯基、羥基、羧基、羧酸鹵化 物基、酯基、酸酐基、碳酸酯基、環氧基、腈基及異氰酸 酯基所組成群組選出之至少一種。 本發明之層合物較好爲藥液用容器。 本發明之層合物較好爲尿素水用容器。 本發明之層合物較好爲燃料用槽。 本發明之層合物較好爲飲料用或食品用槽。 本發明之層合物較好爲埋設地下之管路或軟管。 本發明之層合物較好爲漏斗頸(filler neck)軟管、燃 料軟管、或燃料管路。 以下詳細說明本發明。 本發明之第一層合物爲具有由改質之聚烯烴樹脂所形 成之層(B-1),及上述層(B-1)上形成之由含黏著性官能基 之氟樹脂所形成之層(C)。 構成層(B-1)之改質聚烯烴樹脂爲具有亞胺基或碳二 201236867 具有亞胺基之改質聚烯烴較好爲在自由基產生劑存在 下’使聚烯烴與含有多數亞胺基之聚亞胺化合物經接枝處 理而得之亞胺改質之聚烯烴。 上述亞胺改質之聚烯烴係藉由在自由基產生劑存在下 ,使聚烯烴與含有多數亞胺基之聚亞胺化合物經接枝處理 而選擇。至於聚烯烴較好爲聚乙烯。 上述聚亞胺化合物較好爲例如以下述式表示之化合物 [化1] R1 R2 R3 [式中之R1、R2、R3可分別相同亦可不同,表示非反應性 原子或有機基,R1及R2亦可相互鍵結形成環,η表示 20〜2000之整數]。 式中之R1、R2、R3爲相同或不同,且較好爲氫原子 、烷基、烯基、炔基、環烷基、芳基、雜環基或烷氧基。 該情況下,烷基較好爲包含甲基、乙基、丙基、丁基、戊 基、異丙基、異丁基等之碳數1〜10之烷基,更好爲碳數 1〜8之烷基,又更好爲碳數1~5之烷基,最好爲碳數1~3 之烷基。 上述烯基較好爲碳數2~10之烯基,更好爲碳數2~8 之烯基,又更好爲碳數2~5之烯基,最好爲碳數2〜4之烯 -9- 201236867 上述炔基較好爲乙炔基、1_丙炔基、丨_庚炔基等碳數 2〜18之炔基,更好爲碳數2〜10之炔基,又更好爲碳數 2〜6之炔基,最好爲碳數2〜4之炔基。 上述環烷基較好爲環丙基、環丁基、環戊基、環己基 、環辛基等碳數3〜10之環烷基,更好爲碳數3〜6之環烷 基’最好爲碳數5〜6之環院基。 至於上述芳基較好爲苯基、甲苯基、萘基等碳數 6〜10之芳基。 上述雜環基爲例如以呋喃環、噁唑環、異噁哩環、四 氫呋喃環等五員環,吡喃環等六員環、苯并呋喃環、異苯 并呋喃環、二苯并呋喃環 '咕噸酮環、咕噸環、色滿環、 異色院環、色稀環等縮合環爲代表之含有氧原子作爲雜原 子之雜環,或者例如以噻吩環、噻唑環、異噻哩環、噻二 唑環、苯并噻唑環等爲代表之含硫原子作爲雜原子之雜環 ,另外,列舉爲以例如吡咯環、吡唑環、咪唑環、三哩環 、吡咯啶環等五員環、吡啶環、嗒啶環、嘧啶環、哌陡環 、哌嗪環、嗎啉環等六員環,吲哚環、假吲哚環、異卩引哄 環、吲唑環、吲哚唑環、異吲哚啉環、喹啉環、異喹琳環 、喹啉喹啉環、唾寧環、醌茜環(quinazarin)、駄曝環、 嘌呤環、咔唑環、吖啶環、萘并喹啉環、菲繞曝環、菲繞 啉環、萘陡環、苯并嗤啉環、吩嚼曉環、駄菁環、恵菁等 縮含環爲代表之含氮原子作爲雜原子之雜環等。 至於上述烷氧基’列舉爲甲氧基、乙氧基、丙氧基、 異丙氧基等碳數1〜10、較好1〜6之院氧基。 -10- 201236867 至於聚亞胺化合物之較佳具體例,列舉爲例如聚伸乙 亞胺。 聚亞胺化合物之分子量較好爲1,000以上,但就活化 處理後與烯烴之反應性等之觀點而言,較好爲更高分子量 。具體而言,較好分子量爲1,000~200,000,更好分子量 爲 3,000~200,000,最好分子量爲 1 5,000~200,000。 接枝處理時所用之自由基產生劑列舉爲有機過氧化物 、有機過氧酯。例如,使用苯甲醯基過氧化物、二氯苯甲 醯基過氧化物、二枯基過氧化物、二第三丁基過氧化物、 2.5- 二甲基-2,5-二(過氧化物苯甲酸酯)己炔-3、1,4-雙(第 三丁基過氧異丙基)苯、月桂醯基過氧化物、第三丁基過 氧乙酸酯、2,5-二甲基-2,5-二(第三丁基過氧基)己炔-3、 2.5- 二甲基-2,5-二(第三丁基過氧基)己烷、第三丁基過氧 苯甲酸酯、第三丁基過氧苯基乙酸酯、第三丁基過氧異丁 酸酯、第三丁基過氧第二辛酸酯、第三丁基過氧特戊酸酯 、枯基過氧特戊酸酯及第三丁基過氧二乙基乙酸酯,以及 偶氮化合物,例如偶氮雙異丁腈、二甲基偶氮異丁腈。該 等中較好爲二枯基過氧化物、二第三丁基過氧化物、2,5-二甲基-2,5·二(第三丁基過氧化物)己炔-3、2,5-二甲基- 2.5- 二(第三丁基過氧基)己烷、i,4-雙(第三丁基過氧異丙 基)苯等二烷基過氧化物。 其中,自由基產生劑較好爲有機過氧化物。至於有機 過氧化物以半衰期之分解溫度爲loot以上者較佳。又, 有機過氧化物具體而言較好爲由二枯基過氧化物、苯甲醯 201236867 基過氧化物、二第三丁基過氧化物、2,5-二甲基-二(第三 丁基過氧基)己炔、2,5-二甲基-2,5-(第三丁基過氧基)己 炔-3、月桂醯基過氧化物、及第三丁基過氧基苯甲酸酯等 所組成群組選出之至少一種。 自由基產生劑之使用比例相對於聚烯烴100重量份, 通常爲0.001〜1重量份。 上述亞胺改質之烯烴可藉由均勻混合聚烯烴、聚亞胺 化合物、自由基產生劑而製造。具體而言,列舉爲使用擠 出機或班伯里混練機'捏合機等之熔融混練法,溶解於適 當溶劑中之溶液法、懸浮於適當溶劑中之漿液法、或所謂 氣相接枝法等》 上述處理溫度係考慮聚烯烴之劣化、聚亞胺化合物之 分解、使用之自由基產生劑之分解溫度等而適當選擇。例 如,上述熔融混練法之情況,通常在60〜350 °c之溫度進行 。上述處理溫度較好爲190〜3 50°C,更好爲200〜30(TC。 具有碳二醯亞胺之改質聚烯烴較好爲在未改質之聚烯 烴存在下,使具有與碳二醯亞胺基反應之基之聚烯烴與含 碳二醯亞胺基之化合物反應獲得之碳二醯亞胺改質之聚烯 烴。反應之方法列舉爲在230 °C以上之溫度熔融混練之方 法。 具有與碳二醯亞胺基反應之基之聚烯烴可藉由將具有 與碳二醯亞胺基反應之基之化合物導入於聚烯烴中而獲得 至於聚烯烴列舉爲乙烯、丙烯、1-丁烯、4-甲基-1-戊 201236867 烯、3·甲基-1-丁烯、1-己烯、1-辛烯、四環十二碳烯、降 冰片烯之均聚物或共聚物。 具有與碳二醯亞胺基反應之基之化合物列舉爲丙烯酸 、甲基丙烯酸、馬來酸、富馬酸、四氫苯二甲酸、衣康酸 、檸康酸、巴豆酸、異巴豆酸、降冰片烯二羧酸、雙環 [2,2,1]庚-2-烯-5,6-二羧酸等不飽和羧酸,或該等之酸酐 或該等之衍生物(例如’醯鹵、醯胺、醯亞胺、酯等)。該 等中’較好爲馬來酸酐、(甲基)丙烯酸、衣康酸酐、檸康 酸酐、四氫苯二甲酸酐、雙環[2,2,1]庚-2 -烯-5,6 -二羧酸 酐、(甲基)丙烯酸羥基乙酯、甲基丙烯酸縮水甘油酯、甲 基丙烯酸胺基丙酯。 於聚烯烴中導入具有與碳二醯亞胺基反應之基之化合 物之方法可採用習知之方法,可例示爲例如將具有與碳二 醯亞胺基反應之基之化合物接枝共聚合於聚烯烴主鏈上之 方法’將聚烯烴與具有與碳二醯亞胺基反應之基之化合物 經自由基共聚合之方法等。 至於具有與碳二醯亞胺基反應之基之聚烯烴較好爲聚 乙烯、聚丙烯、聚丁烯-1、聚-4-甲基戊烯-1及該等之α-烯烴共聚物等之結晶性聚烯烴之馬來酸酐接枝共聚物,更 好爲聚乙烯之馬來酸酐接枝共聚物。尤其,較好爲密度 0_915 g/cm3以上之聚乙烯之馬來酸酐接枝共聚物。 含有碳二醯亞胺基之化合物爲具有以下式表示之重複 單位之聚碳二醯亞胺: £ -13- 201236867 -N = C=N-R1- (式中,R1表示碳數2至4〇之二價有機基 聚碳一醯亞肢可藉由在縮合觸媒存在下,無溶劑或在 惰性溶劑中’使脂肪族二異氰酸酯 '芳香族二異氰酸醋、 脂環族一異氛酸醋等有機一異氰酸酯進行脫碳酸縮合反應 而製造。例如’可使用六亞甲基二異氰酸酯、4,4_二苯基 甲院一異氰酸酯' 1,4 -伸苯基—異氰酸醋、2,4_伸甲苯基 二異氰酸酯、伸一甲苯基二異氰酸酯、環己院--二異氰 酸醋、二環己基甲院-4,4’·二異氰酸酯、異佛爾酮二異氰 酸酯等二異氰酸酯等。 未改質之聚Μ烴列舉爲例如低密度聚乙稀、高密度聚 乙烯、線性低密度聚乙稀、聚丙燒、乙稀-丙稀共聚物、 乙烯-α烯烴共聚物、乙烯-丙烯共聚物、乙烯-丁烯共聚物 、乙烯-己烯共聚物、乙烯-辛烯共聚物、聚丁烯_丨、聚_4_ 甲基-1-戊烯、聚-3-甲基-1-丁烯、乙烯-四環十二碳烯共 聚物等環狀聚烯烴等。 本發明之第一層合物較好尙具有在層(Β-1)上形成之 由聚烯烴樹脂所形成之層(Α)。本發明之第一層合物爲具 有層(Α)者時,有提高機械強度之優點。 本發明之第二層合物具有由聚烯烴樹脂所形成之層 (Α)、由改質聚烯烴樹脂所形成之層(Β_2)、及由含黏著性 官能基之氟樹脂所形成之層(C)。 本發明之第二層合物由於爲具有由聚烯烴樹脂所形成 -14- 201236867 之層(A)與由含黏著性官能基之氟樹脂所形成之層(c),故 相較於由過去廣用之塑膠或彈性體形成者,爲耐藥品性、 耐燃性、燃料低透過性優異者,例如爲對乙醇或甲醇等醇 類或尿素水仍可發揮耐藥品性、耐燃料性、燃料低透過性 者。 本發明之第二層合物爲進而具有由改質聚烯烴樹脂所 形成之層(B-2)者,而且,構成前述層(C)之含黏著性官能 基之氟樹脂在主鏈末端及/或側鏈末端具有對構成前述層 (B-2)之改質聚烯烴樹脂具有之官能基顯示反應性之黏著 性官能基。上述黏著性官能基相對於構成含黏著性官能基 之氟樹脂之全部聚合單位100莫耳%爲0.2〜10莫耳%。因 此,可提高由聚烯烴樹脂所形成之層(A)與由含黏著性官 能基之氟樹脂所形成之層(C)之黏著性,且可獲得耐衝擊 性、機械強度極優異之層合物。 構成上述層(C)之含黏著性官能基之氟樹脂在主鏈末 端及/或側鏈末端具有對構成前述層(B-1)及層(B-2)之改質 聚烯烴樹脂具有之官能基顯示反應性之黏著性官能基。亦 即,上述含黏著性官能基之氟樹脂可爲由主鏈末端或側鏈 末端之任一者具有黏著性官能基之聚合物所成者,亦可爲 主鏈末端及側鏈末端二者均具有黏著性官能基之聚合物所 組成者。 上述含黏著性官能基之氟樹脂爲主鏈末端具有黏著性 官能基時,可在主鏈之兩末端具有,亦可僅在任一末端具 有。該黏著性官能基亦可使用聚合起始劑導入。 -15- 201236867 上述含黏著性官能基之氟樹脂爲僅在主鏈末端具有黏 著性官能基之聚合物時,基於不會使機械特性、耐藥品性 顯著下降之理由,或生產性、成本面方面有利,但黏著性 官能基之數目被分子量所左右,而有含有率之最大値有上 限之缺點。 上述含黏著性官能基之氟樹脂爲側鏈末端具有黏著性 官能基時’就可某種程度自由地增加黏著性官能基量以提 高黏著性而言係較佳。 於側鏈末端導入上述黏著性官能基之方法可如上述般 使含黏著性官能基之單體共聚合而導入,亦可在聚合後利 用接枝反應導入。. 利用接枝反應導入黏著性官能基時,相對於完全不含 官能基之樹脂,可使產生自由基之例如有機過氧化物,與 —分子中具有不飽和鍵與黏著性官能基之物質反應而導入 ,或者’使含有較安定之官能基之單體共聚合,在聚合後 使其官能基反應作成反應性高的官能基,將黏著性官能基 導入於其中。 本發明之第一層合物中,上述含黏著性官能基之氟樹 脂所具有之黏著性官能基’相對於構成含黏著性官能基之 氟樹脂之全聚合單位100莫耳%,較好爲005〜1()莫耳% ’更好爲0.05〜5莫耳% ’又更好爲02〜2莫耳0/〇。 本發明之第二層合物中,上述含黏著性官能基之氟樹 脂所具有之黏著性官能基,相對於構成含黏著性官能基之 氟樹脂之全聚合單體1〇〇莫耳%爲〇2~1〇莫耳%。藉由使 201236867 黏著性官能基在上述範圍,而獲得層(B-2)與層(C)極優異 之黏著性’據此,可保持接著面整體均勻而無不均勻之初 期高黏著強度及長期使用後仍高之黏著強度。伴隨於此, 作爲層合物整體,成爲對於耐衝擊性、機械強度均優異之 層合物。 本發明之第二層合物中,黏著性官能基係依據所層合 之對向材料之種類、形狀、黏著目的、用途、需要之黏著 力 '氟樹脂種類與黏著方法等之差異而適當選擇,但相對 於構成含黏著性官能基之氟樹脂之全聚合單位1 〇 〇莫耳% ,較好爲0.2〜5莫耳%,更好爲0.2〜2莫耳%。上述黏著 性官能基之比例可使用N M R或IR之方法求得。 上述黏著性官能基列舉爲具有胺基、羥基、環氧基、 腈基、羰基之官能基等。 上述羰基爲由碳-氧雙鍵所構成之碳二價之基,且以-c( = 〇)-表示。上述具有羰基之官能基列舉爲例如碳酸酯基 、羧酸鹵化物基(鹵基甲醯基)、甲醯基、羧基、酯基[-C( = 0)0-]、酸酐基[-c( = 0)0-c( = 0)_]、異氰酸酯基、醯胺 基、醯亞胺基[-C( = 0)-NH-C( = 0)_]、胺基甲酸酯基[-NH-C( = 0)0-]、胺甲醯基[NH2-C( = 0)_]、胺甲醯氧基[NH2-C( = 〇)〇-]、脲基[NH2-C( = 〇)-NH-]、草醯胺基[nh2-c( = o)_ c(<0)-]等化學構造上之—部分者等。 醯胺基、醯亞胺基、胺基甲酸酯基、胺甲醯基、胺甲 麟氣基、脲基、草醯胺基等之氮原子上所鍵結之氫原子亦 句·經例如烷基等烴基取代。 -17- 201236867 至於上述黏著性官能基,其中較好爲由胺基、醯胺 、胺甲醯基、羥基、羧基、羧酸鹵化物基、酯基、酸酐 、碳酸酯基、環氧基、腈基及異氰酸酯基所組成群組選 之至少一種。上述黏著性官能基更好爲由例如環氧基、 基、及羧基所組成群組選出之至少一種,又更好爲羧基 本發明中,構成上述層(C)之含黏著性官能基之氟 脂爲具有至少一種由含氟乙烯性單體衍生之重複單位之 聚物或共聚物。 上述氟樹脂可爲僅使含氟乙烯性單體聚合而成者, 可爲使含氟乙烯性單體與不具有氟原子之乙烯性單體聚 而成者。 本發明中,氟樹脂層可爲含一種上述氟樹脂者,亦 爲含兩種以上者。 上述含黏著性官能基之氟樹脂較好具有由四氟乙 [TFE]、偏氟化乙烯[VdF]、氯三氟乙烯[CTFE]、氟化乙 [VF]、六氟丙烯[HFP]、六氟異丁烷[HFIB]、 CHfCX^CFJnX、式中,X1 爲 Η 或 F,X2 爲 H、F 爲 ,11爲1~10之整數)表示之單體、以CFfCF-ORf1 (式中 Rf1表示碳數1〜8之全氟烷基)表示之全氟(烷基乙烯基 )[PAVE]、及以 CF2 = CF-OCH2-Rf2(式中,Rf2 爲碳數 1 之全氟烷基)表示之烷基全氟乙烯基醚衍生物、三氟乙 、三氟丙烯、四氟丙烯、五氟丙烯、三氟丁烯、四氟異 烯、含碘之氟化乙烯基醚所組成群組選出之至少一種含 單體爲主之聚合單位。氟樹脂亦可具有由乙烯[Et]、丙 基 基 出 羥 〇 樹 均 亦 合 可 烯 烯 以 C1 7 醚 〜5 烯 丁 氟 稀 -18- 201236867 [Pr]、長鏈烯、及烷基乙烯基醚所組成群組選出之至少一 種單體爲主之聚合單位作爲不含氟之單體。201236867 VI. Description of the Invention: [Technical Field to Which the Invention Is Ascribed] The present invention relates to a laminate. [Prior Art] Conventionally, fluoropolymers have been used in various applications because of their excellent heat resistance, chemical resistance, weather resistance, surface properties (such as low friction properties), and electrical insulation properties. On the other hand, fluoropolymers generally have insufficient mechanical strength or dimensional stability and are expensive. Therefore, in order to maximize the advantages of the active fluoropolymer and to minimize the disadvantages, the adhesion of the sealed fluoropolymer to other organic materials, lamination, adhesion to an inorganic material, lamination, and the like are discussed. For example, Patent Document 1 proposes a laminate of a functional group-containing fluoropolymer and a non-fluorine-based thermoplastic resin such as a polyimide resin. In Patent Document 2, a hollow molded body is described. It has a layer formed of a polyolefin resin (A) a layer (B) formed of a modified polyolefin resin, and a layer (C) formed of a fluororesin, and the layer (C) formed of the fluororesin is the innermost layer a layer of at least either side of the layer or outermost layer. [Prior Art Document] [Patent Document 1] International Publication No. 9 8/5 5 5 5 7 [Patent Document 2] International Publication No. 2008-04 1 643 No. 201236867 [Summary of the Invention] [Problems to be Solved by the Invention] However, in the case of the multi-layer blow molding which is generally used for producing a large groove shape, the hollow molded body described in Patent Document 2 has a short period of time in which the two types of resin constituting the two layers are in contact with each other in a molten state. In the case of color injection molding, since the temperature of the resin which is first ejected is lowered, the adhesion between the layer (B) and the layer (C) is insufficient, and there is still room for improvement. It is an object of the present invention to provide a layer formed of a fluororesin containing an adhesive functional group and a layer formed of a modified polyolefin resin, even when a molding method such as multi-layer blow molding or multi-color injection molding is used. It is a laminate which is strongly adhered and has excellent initial adhesion and initial adhesion, and is excellent in adhesion after fuel impregnation (maintaining adhesion). [Means for Solving the Problem] The inventors of the present invention have found that the modified polyolefin having a specific functional group and the fluororesin having an adhesive functional group can be strongly adhered, and thus the present invention has been completed. That is, the present invention is a laminate (sometimes referred to as a first laminate in the present specification) characterized by having a layer (B-1) formed of a modified polyolefin resin and the above layer (B) -1) a layer (C) formed of a fluororesin containing an adhesive functional group formed thereon, and a modified polyolefin resin constituting the layer (B-1) having an imine group or a carbodiimide group The polyolefin having the adhesive functional group constituting the layer (C) has a functional group for the modified polyolefin resin of the above-mentioned constituent layer (B-1) at the end of the main chain and/or at the side of the side chain. _ 201236867 The base exhibits a reactive adhesive functional group. The modified polyolefin having an imine group is preferably in the presence of a radical generating agent to polymerize the polyolefin with a polyimine compound containing a plurality of imine groups. An imine modified polyolefin obtained by treatment of a branch, a modified polyolefin having a carbodiimide group, which has a polyolefin which can react with a carbodiimide group in the presence of an unmodified polyolefin A carbodiimide modified polyolefin obtained by reacting a compound of a carbodiimide group. Preferably, the layer (A) having a polyolefin resin formed on the layer (B-1) is also a laminate (in the present specification, sometimes referred to as a second laminate), It is characterized by having a layer (A) formed of a polyolefin resin, a layer (B-2) formed of a modified polyolefin resin, and a layer (C) formed of a fluororesin containing an adhesive functional group, and the above-mentioned adhesiveness The layer (C) formed of the functional group fluororesin is a layer of at least one of the innermost layer or the outermost layer, and the fluororesin of the layer (C) containing the adhesive functional group is at the end of the main chain and/or The side chain end has an adhesive functional group which exhibits reactivity with respect to a functional group of the modified polyolefin resin of the above-mentioned constituent layer (B-2), and the above-mentioned adhesive functional group is fluororesin which constitutes an adhesive functional group. The total polymerization unit is 1 0 0 mol%, which is 〇· 2 ~ 1 0 mol%. The above-mentioned adhesive functional group is preferably 100 mol%, preferably 0.2 to 5 mol%, based on the total polymerization unit of the fluororesin constituting the adhesive functional group. The above-mentioned adhesive functional group is preferably 100 mol%, preferably 0.2 to 2 mol%, based on the total polymerization unit of the fluororesin constituting the adhesive functional group. The above adhesive functional group is preferably an amine group, a decylamino group, an amine carbenyl group 201236867, a hydroxyl group, a carboxyl group, a carboxylic acid halide group, an ester group, an acid anhydride group, a carbonate group, an epoxy group, a nitrile group and an isocyanate. The melting point of at least one of the above-mentioned fluororesins containing the adhesive functional group is preferably 120 to 240 〇 C °. The melting point of the fluororesin containing the adhesive functional group is preferably the adhesion of the fluororesin containing the adhesive functional group. The decomposition temperature of the functional group is below. The functionalized polyolefin of the modified polyolefin resin constituting the above layer (B-2) preferably has an amine group, a mercaptoamine group, an amine mercapto group, a hydroxyl group, a carboxyl group, a carboxylic acid halide group, an ester group, an acid anhydride group, At least one selected from the group consisting of a carbonate group, an epoxy group, a nitrile group, and an isocyanate group. The laminate of the present invention is preferably a container for a liquid medicine. The laminate of the present invention is preferably a container for urea water. The laminate of the present invention is preferably a tank for fuel. The laminate of the present invention is preferably a beverage or food tank. The laminate of the present invention is preferably a pipe or hose for embedding underground. The laminate of the present invention is preferably a filler neck hose, a fuel hose, or a fuel line. The invention is described in detail below. The first laminate of the present invention is formed of a layer (B-1) formed of a modified polyolefin resin, and a fluororesin formed of an adhesive functional group formed on the layer (B-1). Layer (C). The modified polyolefin resin constituting the layer (B-1) is an imine group having an imine group or carbon II 201236867 having an imine group, preferably in the presence of a radical generating agent, to make the polyolefin and a plurality of imines The imine-modified polyolefin obtained by grafting the polyimine compound. The above-mentioned imine-modified polyolefin is selected by graft-treating a polyolefin with a polyimine compound containing a plurality of imine groups in the presence of a radical generating agent. The polyolefin is preferably polyethylene. The polyimine compound is preferably, for example, a compound represented by the following formula: R1 R2 R3 [wherein R1, R2 and R3 may be the same or different, and represent a non-reactive atom or an organic group, R1 and R2. They may also be bonded to each other to form a ring, and η represents an integer of 20 to 2000]. R1, R2 and R3 in the formula are the same or different and are preferably a hydrogen atom, an alkyl group, an alkenyl group, an alkynyl group, a cycloalkyl group, an aryl group, a heterocyclic group or an alkoxy group. In this case, the alkyl group is preferably an alkyl group having a carbon number of 1 to 10, preferably a carbon number of 1 to 10, such as a methyl group, an ethyl group, a propyl group, a butyl group, a pentyl group, an isopropyl group or an isobutyl group. The alkyl group of 8 is more preferably an alkyl group having 1 to 5 carbon atoms, more preferably an alkyl group having 1 to 3 carbon atoms. The alkenyl group is preferably an alkenyl group having 2 to 10 carbon atoms, more preferably an alkenyl group having 2 to 8 carbon atoms, more preferably an alkenyl group having 2 to 5 carbon atoms, and most preferably an alkene having 2 to 4 carbon atoms. -9- 201236867 The alkynyl group is preferably an alkynyl group having a carbon number of 2 to 18, such as an ethynyl group, a 1-propynyl group or a fluorenyl-heptynyl group, more preferably an alkynyl group having a carbon number of 2 to 10, more preferably The alkynyl group having 2 to 6 carbon atoms is preferably an alkynyl group having 2 to 4 carbon atoms. The cycloalkyl group is preferably a cycloalkyl group having a carbon number of 3 to 10, such as a cyclopropyl group, a cyclobutyl group, a cyclopentyl group, a cyclohexyl group or a cyclooctyl group, more preferably a cycloalkyl group having a carbon number of 3 to 6 Good for the carbon number 5 ~ 6 ring yard base. The aryl group is preferably an aryl group having 6 to 10 carbon atoms such as a phenyl group, a tolyl group or a naphthyl group. The above heterocyclic group is, for example, a five-membered ring such as a furan ring, an oxazole ring, an isoindole ring or a tetrahydrofuran ring, a six-membered ring such as a pyran ring, a benzofuran ring, an isobenzofuran ring or a dibenzofuran ring. a heterocyclic ring containing an oxygen atom as a hetero atom represented by a condensed ring such as a xanthone ring, a xanthene ring, a color full ring, a heterochromatic ring, or a dilute ring, or, for example, a thiophene ring, a thiazole ring, or an isothiazide ring. a thiadiazole ring, a benzothiazole ring or the like, which is a heterocyclic ring containing a sulfur atom as a hetero atom, and is exemplified by five members such as a pyrrole ring, a pyrazole ring, an imidazole ring, a triterpene ring, and a pyrrolidine ring. Ring, pyridine ring, acridine ring, pyrimidine ring, piperazine ring, piperazine ring, morpholine ring and other six-membered ring, anthracene ring, pseudo-fluorene ring, isoindole ring, indazole ring, carbazole Ring, isoindoline ring, quinoline ring, isoquine ring, quinoline quinoline ring, salin ring, quinazoin, anthraquinone ring, anthracene ring, indazole ring, acridine ring, naphthalene The quinoline ring, the phenanthrene ring, the phenanthroline ring, the naphthalene steep ring, the benzoporphyrin ring, the phthalocyanine ring, the phthalocyanine ring, the phthalocyanine and the like are represented by a shrink ring. Examples of the heterocyclic nitrogen atom and other hetero atoms. The alkoxy group is exemplified by a methoxy group having a carbon number of from 1 to 10, preferably from 1 to 6, such as a methoxy group, an ethoxy group, a propoxy group or an isopropoxy group. -10- 201236867 As a preferred specific example of the polyimine compound, for example, a polyethylenimine is exemplified. The molecular weight of the polyimine compound is preferably 1,000 or more, but from the viewpoint of reactivity with an olefin after activation treatment, etc., a higher molecular weight is preferred. Specifically, the preferred molecular weight is from 1,000 to 200,000, more preferably from 3,000 to 200,000, and most preferably from 5,000 to 200,000. The radical generating agent used in the grafting treatment is exemplified by an organic peroxide or an organic peroxyester. For example, the use of benzammonium peroxide, dichlorobenzhydryl peroxide, dicumyl peroxide, ditributyl peroxide, 2.5-dimethyl-2,5-di (over Oxide benzoate) hexyne-3, 1,4-bis(t-butylperoxyisopropyl)benzene, lauryl peroxide, tert-butyl peroxyacetate, 2,5 -Dimethyl-2,5-di(t-butylperoxy)hexyne-3, 2.5-dimethyl-2,5-di(t-butylperoxy)hexane, third Peroxybenzoic acid ester, tert-butylperoxyphenyl acetate, t-butyl peroxyisobutyrate, t-butyl peroxydioctanoate, tert-butylperoxy Valerate, cumylperoxypivalate and tert-butylperoxydiethylacetate, and azo compounds such as azobisisobutyronitrile, dimethylazoisobutyronitrile. Preferred among these are dicumyl peroxide, ditributyl peroxide, 2,5-dimethyl-2,5.di(t-butylperoxide)hexyne-3,2 a dialkyl peroxide such as 5-dimethyl-2.5-bis(t-butylperoxy)hexane or i,4-bis(t-butylperoxyisopropyl)benzene. Among them, the radical generating agent is preferably an organic peroxide. As for the organic peroxide, it is preferred that the decomposition temperature of the half life is above the loot. Further, the organic peroxide is specifically preferably dicumyl peroxide, benzamidine 201236867-based peroxide, di-tert-butyl peroxide, 2,5-dimethyl-di (third Butylperoxy)hexyne, 2,5-dimethyl-2,5-(t-butylperoxy)hexyne-3, lauryl peroxide, and tert-butylperoxy At least one selected from the group consisting of benzoic acid esters and the like. The use ratio of the radical generator is usually 0.001 to 1 part by weight based on 100 parts by weight of the polyolefin. The above-mentioned imine-modified olefin can be produced by uniformly mixing a polyolefin, a polyimide compound, and a radical generator. Specifically, it is exemplified by a melt kneading method using an extruder or a Banbury kneading machine 'kneader, a solution method dissolved in a suitable solvent, a slurry method suspended in a suitable solvent, or a so-called vapor phase grafting method. The above treatment temperature is appropriately selected in consideration of deterioration of polyolefin, decomposition of a polyimide compound, decomposition temperature of a radical generator used, and the like. For example, in the case of the above melt-kneading method, it is usually carried out at a temperature of 60 to 350 °C. The above treatment temperature is preferably from 190 to 3 50 ° C, more preferably from 200 to 30 (TC. The modified polyolefin having carbodiimide is preferably in the presence of unmodified polyolefin to have carbon and carbon A carbodiimide-modified polyolefin obtained by reacting a polyolefin of a diimine-imine group with a compound containing a carbodiimide group. The method of the reaction is exemplified by melt-kneading at a temperature of 230 ° C or higher. The polyolefin having a group reactive with a carbodiimide group can be obtained by introducing a compound having a group reactive with a carbodiimide group into a polyolefin, and the polyolefin is exemplified as ethylene, propylene, and 1 a homopolymer of butene, 4-methyl-1-penta 201236867 olefin, 3·methyl-1-butene, 1-hexene, 1-octene, tetracyclododecene, norbornene or Copolymers. Compounds having a group reactive with a carbodiimide group are exemplified by acrylic acid, methacrylic acid, maleic acid, fumaric acid, tetrahydrophthalic acid, itaconic acid, citraconic acid, crotonic acid, and isoforms. An unsaturated carboxylic acid such as crotonic acid, norbornene dicarboxylic acid or bicyclo[2,2,1]hept-2-ene-5,6-dicarboxylic acid, or the anhydride or And other derivatives (such as 'halogen halide, decylamine, quinone imine, ester, etc.). Among these, 'maleic anhydride, (meth)acrylic acid, itaconic anhydride, citraconic anhydride, tetrahydrobenzene Formic anhydride, bicyclo[2,2,1]hept-2-ene-5,6-dicarboxylic anhydride, hydroxyethyl (meth)acrylate, glycidyl methacrylate, aminopropyl methacrylate. The method of introducing a compound having a group reactive with a carbodiimide group into a polyolefin may be carried out by a conventional method, and is exemplified by, for example, graft copolymerizing a compound having a group reactive with a carbodiimide group to a polyolefin. The method in the main chain is a method of radically copolymerizing a polyolefin with a compound having a group reactive with a carbodiimide group, etc. The polyolefin having a group reactive with a carbodiimide group is preferably a maleic anhydride graft copolymer of a crystalline polyolefin such as polyethylene, polypropylene, polybutene-1, poly-4-methylpentene-1 or the like α-olefin copolymer, preferably polycondensed a maleic anhydride graft copolymer of ethylene. In particular, a maleic acid of polyethylene having a density of 0 to 915 g/cm 3 or more is preferred. The graft copolymer. The compound containing a carbodiimide group is a polycarbodiimide having a repeating unit represented by the following formula: £ -13 - 201236867 -N = C=N-R1- (wherein R1 represents A divalent organic polycarbocarbene having a carbon number of 2 to 4 Å can be made into an aliphatic diisocyanate 'aromatic diisocyanate vinegar, fat in the absence of a solvent or in an inert solvent in the presence of a condensation catalyst. An organic monoisocyanate such as a cyclohexanic acid vinegar is produced by a decarbonation condensation reaction. For example, 'hexamethylene diisocyanate, 4,4-diphenylylene monoisocyanate' 1,4-phenylene group can be used. Isocyanic acid vinegar, 2,4_tolyl diisocyanate, tolyl diisocyanate, cyclohexyl-diisocyanate, dicyclohexylmethyl-4,4'diisocyanate, isophorone Diisocyanate such as diisocyanate. Unmodified polyalkylene hydrocarbons are exemplified by, for example, low density polyethylene, high density polyethylene, linear low density polyethylene, polypropylene, ethylene-propylene copolymer, ethylene-alpha olefin copolymer, ethylene-propylene copolymerization. , ethylene-butene copolymer, ethylene-hexene copolymer, ethylene-octene copolymer, polybutene oxime, poly-4-methyl-1-pentene, poly-3-methyl-1-butene A cyclic polyolefin such as an olefin or an ethylene-tetracyclododecene copolymer. The first laminate of the present invention preferably has a layer (Α) formed of a polyolefin resin formed on the layer (Β-1). The first laminate of the present invention has the advantage of improving mechanical strength when it has a layer. The second laminate of the present invention has a layer formed of a polyolefin resin, a layer formed of a modified polyolefin resin (Β_2), and a layer formed of a fluororesin containing an adhesive functional group ( C). The second laminate of the present invention has a layer (A) formed of a polyolefin resin-formed layer-14-201236867 and a layer (c) formed of a fluororesin containing an adhesive functional group, as compared with the past A widely used plastic or elastomer is excellent in chemical resistance, flame resistance, and low fuel permeability. For example, it can exhibit chemical resistance, fuel resistance, and low fuel for alcohols such as ethanol or methanol or urea water. Transmissive. The second laminate of the present invention further has a layer (B-2) formed of a modified polyolefin resin, and the fluororesin containing the adhesive functional group constituting the layer (C) is at the end of the main chain. The end of the side chain has an adhesive functional group which exhibits reactivity with a functional group which is a modified polyolefin resin constituting the layer (B-2). The above-mentioned adhesive functional group is 0.2 to 10 mol% based on 100 mol% of the total polymerization unit of the fluororesin constituting the adhesive functional group. Therefore, the adhesion between the layer (A) formed of the polyolefin resin and the layer (C) formed of the fluororesin containing the adhesive functional group can be improved, and the laminate having excellent impact resistance and mechanical strength can be obtained. Things. The fluororesin containing the adhesive functional group constituting the layer (C) has a modified polyolefin resin constituting the layer (B-1) and the layer (B-2) at the end of the main chain and/or at the side of the side chain. The functional group shows a reactive adhesive functional group. That is, the fluororesin having an adhesive functional group may be a polymer having an adhesive functional group at either a main chain end or a side chain end, or may be a main chain end and a side chain end. A polymer composed of an adhesive functional group. When the fluororesin having an adhesive functional group has an adhesive functional group at the terminal of the main chain, it may be present at both ends of the main chain or may be present at only one end. The adhesive functional group can also be introduced using a polymerization initiator. -15- 201236867 The fluororesin containing an adhesive functional group is a polymer having an adhesive functional group only at the end of the main chain, and is based on the reason that the mechanical properties and chemical resistance are not significantly lowered, or the productivity and cost are It is advantageous, but the number of adhesive functional groups is affected by the molecular weight, and there is a disadvantage that the maximum content of the content has an upper limit. When the fluororesin having an adhesive functional group has an adhesive functional group at the side of the side chain, it is preferable to increase the amount of the adhesive functional group to some extent to improve the adhesion. The method of introducing the above-mentioned adhesive functional group at the end of the side chain may be carried out by copolymerizing a monomer having an adhesive functional group as described above, or may be introduced by a graft reaction after polymerization. When an adhesive functional group is introduced by a graft reaction, a radical such as an organic peroxide which reacts with a substance having an unsaturated bond and an adhesive functional group in the molecule can be reacted with respect to a resin which is completely free of a functional group. Further, introduction or "copolymerization of a monomer having a relatively stable functional group, reaction of a functional group after polymerization to form a functional group having high reactivity, and introduction of an adhesive functional group therein. In the first layer of the present invention, the fluororesin containing the adhesive functional group has an adhesive functional group '100 mol% relative to the total polymerization unit of the fluororesin constituting the adhesive functional group, preferably 005~1() Moer% 'better 0.05~5 mol%' and better for 02~2 Moer 0/〇. In the second laminate of the present invention, the adhesive functional group of the fluororesin containing the adhesive functional group has a molar % of the total polymerizable monomer relative to the fluororesin constituting the adhesive functional group. 〇 2~1〇% of the ear. By making the adhesive functional group of 201236867 in the above range, the adhesion of the layer (B-2) and the layer (C) is extremely excellent, and accordingly, the initial high adhesion strength of the bonding surface as a whole without unevenness can be maintained. High adhesion strength after long-term use. With this, the laminate is excellent in impact resistance and mechanical strength as a whole. In the second laminate of the present invention, the adhesive functional group is appropriately selected depending on the type, shape, adhesion purpose, use, and the required adhesive force of the laminated material, the type of the fluororesin and the adhesion method. However, it is preferably from 0.2 to 5 mol%, more preferably from 0.2 to 2 mol%, based on 1% by mole of the total polymerization unit of the fluororesin constituting the adhesive functional group. The ratio of the above adhesive functional groups can be determined by the method of N M R or IR. The above-mentioned adhesive functional group is exemplified by a functional group having an amino group, a hydroxyl group, an epoxy group, a nitrile group or a carbonyl group. The above carbonyl group is a divalent group of carbon composed of a carbon-oxygen double bond, and is represented by -c(= 〇)-. The above functional group having a carbonyl group is exemplified by, for example, a carbonate group, a carboxylic acid halide group (halocarbenyl group), a decyl group, a carboxyl group, an ester group [-C(=0)0-], an acid anhydride group [-c ( = 0)0-c( = 0)_], isocyanate, guanamine, fluorenylene [-C(=0)-NH-C(= 0)_], urethane group [ -NH-C(=0)0-], aminomethyl hydrazino [NH2-C(= 0)_], amine methyl methoxy [NH2-C(= 〇) 〇-], urea-based [NH2-C ( = 〇)-NH-], oxalylamine [nh2-c(=o)_c(<0)-] and other chemical structures. a hydrogen atom bonded to a nitrogen atom such as a guanamine group, a guanidino group, a urethane group, an amine carbaryl group, an amine mercapto group, a ureido group or a sulfhydryl group, for example, Substituted by a hydrocarbon group such as an alkyl group. -17- 201236867 The above-mentioned adhesive functional group is preferably an amine group, a decylamine, an amine carbenyl group, a hydroxyl group, a carboxyl group, a carboxylic acid halide group, an ester group, an acid anhydride, a carbonate group, an epoxy group, At least one selected from the group consisting of a nitrile group and an isocyanate group. The above-mentioned adhesive functional group is more preferably at least one selected from the group consisting of an epoxy group, a group, and a carboxyl group, and more preferably a carboxyl group. In the present invention, the fluorine-containing functional group constituting the above layer (C) The fat is a polymer or copolymer having at least one repeating unit derived from a fluorine-containing ethylenic monomer. The fluororesin may be one obtained by polymerizing only a fluorine-containing ethylenic monomer, and may be a mixture of a fluorine-containing ethylenic monomer and an ethylenic monomer having no fluorine atom. In the present invention, the fluororesin layer may be one containing the above-mentioned fluororesin or two or more. The fluororesin containing an adhesive functional group preferably has tetrafluoroethylene [TFE], vinylidene fluoride [VdF], chlorotrifluoroethylene [CTFE], fluorinated ethylene [VF], hexafluoropropylene [HFP], Hexafluoroisobutane [HFIB], CHfCX^CFJnX, where X1 is Η or F, X2 is H, F is 11 and 11 is an integer from 1 to 10), and CFfCF-ORf1 (wherein Rf1) a perfluoroalkyl group having a carbon number of 1 to 8 and a perfluoro(alkyl vinyl group) [PAVE], and a CF2 = CF-OCH2-Rf2 (wherein, Rf2 is a perfluoroalkyl group having a carbon number of 1) a group consisting of an alkyl perfluorovinyl ether derivative, trifluoroethylene, trifluoropropene, tetrafluoropropene, pentafluoropropene, trifluorobutene, tetrafluoroisoene, fluorinated vinyl ether containing iodine At least one monomer unit mainly comprising a monomer is selected. The fluororesin may also have an ethylene [Et], a propyl group, a hydroxy eucalyptus, an olefin, an alkylene, a C1 7 ether, a pentene fluorocarbon, a long chain olefin, and an alkyl ethene. The polymerization unit in which at least one monomer selected from the group consisting of ethers is a fluorine-free monomer.

氟樹脂更好爲含有由TFE、HFP ' PAVE、CTFE及VF 所組成群組選出之至少一種單體爲主之聚合單位之共聚物 。氟樹脂異亦較好爲具有以Et爲主之聚合單位作爲不含 氟之單體之共聚物。 上述PAVE列舉爲全氟(甲基乙烯基醚)[PMVE]、全氟 (乙基乙烯基酸)[PEVE]、全氟(丙基乙烯基醚)[PPVE]、全 氟(丁基乙烯基醚等。其中,更好爲 PMVE、PEVE或 PPVE。 上述烷基全氟乙烯基醚衍生物較好爲Rf2爲碳數1〜3 之權氟烷基者,更好爲CF2 = CF-OCH2-CF2CF3。 本說明書中,上述「聚合單位」意指氟樹脂之分子構 造上之一部分,且基於對應單體之部分》 上述含黏著性官能基之氟樹脂之主鏈較好爲由 TFE/HFP 共聚物[FEP]、TFE/PAVE 共聚物[PFA]、Et/TFE 共聚物、Et/TFE/HFP共聚物、聚氯三氟乙烯[pcTFE]、 CTFE/TFE共聚物、Et/CTFE共聚物、TFE/VdF共聚物、 ^ VdF/HFP/TFE共聚物、VdF/HFP共聚物、及聚氟化乙烯 [PVF]所組成群組選出之至少一種。上述共聚物亦可爲具 有可與構成各共聚物之單體共聚合之其他聚合單位者,較 好爲例如具有源自具有黏著性官能基之單體之聚合單位者· 〇 又,本說明書中’如上述,記載爲「TFE/HFP共聚物 -19- 201236867 」時,意指含有以TFE爲主之聚合單位(TFE單位)與以 HFP爲主之聚合單位(HFP單位)之共聚物。關於其他共聚 物亦同。 上述含黏著性官能基之氟樹脂較好爲具有源自含黏著 性官能基之單體[α]之聚合單位者。若爲具有源自含黏著 性官能基之單體[α]之聚合單位者,則可容易地調整黏著 性官能基之含量》 至於上述單體[α]爲具有上述黏著性官能基之單體, 且只要是可與構成含黏著性官能基之氟樹脂之其他單體共 聚合者即無特別限制。 上述單體[α]列舉爲例如以下所示之單體。 具有胺基之單體列舉爲例如烯丙基胺、甲基丙烯酸 2-胺基甲酯、甲基丙烯酸甲基胺基乙酯、甲基丙烯酸第三 丁基胺基乙酯、胺基苯乙烯等。其中,較好爲由烯丙基胺 、及胺基苯乙烯所組成群組選出之至少一種單體。 至於具有醯胺基之單體列舉爲例如Ν,Ν-二甲基丙烯 醯胺、Ν·第三丁基丙烯醯胺、Ν-(丁氧基甲基)丙烯醯胺、 Ν-烯基乙醯胺、Ν-乙烯基甲醯胺等。其中,較好爲由 Ν,Ν-二甲基丙烯醯胺、及Ν-乙烯基乙醯胺所組成群組選 出之至少一種單體。 具有胺甲醯基之單體較好爲例如由丙烯醯胺、烯丙基 脲所組成群組選出之至少一種單體。 具有羥基之單體列舉爲烯丙基醇、4-戊烯-1-醇、4-羥 基丁基乙烯基醚、Ν-羥甲基丙烯醯胺、Ν-羥甲基甲基丙烯 -20- 201236867 醯胺等。其中,較好爲由烯丙基醇、及4-戊烯-1-醇所組 成群組選出之至少一種單體。又,具有羥基之單體較好爲 使乙酸乙烯酯共聚合後,經皂化反應轉換成羥基者。 具有羧基之單體列舉爲3 -丁烯酸、4 -戊烯酸' 5 -己烯 酸、丙烯酸、甲基丙烯酸、馬來酸單甲酯、巴豆酸等具有 一個羧基者’又亦列舉爲馬來酸、富馬酸、衣康酸、檸康 酸等一分子中具有兩個竣基者。其中,以由3 -丁稀.酸、4-戊烯酸、5 -己烯酸、丙烯酸、甲基丙烯酸、馬來酸、及巴 豆酸所組成群組選出之至少一種單體較佳。 具有羧基之單體更好爲以下述式(1)表示之不飽和羧 酸: CH2 = CH-(CH2)n-COOH (1) (式中,η爲1〜15之整數)。 其中,式(1)中之η較好爲2〜10之整數,更好爲由戊 烯酸、十一碳烯酸、丁烯酸、己烯酸、癸烯酸、庚烯酸、 辛烯酸、及壬烯酸所組成群組選出之至少一種不飽和羧酸 ,更好爲由戊烯酸及十一碳烯酸所組成群組選出之至少一 種不飽和羧酸。 至於具有酸酐基之單體列舉爲馬來酸酐、衣康酸酐、 檸康酸酐、雙環[2,2,1]庚-2-烯_5,6_二羧酸酐等。其中, 較好爲由馬來酸酐、衣康酸酐、及檸康酸酐所組成群組選 出之至少一種單體。 -21 - 201236867 至於具有酯基之單體列舉爲乙酸乙烯酯、丙烯酸甲酯 、丙烯酸乙酯、丙烯酸正丁酯、甲基丙烯酸甲酯等。其中 ,較好爲由乙酸乙烯酯、丙烯酸甲酯、甲基丙烯酸甲酯所 組成群組選出之至少一種單體。 至於具有碳酸酯基之單體列舉爲碳酸烯丙酯甲酯、碳 酸烯丙酯乙酯'碳酸伸乙烯酯、碳酸乙烯酯伸乙酯等。其 中,較好爲由碳酸烯丙酯甲酯、碳酸烯丙酯乙酯所組成群 組選出之至少一種單體。 至於具有環氧基之單體列舉爲烯丙基縮水甘油醚、甲 基丙烯酸縮水甘油酯、丙烯酸縮水甘油酯、2-乙烯基環氧 乙烷、2-甲基-2-乙烯基環氧乙烷.、1,2-環氧基-5-己烯、 1,2-環氧基-9-癸烯等。其中,較好爲由烯丙基縮水甘油醚 、甲基丙烯酸縮水甘油酯、丙烯酸縮水甘油酯、2 -乙烯基 環氧乙烷所組成群組選出之至少一種單體。 具有腈基之單體列舉爲丙烯腈、烯丙基氰化物、氰基 丙烯酸酯、氰基甲基丙烯酸酯等。其中,較好爲由丙烯睛 、烯丙基氰化物所組成群組選出之至少一種單體。 具有異氰酸醋基之單體較好爲由乙稀基異氰酸酯、稀 丙基異氰酸酯所組成群組選出之至少一種單體。 羧酸鹵化物基較好爲藉由使含有羧基之氟樹脂與亞硫 醯氯或草醯氯等拉電子之鹵化劑反應,使羧基轉換而導入 。具有羧酸鹵化物基之聚合單位較好爲將具有羧基之聚合 單位之羧基轉化成羧酸鹵化物基而成者。 含有黏著性官能基之單體[a]較好爲由具有胺基之單The fluororesin is more preferably a copolymer containing a polymerization unit mainly composed of at least one monomer selected from the group consisting of TFE, HFP 'PAVE, CTFE and VF. The fluororesin is also preferably a copolymer having a polymerization unit mainly composed of Et as a monomer containing no fluorine. The above PAVE is listed as perfluoro(methyl vinyl ether) [PMVE], perfluoro(ethyl vinyl acid) [PEVE], perfluoro(propyl vinyl ether) [PPVE], perfluoro(butyl vinyl) Ether, etc. Among them, more preferably PMVE, PEVE or PPVE. The above alkyl perfluorovinyl ether derivative is preferably a fluoroalkyl group having a carbon number of 1 to 3, and more preferably CF2 = CF-OCH2- CF2CF3. In the present specification, the above "polymerization unit" means a part of the molecular structure of the fluororesin and is based on a part of the corresponding monomer. The main chain of the above-mentioned fluororesin containing an adhesive functional group is preferably copolymerized by TFE/HFP. [FEP], TFE/PAVE copolymer [PFA], Et/TFE copolymer, Et/TFE/HFP copolymer, polychlorotrifluoroethylene [pcTFE], CTFE/TFE copolymer, Et/CTFE copolymer, TFE At least one selected from the group consisting of: VdF copolymer, ^VdF/HFP/TFE copolymer, VdF/HFP copolymer, and polyfluorinated ethylene [PVF]. The above copolymer may also have a copolymerizable composition. The other polymerization unit in which the monomer is copolymerized is preferably, for example, a polymerization unit having a monomer derived from an adhesive functional group. In the above description, as described above, "TFE/HFP copolymer-19-201236867" means copolymerization of a polymerization unit (TFE unit) mainly composed of TFE and a polymerization unit (HFP unit) mainly composed of HFP. The same is true for the other copolymers. The fluororesin having an adhesive functional group is preferably one having a polymerization unit derived from the monomer [α] containing an adhesive functional group. The monomer of the monomer [α] can easily adjust the content of the adhesive functional group. The above monomer [α] is a monomer having the above-mentioned adhesive functional group, and as long as it is compatible with the composition. The other monomer copolymer of the functional group fluororesin is not particularly limited. The above monomer [α] is exemplified by the following monomers. The monomer having an amine group is exemplified by, for example, allylamine, methacrylic acid. 2-aminomethyl ester, methylaminoethyl methacrylate, tert-butylaminoethyl methacrylate, aminostyrene, etc. Among them, allylamine and aminobenzene are preferred. At least one monomer selected from the group consisting of ethylene. The monomer of the amine group is exemplified by, for example, hydrazine, hydrazine-dimethyl decylamine, hydrazine, tert-butyl acrylamide, hydrazine-(butoxymethyl) acrylamide, decyl-ethenylamine, Ν-vinyl formamide, etc. Among them, at least one monomer selected from the group consisting of ruthenium, osmium-dimethyl decylamine, and fluorene-vinyl acetamide is preferred. The monomer is preferably at least one monomer selected from the group consisting of acrylamide and allyl urea. The monomer having a hydroxyl group is exemplified by allyl alcohol, 4-penten-1-ol, 4- Hydroxybutyl vinyl ether, hydrazine-hydroxymethyl acrylamide, hydrazine-hydroxymethyl methacryl-20 - 201236867 decylamine, and the like. Among them, at least one monomer selected from the group consisting of allyl alcohol and 4-penten-1-ol is preferred. Further, the monomer having a hydroxyl group is preferably one obtained by copolymerizing vinyl acetate and then converting it into a hydroxyl group by a saponification reaction. The monomer having a carboxyl group is exemplified by 3-butenoic acid, 4-pentenoic acid '5-hexenoic acid, acrylic acid, methacrylic acid, monomethyl maleate, crotonic acid and the like having one carboxyl group'. Maleic acid, fumaric acid, itaconic acid, citraconic acid and the like have two sulfhydryl groups. Among them, at least one monomer selected from the group consisting of 3-butyric acid, 4-pentenoic acid, 5-hexenoic acid, acrylic acid, methacrylic acid, maleic acid, and crotonic acid is preferred. The monomer having a carboxyl group is more preferably an unsaturated carboxylic acid represented by the following formula (1): CH2 = CH-(CH2)n-COOH (1) (wherein η is an integer of from 1 to 15). Wherein, η in the formula (1) is preferably an integer of from 2 to 10, more preferably from pentenoic acid, undecylenic acid, crotonic acid, hexenoic acid, decenoic acid, heptenoic acid, octene The at least one unsaturated carboxylic acid selected from the group consisting of acid and decenoic acid is more preferably at least one unsaturated carboxylic acid selected from the group consisting of pentenoic acid and undecylenic acid. The monomer having an acid anhydride group is exemplified by maleic anhydride, itaconic anhydride, citraconic anhydride, bicyclo[2,2,1]hept-2-ene-5,6-dicarboxylic anhydride, and the like. Among them, at least one monomer selected from the group consisting of maleic anhydride, itaconic anhydride, and citraconic anhydride is preferred. -21 - 201236867 The monomer having an ester group is exemplified by vinyl acetate, methyl acrylate, ethyl acrylate, n-butyl acrylate, methyl methacrylate or the like. Among them, at least one monomer selected from the group consisting of vinyl acetate, methyl acrylate, and methyl methacrylate is preferred. The monomer having a carbonate group is exemplified by allyl carbonate, propylene carbonate ethyl carbonate, ethylene carbonate, ethyl acetate, and the like. Among them, at least one monomer selected from the group consisting of methyl allyl carbonate and ethyl allyl carbonate is preferred. The monomers having an epoxy group are exemplified by allyl glycidyl ether, glycidyl methacrylate, glycidyl acrylate, 2-vinyloxirane, 2-methyl-2-vinyl epoxy B. Alkyl, 1,2-epoxy-5-hexene, 1,2-epoxy-9-decene, and the like. Among them, at least one selected from the group consisting of allyl glycidyl ether, glycidyl methacrylate, glycidyl acrylate, and 2-vinyloxirane is preferred. The monomer having a nitrile group is exemplified by acrylonitrile, allyl cyanide, cyanoacrylate, cyanomethacrylate or the like. Among them, at least one monomer selected from the group consisting of acrylonitrile and allyl cyanide is preferred. The monomer having an isocyanato group is preferably at least one monomer selected from the group consisting of ethylene isocyanate and propyl isocyanate. The carboxylic acid halide group is preferably introduced by reacting a fluororesin containing a carboxyl group with a halogenating agent such as sulfinium chloride or hydrazine chloride to convert a carboxyl group. The polymerization unit having a carboxylic acid halide group is preferably one obtained by converting a carboxyl group having a polymerization unit of a carboxyl group into a carboxylic acid halide group. The monomer [a] having an adhesive functional group is preferably a single one having an amine group

-22- SS 201236867 體、具有醯胺基之單體、具有胺甲醯基之單體、具有羥基 之單體、具有羧基之單體、具有酸酐基之單體、具有酯基 之單體、具有碳酸酯基之單體、具有環氧基之單體、具有 腈基之單體、及具有羧酸鹵化物基之單體所組成群組選出 之至少一種,更好爲由具有環氧基之單體、具有羥基之單 體、及具有羧基之單體所組成群組選出之至少一種,又更 好爲具有羧基之單體,最好爲以式(1)表示之不飽和羧酸 〇 上述含黏著性官能基之氟樹脂較好爲由TFE/HFP/單 體[α]共聚物、TFE/PAVE/單體[α]共聚物、Et/TFE/單體[α] 共聚物、Et/TFE/HFP/單體[α]共聚物、CTFE/單體[α]共聚 物、CTFE/TFE/單體[α]共聚物、Et/CTFE/單體[α]共聚物 、偏氟化乙烯/單體[α]共聚物、TFE/VdF/單體[α]共聚物、 VdF/HFP/TFE/單體[α]共聚物、VdF/HFP/單體[α]共聚物、 及氟化乙烯[PVF]/單體[α]共聚物所組成群組選出之至少 一種。更好爲由Et/TFE/單體[α]共聚物、及Et/TFE/HFP/ 單體[α]共聚物所組成群組選出之至少一種,更好爲 Et/TFE/HFP/單體[α]共聚物。 本發明之第一層合物中,具有源自上述單體[α]之聚 合單位之含黏著性官能基之氟樹脂相對於構成含黏著性官 能基之氟樹脂之全聚合單位100莫耳%,較好爲〇.〇5〜10 莫耳%,更好爲〇.〇5~5莫耳%,又更好爲0.2〜2莫耳%。 本發明之第二層合物中,具有源自上述單體[α]之聚 合單位之含黏著性官能基之氟樹脂,其源自單體[α]之聚 -23- 201236867 合單位相對於構成含黏著性官能基之氟樹脂之全聚合單位 100莫耳%,較好爲0.2~10莫耳%。更好爲0.2〜5莫耳% ,又更好爲0.2〜2莫耳%。 藉由使源自單體[α]之聚合單位爲上述範圍,可調整 黏著性官能基,獲得層(Β-1)或層(Β-2)與層(C)極優異之黏 著性。因此,伴隨於此,作爲層合物整體成爲耐衝擊性、 機械強度極優異之層合物。 本發明中,上述含黏著性官能基之氟樹脂之融點較好 爲 120~240°C。更好爲 150~230t:,又更好爲 150〜220°C, 最好爲140〜20(TC。藉由使融點在上述範圍,使與改質聚 烯烴之黏著性更爲優異。 上述含黏著性官能基之氟樹脂之融點較好爲所含有之 黏著性官能基之分解溫度以下。更好爲比所含有之黏著性 官能基之分解溫度低5°C以上之溫度。藉由使融點爲上述 範圍,使成形加工時之安定性更爲優異。 黏著性官能基之分解溫度可利用熱重量測定(TG)、或 者示差熱-熱重量同時測定(TG-DTA)之方法決定。 上述含黏著性官能基之氟樹脂之分子量較好在可展現 所得層合物之機械特性、藥液阻隔性等之範圍。例如,以 熔融流速[MFR]作爲分子量之指標,氟樹脂一般之成形溫 度範圍約23 0~300°C之範圍之任意溫度中之MFR較好爲 0.5〜1〇〇 g/l〇 分鐘。 本說明書中,各樹脂之融點係使用DSC裝置(Seiko 公司製造),以1〇 °C/分鐘之速度升溫時之融解熱曲線中之 -24- 201236867 極大値所對應之溫度而求得者,MFR爲使用熔融指數測 定儀(東洋精機製作所公司製造),在各溫度、5kg荷重下 ,自直徑2mm、長度8mm之噴嘴於測定單位時間(10分 鐘)流出之聚合物之重量(g)者。 上述含黏著性官能基之氟樹脂可藉由懸浮聚合、溶液 聚合、乳化聚合、塊狀聚合等過去習知之聚合方法獲得。 上述聚合中,溫度、壓力等各條件、聚合起始劑或其他添 加劑可依據所需氟樹脂之組成或量適當設定。 由上述含黏著性官能基之氟樹脂所形成之層(C),就 提高層間黏著性、提高所得層合物之耐衝擊性或強度方面 而言,其表面亦可經黏著性表面處理。 本發明中之黏著性表面處理並無特別限制,列舉爲例 如蝕刻處理、電漿處理、電暈處理、光化學處理等習知之 技術。 上述黏著性表面處理可依據使用之氟樹脂組成等設定 適當條件而進行。 構成上述層(A)之聚烯烴樹脂列舉爲例如乙烯之均聚 物、或乙烯與其他一種以上之α-烯烴具體爲丙烯、1-丁烯 、4-甲基-1-戊烯、1-己烯、1_辛烯、1-癸烯等之共聚物。 至於聚烯烴樹脂列舉爲丙烯均聚物、丙烯-乙烯嵌段共聚 物' 低密度聚乙烯 '中密度聚乙烯、高密度聚乙烯、超高 密度聚乙烯等。聚烯烴樹脂較好熔融流速(MFR)爲 0.01〜100g/10分鐘,密度爲0.850〜0.980g/cm3。其中上述 聚烯烴樹脂更好爲高密度聚乙烯。 -25- 201236867 本發明之第二層合物爲層(C)之單面上層合層(B-2)者 亦即,爲層(C)與層(B-2)直接接觸之層。 構成上述層(B-2)之改質聚烯烴樹脂列舉爲將例如乙 烯之均聚物、或乙烯與其他一種以上之α-烯烴具體爲丙 烯' 1-丁烯、4-甲基-1-戊烯、1-己烯、1·辛烯、1-癸烯等 之共聚物予以改質者。改質聚烯烴樹脂較好熔融流速 (MFR)爲 〇.〇1 〜l〇〇g/10 分鐘,密度爲 〇.850~0.980g/cm3。 至於改質聚烯烴樹脂較好爲使由丙烯均聚物、丙烯·乙烯 嵌段共聚物、低密度聚乙烯、中密度聚乙烯、高密度聚乙 烯、及超高密度聚乙烯所成群組選出之至少一種予以改質 者,更好爲將高密度聚乙烯改質者。 構成上層(B-2)之改質聚烯烴樹脂具有官能基。構成 層(B-2)之改質聚烯烴樹脂所具有之官能基只要是對構成 上述層(C)之含黏著性官能基之氟樹脂所具有之黏著性官 能基顯示反應性之官能基即無特別限制,較好爲例如由胺 基、醯胺基、胺甲醯基、羥基、羧基、羧酸鹵化物基、酯 基、酸酐基、碳酸酯基、環氧基、腈基及異氰酸酯基所組 成群組選出之至少一種。更好爲由環氧基、胺基及異氰酸 酯基所組成群組選出之至少一種。 構成上述層(B-2)之上述改質聚烯烴樹脂較好爲使自 丙烯均聚物、丙烯-乙烯嵌段共聚物、低密度聚乙烯、中 密度聚乙烯、高密度聚乙烯、及超高密度聚乙烯所組成群 組選出之至少一種改質成具有由胺基、醯胺基、胺甲醯基 、羥基、羧基、羧酸鹵化物基、酯基、酸酐基 '碳酸酯基-22- SS 201236867 A monomer having a mercapto group, a monomer having an amine methyl group, a monomer having a hydroxyl group, a monomer having a carboxyl group, a monomer having an acid anhydride group, a monomer having an ester group, At least one selected from the group consisting of a monomer having a carbonate group, a monomer having an epoxy group, a monomer having a nitrile group, and a monomer having a carboxylic acid halide group, more preferably having an epoxy group At least one selected from the group consisting of a monomer, a monomer having a hydroxyl group, and a monomer having a carboxyl group, and more preferably a monomer having a carboxyl group, preferably an unsaturated carboxylic acid represented by the formula (1) The above fluororesin containing an adhesive functional group is preferably a TFE/HFP/monomer [α] copolymer, a TFE/PAVE/monomer [α] copolymer, an Et/TFE/monomer [α] copolymer, and an Et /TFE/HFP/monomer [α] copolymer, CTFE/monomer [α] copolymer, CTFE/TFE/monomer [α] copolymer, Et/CTFE/monomer [α] copolymer, partial fluorination Ethylene/monomer [α] copolymer, TFE/VdF/monomer [α] copolymer, VdF/HFP/TFE/monomer [α] copolymer, VdF/HFP/monomer [α] copolymer, and fluorine Group of ethylene [PVF] / monomer [α] copolymer Groups of at least one selected. More preferably, at least one selected from the group consisting of Et/TFE/monomer [α] copolymer and Et/TFE/HFP/monomer [α] copolymer, more preferably Et/TFE/HFP/monomer [α] copolymer. In the first laminate of the present invention, the fluororesin having an adhesive functional group derived from the polymerization unit of the above monomer [α] is 100 mol% with respect to the total polymerization unit of the fluororesin constituting the adhesive functional group. Preferably, it is 〇.〇5~10 mol%, more preferably 〇.〇5~5 mol%, and more preferably 0.2~2 mol%. In the second laminate of the present invention, the fluororesin having an adhesive functional group derived from the polymerization unit of the above monomer [α] is derived from the poly-23-201236867 unit of the monomer [α] relative to The total polymerization unit constituting the fluororesin having an adhesive functional group is 100 mol%, preferably 0.2 to 10 mol%. More preferably 0.2 to 5 mol%, and even more preferably 0.2 to 2 mol%. By setting the polymerization unit derived from the monomer [α] to the above range, the adhesive functional group can be adjusted to obtain an extremely excellent adhesion between the layer (Β-1) or the layer (Β-2) and the layer (C). Therefore, as a whole, the laminate has excellent impact resistance and mechanical strength. In the present invention, the melting point of the above-mentioned fluororesin containing an adhesive functional group is preferably from 120 to 240 °C. More preferably, it is 150 to 230 t: and more preferably 150 to 220 ° C, preferably 140 to 20 (TC. By making the melting point within the above range, the adhesion to the modified polyolefin is more excellent. The melting point of the fluororesin containing the adhesive functional group is preferably at least the decomposition temperature of the adhesive functional group contained therein, more preferably 5 ° C or more lower than the decomposition temperature of the adhesive functional group contained. The melting point is in the above range, and the stability during molding processing is further improved. The decomposition temperature of the adhesive functional group can be determined by thermogravimetric measurement (TG) or differential thermal-thermal weight simultaneous measurement (TG-DTA). The molecular weight of the above-mentioned fluororesin containing an adhesive functional group is preferably in a range which exhibits mechanical properties, chemical barrier properties, etc. of the obtained laminate. For example, a melt flow rate [MFR] is used as an index of molecular weight, and a fluororesin is generally used. The MFR at any temperature in the range of the forming temperature range of about 23 to 300 ° C is preferably 0.5 to 1 〇〇 g / l 〇 minutes. In the present specification, the melting point of each resin is a DSC device (manufactured by Seiko Corporation). When heating at a rate of 1 ° C / min In the melting heat curve, the temperature is determined by the temperature corresponding to the maximum 値 - - , , , , , , , , , , , , 熔融 熔融 熔融 熔融 熔融 熔融 熔融 熔融 熔融 熔融 熔融 熔融 熔融 熔融 熔融 熔融 熔融 熔融 熔融 熔融 熔融 熔融 熔融 熔融 熔融 熔融 熔融 熔融 熔融 熔融 熔融 熔融 熔融 熔融 熔融 熔融 熔融The weight (g) of the polymer flowing out of the nozzle per unit time (10 minutes). The fluororesin containing the adhesive functional group may be a conventional polymerization method such as suspension polymerization, solution polymerization, emulsion polymerization, or bulk polymerization. In the above polymerization, various conditions such as temperature, pressure, polymerization initiator or other additives may be appropriately set depending on the composition or amount of the desired fluororesin. Layer (C) formed of the above-mentioned fluororesin containing an adhesive functional group In terms of improving the adhesion between the layers and improving the impact resistance or strength of the obtained laminate, the surface thereof may also be subjected to an adhesive surface treatment. The adhesive surface treatment in the present invention is not particularly limited and is exemplified by etching treatment, for example. , conventional techniques such as plasma treatment, corona treatment, and photochemical treatment. The above adhesive surface treatment can be based on the composition of the fluororesin used. The polyolefin resin constituting the layer (A) is exemplified by, for example, a homopolymer of ethylene or ethylene and one or more other α-olefins, specifically propylene, 1-butene, 4-methyl-1- a copolymer of pentene, 1-hexene, 1-octene, 1-decene, etc. The polyolefin resin is exemplified by a propylene homopolymer, a propylene-ethylene block copolymer, a low density polyethylene, a medium density polyethylene. , high-density polyethylene, ultra-high-density polyethylene, etc. The polyolefin resin preferably has a melt flow rate (MFR) of 0.01 to 100 g/10 min and a density of 0.850 to 0.980 g/cm 3 , wherein the polyolefin resin is preferably a high density. Polyethylene. -25- 201236867 The second laminate of the present invention is a one-side laminate layer (B-2) of layer (C), that is, the layer (C) is in direct contact with the layer (B-2). Floor. The modified polyolefin resin constituting the above layer (B-2) is exemplified by a homopolymer such as ethylene or ethylene and one or more other α-olefins specifically propylene '1-butene, 4-methyl-1- A copolymer of pentene, 1-hexene, 1-octene, 1-decene or the like is modified. The modified polyolefin resin preferably has a melt flow rate (MFR) of 〇.〇1 to l〇〇g/10 minutes and a density of 850.850 to 0.980 g/cm3. The modified polyolefin resin is preferably selected from the group consisting of propylene homopolymer, propylene/ethylene block copolymer, low density polyethylene, medium density polyethylene, high density polyethylene, and ultra high density polyethylene. At least one of those who have been upgraded is better at upgrading high-density polyethylene. The modified polyolefin resin constituting the upper layer (B-2) has a functional group. The functional group of the modified polyolefin resin constituting the layer (B-2) is a functional group which exhibits reactivity with respect to the adhesive functional group of the fluororesin of the adhesive functional group constituting the layer (C). It is not particularly limited, and is preferably, for example, an amine group, a mercaptoamine group, an amine mercapto group, a hydroxyl group, a carboxyl group, a carboxylic acid halide group, an ester group, an acid anhydride group, a carbonate group, an epoxy group, a nitrile group, and an isocyanate group. At least one of the selected groups is selected. More preferably, it is at least one selected from the group consisting of an epoxy group, an amine group, and an isocyanate group. The modified polyolefin resin constituting the above layer (B-2) is preferably a self-propylene homopolymer, a propylene-ethylene block copolymer, a low density polyethylene, a medium density polyethylene, a high density polyethylene, and a super At least one selected from the group consisting of high density polyethylene is modified to have an amine group, a mercaptoamine group, an amine mercapto group, a hydroxyl group, a carboxyl group, a carboxylic acid halide group, an ester group, and an acid anhydride group 'carbonate group.

-26- S 201236867 、環氧基、腈基及異氰酸酯基所組成群組選出之至少一種 基者。 其中上述改質之聚烯烴樹脂中,較佳爲由不飽和羧酸 改質之聚乙烯、環氧改質之聚乙烯、胺(nh2)改質之聚乙 烯、及異氰酸酯改質之聚乙烯所組成群組選出之至少一種 改質聚乙烯,更好爲由環氧改質之聚乙烯、胺(NH2)改質 之聚乙烯及以氰酸酯改質之聚乙烯所組成群組選出之至少 一種改質聚乙烯。 上述不飽和羧酸改質之聚乙烯可藉由在自由基產生劑 存在下,使聚乙烯與不飽和羧酸及/或其衍生物經接枝處 理而獲得》 上述不飽和羧酸改質之聚乙烯之接枝量較好爲 0_01〜10重量%,更好爲0.1~5重量%。接枝量若在上述範 圍,則接著性變得更好。 上述不飽和羧酸改質之聚乙烯較好密度爲 0.85 0~0‘980 g/cm3,更好爲 0.870 〜0.970g/cm3» 密度爲 0.85 0g/cm3以上時,製品顆粒不易阻塞故較佳^ 上述不飽和羧酸及其衍生物列舉爲丙烯酸、馬來酸、 富馬酸、四氫苯二甲酸、衣康酸、檸康酸、巴豆酸、異巴 豆酸、納迪克酸(商品名)(挂-順式-雙環[2,2,1]庚-5-烯_ 2,3-二羧酸)等不飽和羧酸、及該等之衍生物(例如,醯國 、醯胺、醯亞胺、酸酐、酯等)。亦列舉爲例如丙二醯氯 、馬來醯亞胺、馬來酸酐、檸康酸酐' 馬來酸單甲酯、馬 來酸二甲酯、馬來酸縮水甘油酯等。-26-S 201236867, at least one selected from the group consisting of epoxy, nitrile and isocyanate groups. Among the above modified polyolefin resins, polyethylene modified with an unsaturated carboxylic acid, epoxy modified polyethylene, amine (nh2) modified polyethylene, and isocyanate modified polyethylene are preferred. The at least one modified polyethylene selected from the group is preferably selected from the group consisting of epoxy modified polyethylene, amine (NH2) modified polyethylene, and cyanate modified polyethylene. A modified polyethylene. The above unsaturated carboxylic acid modified polyethylene can be obtained by grafting a polyethylene with an unsaturated carboxylic acid and/or a derivative thereof in the presence of a radical generating agent. The graft amount of the polyethylene is preferably from 0 to 01% by weight to 10% by weight, more preferably from 0.1 to 5% by weight. If the graft amount is in the above range, the adhesion becomes better. The above unsaturated carboxylic acid modified polyethylene preferably has a density of 0.85 0 to 0'980 g/cm3, more preferably 0.870 to 0.970 g/cm3». When the density is 0.85 0g/cm3 or more, the product particles are not easily blocked, so that it is preferred. ^ The above unsaturated carboxylic acid and its derivatives are listed as acrylic acid, maleic acid, fumaric acid, tetrahydrophthalic acid, itaconic acid, citraconic acid, crotonic acid, isocrotonic acid, nadic acid (trade name) Unsaturated carboxylic acids such as (hang-cis-bicyclo[2,2,1]hept-5-ene-2,3-dicarboxylic acid), and derivatives thereof (for example, samarium, decylamine, hydrazine) Imine, anhydride, ester, etc.). Also listed are, for example, propylene dichloride, maleimide, maleic anhydride, citraconic anhydride, monomethyl maleate, dimethyl maleate, glycidyl maleate, and the like.

S -27- 201236867 上述不飽和羧酸及其衍生物較好爲一元不飽和羧酸、 以及二元不飽和羧酸、及由該等之金屬鹽、醯胺、醯亞胺 、酯或酸酐所組成群組選出之至少一種。 上述一元不飽和羧酸一般爲碳數20個以下,較好爲 15個以下。且上述一元不飽和羧酸之衍生物通常爲碳數 20個以下,較好爲15個以下》 上述二元不飽和羧酸一般爲碳數30個以下,較好爲 25個以下。又,上述二元不飽和羧酸之衍生物通常爲碳 數3 0個以下,較好爲25個以下。 上述不飽和羧酸及其衍生物,其中以由丙烯酸、甲基 丙烯酸、納迪克酸、馬來酸及其酸酐、5-降冰片烯-2,3-二 羧酸及其酸酐、以及甲基丙烯酸縮水甘油酯所組成群組選 出之至少一種,最好爲由馬來酸酐及5 ·降冰片烯酸酐所 組成群組選出之至少一種。 接枝處理時使用之自由基產生劑列舉爲有機過氧化物 、有機過氧酯。例如,使用苯甲醯基過氧化物、二氯苯甲 醯基過氧化物、二枯基過氧化物、二第三丁基過氧化物、 2.5- 二甲基-2,5-二(過氧化物苯甲酸酯)己炔-3、1,4-雙(第 三丁基過氧異丙基)苯、月桂醯基過氧化物、第三丁基過 氧乙酸酯、2,5-二甲基-2,5-二(第三丁基過氧基)己炔-3、 2.5- 二甲基-2,5-二(第三丁基過氧基)己烷、第三丁基過氧 苯甲酸酯、第三丁基過氧苯基乙酸酯、第三丁基過氧異丁 酸酯、第三丁基過氧第二辛酸酯、第三丁基過氧特戊酸酯 、枯基過氧特戊酸酯及第三丁基過氧二乙基乙酸酯,以及 28- 201236867 偶氮化合物,例如偶氮雙異丁腈、二甲基偶氮異丁腈。該 等中較好爲二枯基過氧化物、二第三丁基過氧化物、2,5-二甲基-2,5-二(第三丁基過氧化物)己炔-3、2,5-二甲基-2,5-二(第三丁基過氧基)己烷、1,4-雙(第三丁基過氧基異 丙基)苯等二烷基過氧化物。 其中,作爲自由基產生劑,較好爲有機過氧化物。至 於有機過氧化物以半衰期之分解溫度爲100 °c以上者較佳 。又,有機過氧化物具體較好爲由二枯基過氧化物、苯甲 醯基過氧化物、二第三丁基過氧化物、2,5-二甲基-二(第 三丁基過氧基)己烷、2,5-二甲基-2,5-(第三丁基過氧基)己 烷-3'月桂醯基過氧化物及第三丁基過氧苯甲酸酯等所.組 成群組選出之至少一種。 自由基產生劑之使用比例相對於改質聚烯烴1 〇〇重量 份,通常爲0.001〜1重量份。 上述不飽和羧酸改質之聚烯烴可藉由均勻混合聚乙烯 樹脂、不飽和羧酸及/或其衍生物、自由基產生劑並經處 理而製造。具體而言,列舉爲使用擠出機或班伯里混練機 、捏合機等之熔融混練法,溶解於適當溶劑中之溶液法、 懸浮於適當溶劑中之漿液法、或所謂氣相接枝法等。 上述處理溫度係考慮聚乙烯樹脂之劣化、不飽和羧酸 及/或其衍生物之分解、使用之自由基產生劑之分解溫度 等而適當選擇。例如,上述熔融混練法之情況,通常在 60〜3 5 0 °c之溫度下進行。上述處理溫度較好爲190〜3 50°c ,更好爲200〜300°C。 -29- 201236867 每當製造上述不飽和羧酸改質之聚乙烯時,爲提高其 性能,可採用特開昭62-01 01 07號公報所記載之過去已知 之方法,例如,於接枝改質時或改質後,以環氧化合物、 含胺基或羥基之多官能性化合物處理之方法,進而藉由加 熱或洗淨等去除未反應之單體(不飽和羧酸或其衍生物)或 副產生之諸成分等之方法。 上述環氧改質之聚乙烯可藉由乙烯與含環氧基之不飽 和化合物之共聚合,或藉由在自由基產生劑存在下,使聚 乙烯與含環氧基之不飽和化合物經接枝處理。乙烯與含有 環氧基之不飽和化合物之共聚合可使用在200〜2500巴之 壓力下之自由基聚合法進行。接枝處理可對於溶劑相中 ,或在過氧化物存在下之熔融聚乙烯進行。該接枝處理法 本身爲習知。 含環氧基之不飽和化合物列舉爲例如以下者。 (1) 脂肪族縮水甘油酯及脂肪族縮水甘油醚:例如烯 丙基縮水甘油醚、乙烯基縮水甘油醚、馬來酸縮水甘油酯 、及衣康酸酯、(甲基)丙烯酸縮水甘油酯 (2) 脂環式縮水甘油酯及醚:例如2-環己烯-1-縮水 甘油醱、4,5-二縮水甘油基環己烯-羧酸酯、4-縮水甘油基 環己烯羧酸酯、5-降冰片烯-2-甲基-2-縮水甘油基羧酸酯 、2,3-二縮水甘油基-挂-順式-雙環(2.2.1)-5-庚烯-羧酸酯 聚乙烯經接枝處理時,可對聚乙烯之均聚物或共聚物 進行接枝。 上述環氧改質之聚乙烯亦較好爲乙烯/(甲基)丙烯酸烷 -30- 201236867 酯/含環氧基之不飽和化合物共聚物。該情況下,較好爲 含有40重量%以下,較好5〜40重量%之(甲基)丙烯酸烷 酯,含有10重量%以下,較好含有0.1〜8重量%之含環氧 基之不飽和化合物。含環氧基之不飽和化合物更好爲(甲 基)丙烯酸縮水甘油酯。 至於(甲基)丙烯酸烷酯較好爲由(甲基)丙烯酸甲酯、 丙烯酸乙酯、丙烯酸正丁酯、丙烯酸異丁酯及丙烯酸2-乙基己酯所組成群組選出之至少一種。上述環氧改質之聚 乙烯中,(甲基)丙烯酸烷酯較好爲20〜35重量%。較好 MFI 爲 5〜1 00( 1 90°C/2.16kg 之 g/l〇 分鐘),融點爲 60〜110 °C。上述環氧改質之聚乙烯可藉由使單體經自由基 聚合獲得。 上述聚乙烯可購自一般以顆粒形式銷售之在 2 00〜25 0 0巴之壓力下以自由基聚合製作之市售者。例如 可藉由使用GARVA公司(Gala,美國維吉尼亞州)之水中 切斷法或冷凍粉碎之微顆粒法(microgranulation)而粉末化 上述胺改質之聚乙烯係在自由基產生劑存在下,藉由 使聚乙烯與含多數醯胺基或胺基之多元胺化合物經接枝處 理而獲得。 上述多元胺化合物爲其分子內具有一級胺(R-NH2)、 二級胺(RyNH)、三級胺(R3-N)、或該等之衍生物(例如醯 胺(R-CONH2))之聚合物或共聚物。各式中之r爲烴基, 較好爲由烷基、芳基、芳烷基、烯基及炔基所組成群組選 -31 - 201236867 出之至少一種烴基。更好爲甲基、乙基、丙基、丁基、戊 基、異丙基、異丁基等之碳數1~10,較好爲1〜8,更好爲 1〜5 ’最好爲1〜3之烷基:乙烯基、烯丙基等之碳數2~10 、較好2〜8、更好2~5,最好2〜4之烯基;或苯基、萘基 等之碳數6〜1 0之芳基所組成群組選出之至少一種烴基。 上述多元胺化合物之較佳具體例列舉爲例如舉乙烯基 胺、聚烯丙基胺及芳香族胺。 上述多元胺化合物之分子量較好爲1,000以上,但就 活化處理後之與烯烴反應性等之觀點而言,較好爲更高分 子量。具體而言,較好分子量爲1,000〜200,000,更好分 子量爲3,000〜200,000,最好分子量爲15,000〜200,000。 上述自由基產生劑可利用作爲使不飽和羧酸改質之聚 乙烯經接枝處理時使用者所列舉之自由基產生劑。適用之 自由基產生劑之種類、使用比例等亦相同。又,關於接枝 處理之方法,亦可爲與使不飽和羧酸改質之聚乙烯經接枝 處理之方法相同之方法。 上述異氰酸酯改質之聚乙烯係藉由在自由基產生劑存 在下,使聚乙烯與含異氰酸酯基之不飽和化合物經接枝處 理而成。上述異氰酸酯改質之聚乙烯較好爲將0.001〜1.5 莫耳%之含異氰酸酯基之不飽和化合物接枝於聚乙烯上而 成者。含異氰酸酯基之不飽和化合物之接枝量太少時,會 有缺乏黏著性之虞,太多時亦有缺'乏黏著性之虞。 上述含異氰酸酯基之不飽和化合物爲具有至少一個雙 鍵且含有至少一個異氰酸酯基(-NCO)之化合物。具體而言 -32-S -27- 201236867 The above unsaturated carboxylic acid and its derivative are preferably a monounsaturated carboxylic acid, a dibasic unsaturated carboxylic acid, and a metal salt, a guanamine, a quinone imine, an ester or an acid anhydride. At least one of the selected groups is selected. The above monounsaturated carboxylic acid generally has a carbon number of 20 or less, preferably 15 or less. Further, the above-mentioned monounsaturated carboxylic acid derivative is usually 20 or less carbon atoms, preferably 15 or less. The above-mentioned diunsaturated carboxylic acid generally has 30 or less carbon atoms, preferably 25 or less. Further, the derivative of the above-mentioned dibasic unsaturated carboxylic acid usually has a carbon number of 30 or less, preferably 25 or less. The above unsaturated carboxylic acid and its derivative, wherein acrylic acid, methacrylic acid, nadic acid, maleic acid and its anhydride, 5-norbornene-2,3-dicarboxylic acid and its anhydride, and methyl group At least one selected from the group consisting of glycidyl acrylate is preferably at least one selected from the group consisting of maleic anhydride and 5 · norbornene anhydride. The radical generating agent used in the grafting treatment is exemplified by an organic peroxide or an organic peroxyester. For example, the use of benzammonium peroxide, dichlorobenzhydryl peroxide, dicumyl peroxide, ditributyl peroxide, 2.5-dimethyl-2,5-di (over Oxide benzoate) hexyne-3, 1,4-bis(t-butylperoxyisopropyl)benzene, lauryl peroxide, tert-butyl peroxyacetate, 2,5 -Dimethyl-2,5-di(t-butylperoxy)hexyne-3, 2.5-dimethyl-2,5-di(t-butylperoxy)hexane, third Peroxybenzoic acid ester, tert-butylperoxyphenyl acetate, t-butyl peroxyisobutyrate, t-butyl peroxydioctanoate, tert-butylperoxy Valerate, cumylperoxypivalate and tert-butylperoxydiethylacetate, and 28-201236867 azo compounds, such as azobisisobutyronitrile, dimethylazoisobutyronitrile . Preferred among these are dicumyl peroxide, di-tert-butyl peroxide, 2,5-dimethyl-2,5-di(t-butylperoxide)hexyne-3,2 a dialkyl peroxide such as 5-dimethyl-2,5-di(t-butylperoxy)hexane or 1,4-bis(t-butylperoxyisopropyl)benzene. Among them, as the radical generating agent, an organic peroxide is preferred. It is preferred that the organic peroxide has a decomposition temperature of 100 ° C or more in half life. Further, the organic peroxide is preferably preferably dicumyl peroxide, benzamyl peroxide, ditributyl peroxide, 2,5-dimethyl-di (t-butyl) Oxy)hexane, 2,5-dimethyl-2,5-(t-butylperoxy)hexane-3' lauryl peroxide, and tert-butyl peroxybenzoate At least one of the selected groups. The use ratio of the radical generator is usually 0.001 to 1 part by weight based on 1 part by weight of the modified polyolefin. The above unsaturated carboxylic acid-modified polyolefin can be produced by uniformly mixing a polyethylene resin, an unsaturated carboxylic acid and/or a derivative thereof, and a radical generator. Specifically, it is exemplified by a melt kneading method using an extruder or a Banbury kneader or a kneader, a solution method dissolved in a suitable solvent, a slurry method suspended in a suitable solvent, or a so-called vapor phase grafting method. Wait. The treatment temperature is appropriately selected in consideration of deterioration of the polyethylene resin, decomposition of the unsaturated carboxylic acid and/or its derivative, decomposition temperature of the radical generator used, and the like. For example, the above melt-kneading method is usually carried out at a temperature of 60 to 350 °C. The above treatment temperature is preferably from 190 to 3 50 ° C, more preferably from 200 to 300 ° C. -29- 201236867 Whenever the above-mentioned unsaturated carboxylic acid-modified polyethylene is produced, in order to improve its performance, a method known in the art described in JP-A-62-01-01 can be used, for example, in grafting. After the quality or modification, the unreacted monomer (unsaturated carboxylic acid or its derivative) is removed by heating, washing or the like by treating with an epoxy compound, an amine group or a hydroxyl group-containing polyfunctional compound. Or a method of producing components such as by-products. The epoxy modified polyethylene may be copolymerized with an epoxy group-containing unsaturated compound by copolymerization of ethylene and an epoxy group-containing unsaturated compound, or by an epoxy group-containing unsaturated compound in the presence of a radical generating agent. Branch processing. The copolymerization of ethylene and an epoxy group-containing unsaturated compound can be carried out by a radical polymerization method at a pressure of from 200 to 2,500 bar. The grafting treatment can be carried out for the molten phase in the solvent phase or in the presence of a peroxide. This graft treatment method is known per se. The epoxy group-containing unsaturated compound is exemplified by, for example, the following. (1) Aliphatic glycidyl esters and aliphatic glycidyl ethers: for example, allyl glycidyl ether, vinyl glycidyl ether, glycidyl maleate, and itaconate, glycidyl (meth)acrylate (2) alicyclic glycidyl esters and ethers: for example 2-cyclohexene-1-glycidyl hydrazide, 4,5-diglycidylcyclohexene-carboxylate, 4-glycidylcyclohexene carboxylate Acid ester, 5-norbornene-2-methyl-2-glycidyl carboxylate, 2,3-diglycidyl-hang-cis-bicyclic (2.2.1)-5-heptene-carboxylate When the ester polyethylene is grafted, a homopolymer or copolymer of polyethylene can be grafted. The above epoxy-modified polyethylene is also preferably an ethylene/(meth)acrylic acid alkyl-30-201236867 ester/epoxy-containing unsaturated compound copolymer. In this case, it is preferred to contain 40% by weight or less, preferably 5 to 40% by weight, of the alkyl (meth)acrylate, and 10% by weight or less, preferably 0.1 to 8% by weight, based on the epoxy group-containing group. Saturated compound. The epoxy group-containing unsaturated compound is more preferably glycidyl (meth)acrylate. The alkyl (meth)acrylate is preferably at least one selected from the group consisting of methyl (meth)acrylate, ethyl acrylate, n-butyl acrylate, isobutyl acrylate and 2-ethylhexyl acrylate. Among the above epoxy-modified polyethylenes, the alkyl (meth)acrylate is preferably from 20 to 35 % by weight. Preferably, the MFI is 5 to 1 00 (1 90 ° C / 2.16 kg g / l 〇 minutes), and the melting point is 60 to 110 ° C. The above epoxy-modified polyethylene can be obtained by subjecting a monomer to radical polymerization. The above polyethylene can be purchased from a commercially available product which is generally produced in the form of pellets and which is produced by radical polymerization at a pressure of from 200 to 250 bar. For example, the above-described amine-modified polyethylene can be powdered in the presence of a radical generator by using a water cutting method of GARVA (Gala, Virginia, USA) or a microgranulation method of freeze-grinding. It is obtained by grafting a polyethylene with a polyamine compound containing a majority of an amidino group or an amine group. The above polyamine compound has a primary amine (R-NH2), a secondary amine (RyNH), a tertiary amine (R3-N), or a derivative thereof (for example, decylamine (R-CONH2)) in its molecule. Polymer or copolymer. In the formula, r is a hydrocarbon group, preferably a group consisting of an alkyl group, an aryl group, an aralkyl group, an alkenyl group and an alkynyl group, and at least one hydrocarbon group is selected from -31 to 201236867. More preferably, the number of carbon atoms of methyl, ethyl, propyl, butyl, pentyl, isopropyl, isobutyl or the like is from 1 to 10, preferably from 1 to 8, more preferably from 1 to 5'. The alkyl group of 1 to 3: a vinyl group, an allyl group or the like having 2 to 10 carbon atoms, preferably 2 to 8, more preferably 2 to 5, most preferably 2 to 4 alkenyl groups; or a phenyl group, a naphthyl group or the like. At least one hydrocarbon group selected from the group consisting of aryl groups having 6 to 10 carbon atoms. Preferred specific examples of the above polyamine compound are exemplified by vinylamine, polyallylamine and aromatic amine. The molecular weight of the above polyamine compound is preferably 1,000 or more, but it is preferably a higher molecular weight from the viewpoint of reactivity with an olefin after activation treatment or the like. Specifically, the molecular weight is preferably from 1,000 to 200,000, more preferably from 3,000 to 200,000, and most preferably from 15,000 to 200,000. The above-mentioned radical generating agent can be used as a radical generating agent exemplified by a user when the polyethylene which is an unsaturated carboxylic acid is subjected to graft treatment. The types and proportions of the free radical generators that are suitable are also the same. Further, the method of the graft treatment may be the same as the method of graft-treating the polyethylene in which the unsaturated carboxylic acid is modified. The above-mentioned isocyanate-modified polyethylene is obtained by graft-treating polyethylene and an isocyanate group-containing unsaturated compound in the presence of a radical generating agent. The above isocyanate-modified polyethylene is preferably obtained by grafting 0.001 to 1.5 mol% of an isocyanate group-containing unsaturated compound onto polyethylene. When the amount of the isocyanate group-containing unsaturated compound is too small, there is a lack of adhesion, and when there is too much, there is a lack of adhesion. The above isocyanate group-containing unsaturated compound is a compound having at least one double bond and containing at least one isocyanate group (-NCO). Specifically -32-

S 201236867 ,列舉爲(甲基)丙烯醯基異氰酸酯、巴豆醯基異氰酸酯、 巴兄酸異氰酸酯基乙酯、巴豆酸異氰酸酯基丁酯、巴豆酸 異氰酸醋基乙基乙二醇酯、巴豆酸異氰酸酯乙基二乙二醇 酯、巴丑酸異氰酸酯基乙基三乙二醇酯、(甲基)丙烯酸異 氰酸酯基乙酯 '(甲基)丙烯酸異氰酸酯基丁酯 '(甲基)丙 燒酸異氰酸酯基己酯、(甲基)丙烯酸異氰酸酯基辛酯、( 甲基)丙嫌酸異氰酸酯基月桂酯 '(甲基)丙烯酸異氰酸酯 基十六烷酯、(甲基)丙烯酸異氰酸酯基乙二醇酯、(甲基) 丙烯酸異氰酸酯基乙基二乙二醇酯、(甲基)丙烯酸異氰酸 酯基乙基三乙二醇酯等,尤其以(甲基)丙烯酸異氰酸酯基 乙酯較佳。 自由基產生劑較好爲有機過氧化物,更好爲一分鐘半 衰期爲100〜280°C者。尤其,以一分鐘之半衰期爲 12 0~23 0°C者較佳。有機過氧化物之代表例列舉爲第三丁 基過氧苯甲酸酯、2,5-二甲基-2,5-二(第三丁基過氧基)己 烷、二第三丁基過氧化物。該等有機過氧化物可單獨使用 ,亦可倂用兩種以上。 上述異氰酸酯改質之聚乙烯經接枝處理時,相對於聚 乙烯100重量份,含異氰酸酯基之不飽和化合物之調配比 例較好爲0.01〜10重量份,更好爲0.02〜5重量份,又更 好爲0.05〜5重量份。含異氰酸酯基之不飽和化合物相對 於1〇〇重量份之聚乙烯之比例太少時,構成層(B-2)之官 能基數變少,會有層(B-2)與層(C)缺乏接著性之虞。另一 方面,太多時,由於接枝反應效率降低’使未反應或副產 -33- 201236867 物的均聚合之含異氰酸酯基之不飽和化合物殘留於改質聚 乙烯樹脂中,故不會使黏著性繼續下降,且會有損及聚乙 烯樹脂原有物性之虞。 有機過氧化物之調配比例相對於聚乙烯1 00重量份, 較好爲0.001〜0.18重量份,更好爲0.01〜0.18重量份,又 更好爲0.02〜0.15重量份。有機過氧化物對100重量份之 聚乙烯之調配量太少時,會有層(B-2)與層(C)缺乏黏著性 之虞,太多時,會有損及聚乙烯原有物性之虞,且由於接 枝反應效率降低故會有未反應或副產物的均聚合之含異氰 酸酯基之不飽和化合物殘留於改質聚乙烯中而有使黏著性 下降之虞。 上述改質聚乙烯樹脂可藉由使用一般合成樹脂領域中 使用之擠出機,邊熔融混練邊進行改質而獲得。此時,使 用之擠出機可使用無帶式或皮帶式之任一種,但就去除未 反應或副產物的均聚合之含異氰酸酯基之不飽和化合物及 有機過氧化物之分解物之觀點而言,宜爲皮帶式擠出機。 上述混練溫度較好爲140〜280°C,雖隨使用之聚乙烯 、有機過氧化物之種類而異,但更好爲1 80〜23 0°C。混練 溫度太低時,會有改質無法良好進行之虞,太高時會有使 用之聚乙烯之一部分隨之劣化之虞。 又擠出機內滯留時間較好爲60秒以上,尤其90秒以 上較佳。擠出機內滯留時間未達60秒時,有無法進行應 滿意之改質之虞。 熔融改質時,亦可添加聚乙烯之領域中一般使用之對 -34-S 201236867, listed as (meth) propylene decyl isocyanate, crotonyl isocyanate, barbituric acid isocyanate ethyl ester, crotonic acid isocyanate butyl ester, crotonic acid isocyanate ethyl glycol ester, crotonic acid Isocyanate ethyl diethylene glycol ester, barium acid isocyanate ethyl triethylene glycol ester, (meth)acrylic acid isocyanate ethyl ester '(meth)acrylic acid isocyanate butyl ester '(meth)propanoic acid isocyanate Hexyl hexyl ester, (meth)acrylic acid isocyanate octyl ester, (methyl) acrylic acid isocyanate-based lauryl ester (meth)acrylic acid isocyanate hexadecyl ester, (meth)acrylic acid isocyanate glycolate, (meth)acrylic acid isocyanate ethyl diethylene glycol ester, (meth)acrylic acid isocyanate ethyl triethylene glycol ester, etc., particularly preferably (meth)acrylic acid isocyanate ethyl ester. The radical generating agent is preferably an organic peroxide, more preferably a one-minute half-life of 100 to 280 °C. In particular, it is preferred to have a half-life of one minute of 12 0 to 23 ° C. Representative examples of organic peroxides are exemplified by t-butyl peroxybenzoate, 2,5-dimethyl-2,5-di(t-butylperoxy)hexane, di-tert-butyl peroxide. These organic peroxides may be used singly or in combination of two or more. When the above-mentioned isocyanate-modified polyethylene is subjected to graft treatment, the ratio of the isocyanate group-containing unsaturated compound is preferably 0.01 to 10 parts by weight, more preferably 0.02 to 5 parts by weight, based on 100 parts by weight of the polyethylene. More preferably 0.05 to 5 parts by weight. When the ratio of the isocyanate group-containing unsaturated compound to the 1 part by weight of the polyethylene is too small, the number of functional groups constituting the layer (B-2) decreases, and the layer (B-2) and the layer (C) are lacking. Then the shackles of sex. On the other hand, when there are too many, since the graft reaction efficiency is lowered, the isocyanate group-containing unsaturated compound of the unreacted or by-produced product of 33-201236867 remains in the modified polyethylene resin, so that it does not cause Adhesiveness continues to decline, and it will damage the original physical properties of polyethylene resin. The compounding ratio of the organic peroxide is preferably 0.001 to 0.18 parts by weight, more preferably 0.01 to 0.18 parts by weight, still more preferably 0.02 to 0.15 parts by weight, per 100 parts by weight of the polyethylene. When the compounding amount of the organic peroxide to 100 parts by weight of polyethylene is too small, the layer (B-2) and the layer (C) lack adhesiveness, and when too much, the original physical property of the polyethylene may be impaired. Then, since the graft reaction efficiency is lowered, the isocyanate group-containing unsaturated compound which is unreacted or by-product of the unreacted product remains in the reformed polyethylene, and the adhesiveness is lowered. The above-mentioned modified polyethylene resin can be obtained by upgrading by melt-kneading using an extruder used in the field of general synthetic resin. In this case, the extruder to be used may be either a beltless belt or a belt type, but the viewpoint of removing the isocyanate group-containing unsaturated compound and the decomposition product of the organic peroxide which are unreacted or by-products. In other words, it should be a belt extruder. The above kneading temperature is preferably from 140 to 280 ° C, and although it varies depending on the type of polyethylene or organic peroxide to be used, it is preferably from 1 80 to 23 ° C. When the temperature of the kneading is too low, there is a possibility that the modification cannot be performed well, and when it is too high, there is a possibility that one of the polyethylenes used is deteriorated. Further, the residence time in the extruder is preferably 60 seconds or more, and particularly preferably 90 seconds or more. When the residence time in the extruder is less than 60 seconds, there is a possibility that the satisfactory modification cannot be performed. In the case of melt modification, it is also possible to add a pair of commonly used in the field of polyethylene -34-

S 201236867 氧或熱之安定劑、塡充劑(例如、雲母、滑石、玻璃、有 機纖維、木粉)、滑劑以及難燃化劑。 構成上述層(B-2)之改質聚烯烴樹脂較好爲改質高密 度聚乙烯,其中,較好爲由不飽和羧酸改質之高密度聚乙 烯、環氧改質之高密度聚乙烯、胺(NH2)改質之高密度聚 乙烯、及異氰酸酯改質之高密度聚乙烯所組成群組選出之 至少一種改質高密度聚乙烯,而且,更好爲由環氧改質之 高密度聚乙烯、胺(NH2)改質之高密度聚乙烯、及異氰酸 酯改質之高密度聚乙烯所組成群組選出之至少一種改質高 密度聚乙烯。 構成上述各層之樹脂可爲僅含1種各樹脂者,亦可爲 含兩種以上者。 上述各層亦可依據目的及用途,在不損及其性能之範 圍內,亦可爲另調配無機質粉末、玻璃纖維、金屬氧化物 等各種塡充劑者,又,亦可爲除塡充劑以外,調配熱安定 化劑、補強劑、紫外線吸收劑、顏料等其他任意之添加劑 者。 至於上述添加劑,就例如降低藥液透過之觀點而言, 亦可添加蒙脫土、貝德石(beidellite)、官石(saponite)、 綠脫石(nontronite)、水輝石(hectorite)、鋅蒙脫土 (sauconite)、矽鎂石(Stevens ite)等之矽鎂石系層狀黏度礦 物’或雲母等具有高長寬比之微小層狀礦物。 至於上述添加劑,亦可添加例如導電性塡充劑以賦予 導電性。導電性塡充劑並無特別限制,列舉爲例如金屬、 -35- 201236867 碳等導電性單體粉末或導電性單體纖維;氧化鋅等導電性 化合物之粉末;表面導電化處理粉末等。 上述導電性單體粉末或導電性單體纖維並無特別限制 ,列舉爲例如銅'鎳等金屬粉末;鐵、不鏽鋼等金屬纖維 :碳黑、碳纖維、特開平3-1 74 018號公報等中所記載之 碳纖絲等。 上述表面導電化處理粉末爲對玻璃珠、氧化鈦等非導 電性粉末之表面施以導電化處理所得之粉末。 上述導電化處理之方法並無特別限制,列舉爲例如印 刷基板、金屬濺鍍、無電解電鍍等。上述導電性塡充劑中 之碳黑,就經濟性或防止靜電累積之觀點而言爲有利故較 適用。調配上述導電性塡充劑時,較好經熔融混練預先製 作顆粒。 調配導電性塡充劑而成之樹脂導電性組成物之體積電 阻率較好爲lxlOG〜1χ109Ω. cm。更好下限爲1χ102Ω. cm ,更好上限爲1 χ1〇8Ω · cm。 賦予導電性時,亦可僅對最內層之與藥液接觸之氟樹 脂賦予導電性。該情況下,亦可設置導電性之氟樹脂層作 爲氟樹脂層之更內層。 本發明之第二層合物爲依序層合由聚烯烴樹脂所形成 之層(A)、由改質聚烯烴樹脂所形成之層(B-2)、由含黏著 性官能基之氟樹脂所形成之層(C)而成者,且最內層或最 外層之至少一層爲層(C)。該情況下,層合物爲在層(A)與 層(C)之間具有層(B-2)者,故可提高層(A)與層(C)之黏著 -36- 201236867 性。最內層或最外層之用語,在層合物爲管路或軟管時, 意指按照字義爲最內層或最外層,而層合物爲薄片或薄膜 時意指薄片或薄膜之最外側之層。層合物包含層(A)、層 (B)及層(C)以外之層時,層(C)以外之層亦可位在層(C)之 內側或外側。 本發明之弟一及弟—·層合物之層合構造之較佳層構成 並無特別限制,列舉爲例如聚乙烯樹脂/改質聚乙烯樹脂/ 氟樹脂、聚乙烯樹脂/改質聚乙烯樹脂/氟樹脂/氟樹脂、氟 樹脂/改質聚乙烯/聚乙烯樹脂/改質聚乙烯樹脂/氟樹脂、 氟樹脂/氟樹脂/改質聚乙烯/聚乙烯樹脂/改質聚乙烯樹脂/ 氟樹脂/氟樹脂等。 本發明之第一及第二層合物之層合構造較好爲聚烯烴 樹脂[層(A)] /改質聚嫌烴樹脂[層(B-1)或層(B-2)] /氟樹脂[ 層(C)](外面層/中間層/內面層)。藉由設置改質聚烯烴樹 脂[層(B-1)或層(B-2)]作爲中間層,可提高氟樹脂[層(c)] 與聚烯烴樹脂[層(A)]之黏著性。 尤其,藉由設置層(B-1),可實現極高之黏著強度, 與設置層(B-2)之情況相比較,可實現相當高的黏著強度 〇 又’亦可加入製造上述之層以外之多層薄膜時或加工 成袋狀時產生之樹脂廢料’或回收上述層合物而分離之樹 脂以二軸擠出機或短軸擠出機熔融混練獲得之顆粒作爲回 收層。 本發明之層合物中’層(C)可爲50〜500μιη,層(C)以 -37- 201236867 外之層之合計可爲100〜50000μιη。 上述層(C)之較佳膜厚爲100~300μπι,層(C)以外之層 之較佳膜厚合計爲3 00~20000μιη,更好爲600〜ΙΟΟΟΟμιη。 上述層合物可依據其用途選擇其大小。 本說明書中,各層之膜厚爲以顯微鏡等測定者。 上述氟樹脂之燃料透過係數較好爲10g· mm/m2/天以 下,更好爲7g· mm/m2 /天以下,又更好爲5g. mm/m2 /天 以下。本發明之層合物藉由使上述氟樹脂之燃料透過係數 在上述範圍內,可成爲具有更高度之燃料低透過性者》 本說明書中,上述燃料透過係數係將由測定對象樹脂 獲得之薄膜放入分別投入有異辛烷、甲苯及乙醇以45 : 45:10之體積比混合而成之異辛烷/甲苯/乙醇混合溶劑(以 下稱爲CE10),與以7.5: 7.5: 85之體積比混合之混合溶 劑(以下稱爲CE85)之燃料透過係數測定用杯中,由在 6〇°C測定之質量變化算出之兩個値中,其較大的値。 本發明之層合物之燃料透過速度之下限可爲例如 0.05g/m2/天,上限可爲例如30g/m2/天。 本說明書中,上述燃料透過速度爲自層合物整體之每 單位日數、每單位內面積透過之藥液之質量,爲使用 CE10或CE85於測定60°C之透過量所得之値》 本發明之層合物之形成方法並無特別限制,可依據層 合物之用途與形狀選擇最適當方法。成形方法之例列舉爲 射出成形、利用真空或加壓進行之壓製成形、吹塑成形、 吹氣成形、擠出成形等。 -38-S 201236867 Oxygen or heat stabilizers, chelating agents (eg, mica, talc, glass, organic fibers, wood flour), slip agents and flame retardants. The modified polyolefin resin constituting the above layer (B-2) is preferably a modified high-density polyethylene, and among them, a high-density polyethylene modified by an unsaturated carboxylic acid or an epoxy-modified high-density polymer is preferred. At least one modified high-density polyethylene selected from the group consisting of ethylene, amine (NH2) modified high density polyethylene, and isocyanate modified high density polyethylene, and more preferably modified by epoxy At least one modified high density polyethylene selected from the group consisting of density polyethylene, amine (NH2) modified high density polyethylene, and isocyanate modified high density polyethylene. The resin constituting each of the above layers may be one containing only one type of resin, or may be two or more types. The above layers may also be formulated with various kinds of sputum agents such as inorganic powder, glass fiber, metal oxide, etc., depending on the purpose and use, without damaging the performance thereof. , blending thermal stabilizers, reinforcing agents, UV absorbers, pigments and other additives. As for the above additives, for example, montmorillonite, beidellite, saponite, nontronite, hectorite, zinc monoxide may be added from the viewpoint of reducing the permeation of the liquid. A layered mineral with a high aspect ratio such as sauconite, stevenite ore, or a layered viscosity mineral such as mica. As the above additive, for example, a conductive chelating agent may be added to impart conductivity. The conductive chelating agent is not particularly limited, and examples thereof include a metal, a conductive monomer powder such as -35-201236867 carbon, or a conductive monomer fiber; a powder of a conductive compound such as zinc oxide; and a surface conductive powder. The conductive monomer powder or the conductive monomer fiber is not particularly limited, and examples thereof include metal powders such as copper 'nickel; metal fibers such as iron and stainless steel: carbon black, carbon fiber, and JP-A-3-174018. Carbon filaments and the like described. The surface conduction-treated powder is a powder obtained by subjecting a surface of a non-conductive powder such as glass beads or titanium oxide to a conductive treatment. The method of the above-described conductive treatment is not particularly limited, and examples thereof include a printed substrate, metal sputtering, electroless plating, and the like. The carbon black in the above conductive chelating agent is advantageous in terms of economy or prevention of static electricity accumulation. When the above conductive chelating agent is blended, it is preferred to prepare granules by melt-kneading in advance. The volume resistivity of the resin conductive composition obtained by blending the conductive chelating agent is preferably from lxlOG to 1 χ 109 Ω·cm. The lower limit is 1 χ 102 Ω·cm, and the upper limit is 1 χ 1 〇 8 Ω · cm. When conductivity is imparted, conductivity can be imparted only to the fluororesin which is in contact with the chemical solution in the innermost layer. In this case, a conductive fluororesin layer may be provided as the inner layer of the fluororesin layer. The second laminate of the present invention is a layer (A) formed of a polyolefin resin, a layer (B-2) formed of a modified polyolefin resin, and a fluororesin containing an adhesive functional group. The layer (C) formed is formed, and at least one of the innermost layer or the outermost layer is a layer (C). In this case, since the laminate has the layer (B-2) between the layer (A) and the layer (C), the adhesion of the layer (A) to the layer (C) can be improved -36-201236867. The term of the innermost layer or the outermost layer means that when the laminate is a pipe or a hose, it means the innermost layer or the outermost layer according to the meaning of the word, and when the laminate is a sheet or a film, it means the outermost side of the sheet or film. Layer. When the laminate comprises a layer other than the layer (A), the layer (B) and the layer (C), the layer other than the layer (C) may be located inside or outside the layer (C). The preferred layer constitution of the laminated structure of the first and second-layer laminates of the present invention is not particularly limited, and examples thereof include polyethylene resin/modified polyethylene resin/fluororesin, polyethylene resin/modified polyethylene. Resin/fluororesin/fluororesin, fluororesin/modified polyethylene/polyethylene resin/modified polyethylene resin/fluororesin, fluororesin/fluororesin/modified polyethylene/polyethylene resin/modified polyethylene resin/ Fluororesin / fluororesin, etc. The laminated structure of the first and second laminates of the present invention is preferably a polyolefin resin [layer (A)] / modified polyhydrocarbon resin [layer (B-1) or layer (B-2)] / Fluororesin [layer (C)] (outer layer / intermediate layer / inner layer). By providing a modified polyolefin resin [layer (B-1) or layer (B-2)] as an intermediate layer, adhesion of the fluororesin [layer (c)] to the polyolefin resin [layer (A)] can be improved. . In particular, by providing the layer (B-1), an extremely high adhesive strength can be achieved, and a relatively high adhesive strength can be achieved as compared with the case of the layer (B-2). The resin obtained by the multilayer film or the resin waste produced when processed into a bag shape or the resin obtained by recovering the above-mentioned laminate is melt-kneaded by a two-axis extruder or a short-axis extruder as a recovery layer. In the laminate of the present invention, the layer (C) may be 50 to 500 μm, and the layer (C) may be 100 to 50000 μm in total of layers other than -37 to 201236867. The film thickness of the layer (C) is preferably from 100 to 300 μm, and the film thickness of the layer other than the layer (C) is preferably from 30,000 to 20,000 μm, more preferably from 600 to ΙΟΟΟΟμηη. The above laminate may be selected in accordance with its use. In the present specification, the film thickness of each layer is measured by a microscope or the like. The fuel permeability coefficient of the above fluororesin is preferably 10 g·mm/m 2 /day or less, more preferably 7 g·mm/m 2 /day or less, and more preferably 5 g·mm/m 2 /day or less. When the fuel permeability coefficient of the fluororesin is within the above range, the laminate of the present invention can have a higher fuel permeability. In the present specification, the fuel permeability coefficient is obtained by the film obtained from the resin to be measured. An isooctane/toluene/ethanol mixed solvent (hereinafter referred to as CE10) mixed with isooctane, toluene and ethanol in a volume ratio of 45:45:10, and a volume ratio of 7.5:7.5:85 In the fuel permeability coefficient measuring cup of the mixed solvent (hereinafter referred to as CE85), the larger of the two enthalpy calculated from the mass change measured at 6 °C. The lower limit of the fuel permeation rate of the laminate of the present invention may be, for example, 0.05 g/m2/day, and the upper limit may be, for example, 30 g/m2/day. In the present specification, the fuel permeation rate is the mass per unit day of the laminate and the mass per unit area per unit area, and is obtained by measuring the permeation amount at 60° C. using CE10 or CE85. The method for forming the laminate is not particularly limited, and the most appropriate method can be selected depending on the use and shape of the laminate. Examples of the molding method are injection molding, press molding by vacuum or pressurization, blow molding, blow molding, extrusion molding, and the like. -38-

S 201236867 上述射出成形廣泛使用於熱可塑性樹脂之成形,適合 複雜形狀之成形體之製作。爲形成成形體,可例如藉由重 複地進行將熔融之樹脂射出於成形體構件之模具中’藉由 固化而成形於樹脂層上,射出熔融之其他樹脂且經固化而 成形之方法進行。 但,使用上述射出成形法時,由於必需在成形後卸除 模具,故無法一次製作層合物,需分成數構件成形,隨後 藉由熱熔著、黏著等手段進行一體接合,可獲得所需層合 物。 本發明之層合物由於氟樹脂層必須位在最內層或最外 層之任一者,故即使在進行上述接合時,由於必定使氟樹 脂層彼此接合,故可維持層合物整體之燃料低透過性。 上述各層之成形步驟之順序可依據所需層合構造適當 選擇,可如上述般自成爲外面之層先成形,亦可先進行成 爲內面之層之成形。 上述射出成形之各條件可依據使用之樹脂種類或量適 當選擇。 上述壓製成形,係以利用後述之成形方法獲得之薄片 或薄板(該薄片或薄板以下通稱爲層合物薄片)作爲原材料 ’使其在加熱下經真空或加壓,或利用公模具擠壓至模具 中而進行成形者。 上述壓製成形中之各條件可依據使用之層合物薄片之 組成或厚度適當選擇,但將層合物薄片加熱之第一步驟中 ,依據各層之熔融溫度’較好將上加熱器與下加熱器之溫 -39- 201236867 度設定成不同之溫度。 製作成爲上述原材料之層合物薄片之方法列舉爲例如 (1)以熔融狀態使樹脂共擠出成形,藉此在層間經熱熔融 著(熔融黏著)以一段形成多層構造之層合物之方法(共擠 出成形),(2)利用擠出機使分別個別製作之薄膜重疊並藉 熱熔著使層間黏著之方法,(3)利用擠出機將熔融樹脂擠 出於預先製作之薄膜表面上形成層合物之方法,(4)於預 先製作之薄膜之表面上靜電塗裝構成與該薄膜成鄰接之層 之聚合物後,藉由對所得塗裝物整體或自塗裝之側加熱, 使供給於塗裝之聚合物加熱熔融形成層之方法等。 若爲可共擠出構成各層之樹脂者,則一般係以上述 (I)之共擠出成形形成。上述共擠出成形列舉爲多歧管法 、饋料套管法、多層吹製法、多層吹氣成形法等過去習知 之多層共擠出製造法。利用該等方法成形,可成爲薄片狀 、或薄膜狀之層合物》 本發明之層合物亦可藉習知之任何手段接合而接上上 述層合物薄片,成爲袋狀而成爲槽等中空成形體。 接合之手段,於使用熱密封法等熱熔融黏著方法時, 具體而言係使兩片上述層合物薄片,較好以使氟樹脂彼此 鄰接之方式重疊,進行熱密封。熱密封溫度就薄片間之密 封強度之觀點而言,有必要爲黏著樹脂之融點以上、經黏 著樹脂及經層合之熱可塑性樹脂之熱分解溫度以下。熱密 封法就並無因黏著劑之劣化之影響方面而言係較佳。 上述熱熔融黏著方法列舉爲使用加熱盤之方法、利用 -40-S 201236867 The above injection molding is widely used for the molding of thermoplastic resins, and is suitable for the production of molded bodies of complicated shapes. The formation of the molded body can be carried out, for example, by repeatedly performing a method in which the molten resin is injected into the mold of the molded body member, which is formed by solidification on the resin layer, and the molten other resin is injected and cured. However, when the above injection molding method is used, since it is necessary to remove the mold after molding, the laminate cannot be produced at one time, and it is divided into a plurality of members, and then integrally joined by means of heat fusion, adhesion, or the like, thereby obtaining the desired Laminate. In the laminate of the present invention, since the fluororesin layer must be located at either the innermost layer or the outermost layer, even when the above bonding is performed, since the fluororesin layers are necessarily bonded to each other, the fuel of the entire laminate can be maintained. Low permeability. The order of the forming steps of the above layers may be appropriately selected depending on the desired lamination structure, and the outer layer may be formed as described above, or the inner layer may be formed first. The conditions of the above injection molding can be appropriately selected depending on the kind or amount of the resin to be used. The above press forming is performed by using a sheet or a sheet obtained by a forming method described later (the sheet or sheet is hereinafter referred to as a laminate sheet) as a raw material, which is subjected to vacuum or pressurization under heating, or extruded by a male mold to Formed in the mold. The conditions in the above press forming may be appropriately selected depending on the composition or thickness of the laminate sheet to be used, but in the first step of heating the laminate sheet, the upper heater and the lower heater are preferably heated according to the melting temperature of each layer. The temperature of the device -39 - 201236867 degrees is set to a different temperature. The method of producing a laminate sheet which is the above-mentioned raw material is exemplified by, for example, (1) a method of coextruding a resin in a molten state, thereby thermally melting (melting and adhering) between layers to form a laminate of a multilayer structure. (co-extrusion molding), (2) a method of laminating the separately formed films by an extruder and adhering them by heat fusion, and (3) extruding the molten resin onto the surface of the pre-made film by an extruder a method of forming a laminate thereon, (4) electrostatically coating a polymer constituting a layer adjacent to the film on a surface of a pre-formed film, and heating the entire coated article or the side of the self-coating layer A method of heating and melting a polymer supplied to a coating to form a layer. In the case where the resin constituting each layer can be coextruded, it is generally formed by coextrusion molding of the above (I). The above coextrusion molding is exemplified by a conventional multi-layer coextrusion production method such as a multi-manifold method, a feed sleeve method, a multilayer blowing method, or a multilayer blow molding method. The laminate of the present invention can be formed into a sheet-like or film-like laminate by any of the above methods. The laminate of the present invention can be joined by any means known in the art, and the laminate sheet can be attached to the sheet to form a bag shape and become a hollow such as a groove. Shaped body. In the method of bonding, when a heat fusion bonding method such as a heat sealing method is used, specifically, two sheets of the above-mentioned laminate sheets are preferably superposed such that the fluororesins are adjacent to each other and heat-sealed. The heat-sealing temperature is preferably equal to or higher than the thermal decomposition temperature of the adhesive resin and the laminated thermoplastic resin from the viewpoint of the sealing strength between the sheets. The heat sealing method is not preferred in terms of the influence of deterioration of the adhesive. The above thermal fusion bonding method is exemplified by the method of using a heating plate, using -40-

S 201236867 熱風之方法、利用摩擦熱之方法(機械的、超音波)或利用 高頻之方法等。層合薄片以真空成形、壓空成形、公模具 成形、射出成形等方法成形後,立即冷卻,利用該等熱溶 融黏著方法,亦可成爲袋狀。真空成形、壓空成形、公模 具成形由於成形時之層合薄片已加熱,故隨後可立即進行 熱熔融黏著,生產效率較佳。又,亦可組合進行上述之熱 熔融黏著。 再者,亦可採用使用電熱線之熔著部電熔合(電熔著 接合)作爲熱熔融接著方法。 本發明之層合物經接合接上成爲袋狀時,就燃料透過 性及耐藥品性之觀點而言,較好使氟樹脂彼此熔融黏著, 另外’使其他層彼此,尤其是外層之聚烯烴層彼此熔融接 著者,就機械強度之觀點而言係較佳。由於各層彼此容易 熔融接著,故熔融薄片邊緣之至少一部分亦可如圖1般預 先進行加工。 以下,使用圖1,針對熔著之薄片端之加工樣態加以 說明。圖1爲預先加工所接合之上述層合物薄片之端之樣 態之一例。3表示由聚烯烴樹脂所形成之層(A),4表示由 改質聚烯烴樹脂所形成之層(B-1)或層(B-2),5表示由含 黏著性官能基之氟樹脂所形成之層(C) 〇藉由使加工前之 薄片1之端加工成加工後之薄片2,可使各層容易地熔融 黏著。亦可暫時使加工前之薄片1熔著後,對端部施予同 樣的加工,再次對熔著部施加熱與壓力》 又,其他接合手段亦有利用黏著劑之方法。該情況下 -41 - 201236867 ,例如對接縫塗佈黏著劑,相互壓著,接著使該黏著劑至 少部分硬化。接著,放置於135〜150 °C之環境後,在加壓 下使該接縫冷卻。該接縫完全硬化需在室溫下5〜8天。 本發明之層合物爲袋狀之情況下,其厚度只要依用途 適當設定即可,而可爲50 μιη以上,較好亦可爲1〇〇 pm以 上。又,可爲500μιη以下,較好亦可爲300μιη以下。厚 度太薄時,會有燃料低透過性或機械強度變不足之虞,厚 度太厚時,會有柔軟性變不足之虞。 本發明之層合物亦可利用多層吹塑成形獲得。上述多 層吹塑成形可使用依據需要層數之台數之擠出機,使熔融 之樹脂經過多層吹塑成形用模嘴擠出雛型,且以鑲嵌模夾 住該雛型,於夾住上下爲袋狀之雛型內吹入空氣等,經膨 脹’密合於具有所需形狀之模具內壁,經冷卻固化後,以 成形品取出而進行。又,亦可使用射出吹塑成形或延伸吹 塑成形。上述多層吹塑成形係連續一連串之步驟,故就成 形容易性而言係較佳。 本發明之層合物亦可爲藉由塗覆構成內面層之氟樹脂 層而成形者。 藉由上述塗覆之氟樹脂層成形可進行例如上述之射出 成形或真空成形’獲得由具有爲目標之形狀之氟樹脂層以 外之層所成之成形體構件後,以過去習知方法將含氟樹脂 塗料塗佈於該成形體構件上,並經乾燥而進行。 利用上述塗覆之氟樹脂層爲進一步提高藥液阻隔性, 較好以過去習知之方法氟化。亦即,亦可利用PVdF共聚 -42-S 201236867 The method of hot air, the method of using frictional heat (mechanical, ultrasonic) or the method of using high frequency. The laminated sheet is formed by vacuum molding, pressure forming, male mold molding, injection molding, or the like, and then immediately cooled, and may be in the form of a bag by these thermal fusion bonding methods. Vacuum forming, pressure forming, and male mold forming are performed because the laminated sheets are heated at the time of forming, and then heat fusion bonding can be performed immediately, and the production efficiency is better. Further, the above-described heat fusion bonding may be carried out in combination. Further, it is also possible to use a fusion portion of the heating wire for electric fusion (electrofusion bonding) as a method of heat fusion. When the laminate of the present invention is joined to form a bag, it is preferred that the fluororesins are fused to each other from the viewpoint of fuel permeability and chemical resistance, and that the other layers, particularly the outer layer of the polyolefin, are formed. It is preferable from the viewpoint of mechanical strength that the layers are fused to each other. Since the layers are easily melted with each other, at least a portion of the edges of the molten sheet can be processed in advance as shown in Fig. 1. Hereinafter, the processing state of the sheet end of the fusion will be described using Fig. 1 . Fig. 1 is an example of a state in which the end of the above-mentioned laminate sheet joined is preliminarily processed. 3 denotes a layer (A) formed of a polyolefin resin, 4 denotes a layer (B-1) or a layer (B-2) formed of a modified polyolefin resin, and 5 denotes a fluororesin containing an adhesive functional group. The formed layer (C) can be easily melted and adhered by processing the end of the sheet 1 before processing into the processed sheet 2. It is also possible to temporarily melt the sheet 1 before processing, and apply the same processing to the end portion to apply heat and pressure to the fusion portion again. Further, other bonding means may use an adhesive. In this case -41 - 201236867, for example, the seam is coated with an adhesive, pressed against each other, and then the adhesive is hardened at least partially. Next, after being placed in an environment of 135 to 150 ° C, the joint was cooled under pressure. The seam is completely hardened at room temperature for 5 to 8 days. In the case where the laminate of the present invention is in the form of a bag, the thickness thereof may be appropriately set according to the use, and may be 50 μm or more, preferably 1 μm or more. Further, it may be 500 μm or less, preferably 300 μm or less. When the thickness is too thin, there is a problem that the fuel has low permeability or the mechanical strength is insufficient, and when the thickness is too thick, the flexibility is insufficient. The laminate of the present invention can also be obtained by multilayer blow molding. The above-mentioned multi-layer blow molding can use an extruder according to the number of layers required to extrude the molten resin through a multi-layer blow molding die, and clamp the prototype with a mosaic mold to clamp the upper and lower sides. Air or the like is blown into the bag-shaped blank, and is expanded and adhered to the inner wall of the mold having a desired shape, and after cooling and solidifying, the molded article is taken out. Further, injection blow molding or stretch blow molding can also be used. The above multilayer blow molding is a series of successive steps, so that it is preferable in terms of ease of formation. The laminate of the present invention may also be formed by coating a fluororesin layer constituting the inner surface layer. By the above-described coating of the fluororesin layer, for example, the above-described injection molding or vacuum forming can be carried out to obtain a molded body member formed of a layer other than the fluororesin layer having a desired shape, which will be contained in a conventional method. A fluororesin coating is applied onto the formed body member and dried. In order to further improve the liquid barrier property by using the above-mentioned coated fluororesin layer, it is preferred to fluorinate by a conventional method. That is, PVdF copolymer can also be used -42-

S 201236867 物或氟化乙烯等之燒結溫度或利用含氟濃度低之含氟樹脂 塗料形成塗膜後,藉由氟化而形成具有高阻隔性之氟樹脂 層。 至於本發明之層合物之用途,可較好地使用作爲例如 印刷基板、自車等之汽油槽、輕油槽等之燃料用槽、散熱 器槽、溶劑用槽、塗料用槽、半導體用藥液等之酸、鹼等 之腐蝕性、侵蝕性強的藥液之容器或硏磨材之漿料用容器 、飮料用或飮食物用槽等、收容液體之瓶、容器、槽、袋 、燃料補給站所用之埋設地下之管路或軟管等。又,本發 明之層合物亦可作爲對柴油引擎排氣噴霧尿素水而減低 N〇x之系統中之尿素水容器,由於其優異之耐藥品性而可 較好地使用。 本發明亦爲由上述層合物所成之藥液用容器。且,亦 可爲由上述層合物所成之尿素水用容器。亦爲由上述層合 物所成之燃料用槽。亦爲由上述層合物所成之飲料用或食 品用槽。亦爲由上述層合物所成之埋設地下之管路或軟管 。埋設地下之管路或軟管較好爲例如燃料補給站所用者。 亦爲由上述層合物所成之漏斗頸軟管、燃料軟管或燃料管 路。漏斗頸軟管、燃料軟管或燃料管路通常爲使用於汽車 等之內燃機等者。S 201236867 A fluororesin layer having a high barrier property is formed by fluorination after forming a coating film of a material or a fluorinated ethylene or the like or a fluorine-containing resin coating material having a low fluorine content. For the use of the laminate of the present invention, a fuel tank such as a printing substrate, a gasoline tank such as a car, a fuel tank such as a light oil tank, a radiator tank, a solvent tank, a coating tank, and a semiconductor liquid can be preferably used. A container for a corrosive or aggressive chemical liquid such as an acid or an alkali, a slurry container for a honing material, a food or a food tank, a liquid bottle, a container, a tank, a bag, and a fuel supply. Underground pipes or hoses used in the station. Further, the laminate of the present invention can also be used as a urea water container in a system for reducing the N 〇 x by spraying urea water to a diesel engine exhaust, and can be preferably used because of its excellent chemical resistance. The present invention is also a container for a liquid medicine formed from the above laminate. Further, it may be a container for urea water formed from the above laminate. It is also a fuel tank formed of the above laminate. It is also a tank for beverages or foods formed from the above laminate. It is also a pipe or hose buried underground by the above laminate. The underground pipeline or hose is preferably used by, for example, a fuel supply station. Also a funnel neck hose, fuel hose or fuel line formed from the above laminate. The funnel neck hose, fuel hose or fuel line is usually used for an internal combustion engine such as an automobile.

[發明效果J 本發明之層合物係由上述構成所成,故可使由含有黏 著性官能基之氟樹脂所形成之層與改質聚烯烴樹脂所形成 -43- 201236867 之層直接強固地接合,其初期黏著性以及初期黏著性之均 一性、進而保持黏著性優異。 【實施方式】 以下列舉實施例更詳細說明本發明,但本發明並非僅 限於該等實施例者。 實施例及比較例中,各種測定係以下述方法進行。 [氟樹脂之單體組成] 使用 NMR分析裝置(Bruker BioSpin公司製造, AC3 00,高溫探針),以熔融狀態測定。 [官能基含有率] [含環氧基之氟樹脂之環氧基] 熔融下,使用300MHz之l9F-NMR,利用以下之算式 ,自所得之圖表計算TFE、Et、HFP 3元之組成比率。 TFE 之含有莫耳比={3B + 3C-2A}/{4A + 6B + 3C}[Effect of the Invention] The laminate of the present invention is formed by the above-described constitution, so that the layer formed of the fluororesin containing the adhesive functional group and the layer formed of the modified polyolefin resin can be directly strengthened by the layer of -43-201236867. The bonding is excellent in initial adhesion and initial adhesion, and further maintains adhesion. [Embodiment] The present invention will be described in more detail below by way of examples, but the invention is not limited to the embodiments. In the examples and comparative examples, various measurement systems were carried out by the following methods. [Monomer composition of fluororesin] It was measured in a molten state using an NMR analyzer (manufactured by Bruker BioSpin Co., Ltd., AC3 00, high temperature probe). [Functional group content ratio] [Epoxy group of epoxy group-containing fluororesin] The composition ratio of TFE, Et, and HFP 3 was calculated from the obtained chart by using the following formula using l9F-NMR at 300 MHz. The molar content of TFE = {3B + 3C-2A} / {4A + 6B + 3C}

Et 之含有莫耳比= {2A + 3B}/{4A + 6B + 3C} HFP 含有莫耳比=4A/{4A + 6B + 3C} 又, A = -82〜- 61ppm之範圍之積分値 6 = -117〜-94?1>111之範圍之積分値 0 = -147〜-117??111之範圍之積分値 另一方面,使用含氟樹脂離子作爲溶劑,在高溫下, -44-Mo content ratio of Et = {2A + 3B}/{4A + 6B + 3C} HFP contains Moh ratio = 4A/{4A + 6B + 3C} Further, A = -82~- 61ppm range of integral 値6 = -117~-94?1> The integral of the range of 値0 = -147~-117?? The integral of the range of 111. On the other hand, the fluorine-containing resin ions are used as a solvent at a high temperature, -44-

S 201236867 充分膨潤之狀態下,使用3 00MHz之1 H-NMR測定,且利 用以下算式,由所得之圖表計算Et與含環氧基之單體之 2元之組成比率。S 201236867 In the state of full swelling, the composition ratio of Et and the epoxy group-containing monomer was calculated from the obtained chart using 1 H-NMR of 300 MHz.

Et 之含有莫耳比= {2F-2D-3E}/{2F-2D-E} 含有含環氧基之單體之莫耳比= 2E/{2F-2D-E} 又, D = 4.04~4.84ppm之箪货圍之積分値 E = 3.43~4.04ppm之範圍之積分値 F = 1.39〜3.43ppm之範圍之積分値 由以上之結果,求得TFE、Et、HFP、含環氧基之單 體之4元組成比,計算出含環氧基之單體之組成(莫耳%) 作烏環氧基之含有率。 [含碳酸酯基之氟樹脂之主鏈末端之碳酸酯基] 在室溫下將共聚物之白色粉末之切斷片壓縮成形,製 備厚度50〜200μιη之薄膜。該薄膜利用紅外線吸收光譜分 析,源自碳酸酯基[-〇C( = 0)0-]之羰基之峰出現在 1810~1815 cmlvCCsO)]之吸收波長,故測定其v(C = 0)峰 之吸光度,且以下述式(a)計算出碳酸酯基之組成。 碳酸酯基之含有率(莫耳%) = AW/(10 · sdf) (a) A :源自碳酸酯基[-0C( = 0)0-]之v(C = 0)峰之吸光度 ε:源自碳酸酯基[-0<:( = 0)0-]之v(C = 0)峰之莫耳吸 光度係數。來自模型化合物之ε=170(1 . cm」.moP1) W:由共聚物之組成計算之單體之平均分子量Et contains molar ratio = {2F-2D-3E}/{2F-2D-E} Mohs ratio of monomer containing epoxy group = 2E/{2F-2D-E} Again, D = 4.04~ The integral of 4.84ppm 箪 値 = E = 3.43~4.04ppm 値F = 1.39~3.43ppm integral 値 From the above results, TFE, Et, HFP, epoxy-containing single The composition ratio of the epoxy group-containing monomer (% by mole) was calculated as the content ratio of the quaternary epoxy group. [Carbide group at the end of the main chain of the carbonate-containing fluororesin] The cut piece of the white powder of the copolymer was compression-molded at room temperature to prepare a film having a thickness of 50 to 200 μm. The film was analyzed by infrared absorption spectroscopy, and the peak of the carbonyl group derived from the carbonate group [-〇C(=0)0-] appeared at the absorption wavelength of 1810~1815 cmlvCCsO)], so the peak of v(C=0) was determined. The absorbance was measured, and the composition of the carbonate group was calculated by the following formula (a). Carbonate group content (% by mole) = AW / (10 · sdf) (a) A : Absorbance of v (C = 0) peak derived from carbonate group [-0C( = 0)0-]: Mohr absorbance coefficient derived from the v (C = 0) peak of the carbonate group [-0<:( = 0)0-]. ε = 170 (1 . cm".moP1 from the model compound W: average molecular weight of the monomer calculated from the composition of the copolymer

C -45- 201236867 [含羧基之氟樹脂之羧基含有率] 含羧基之氟樹脂之組成 熔融下,使用3 00MHz之19F-NMR,利用以下之算式 ,自所得之圖表計算TFE、Et、HFP 3元之組成比率。 TFE 之含有莫耳比={3B + 3C-2A}/{4A + 6B + 3C}C -45- 201236867 [Carboxyl group content of carboxyl group-containing fluororesin] The composition of the carboxyl group-containing fluororesin is melted, and 19F-NMR of 300 MHz is used, and TFE, Et, and HFP 3 are calculated from the obtained chart using the following formula. The composition ratio of the yuan. The molar content of TFE = {3B + 3C-2A} / {4A + 6B + 3C}

Et 之含有莫耳比= {2A + 3B}/{4A + 6B + 3C} HFP 含有莫耳比=4A/{4A + 6B + 3C} 又, A = -82〜- 61ppm之範圍之積分値 B = -l 17〜-9 4PPm之範圍之積分値 C = -147~-117ppm之範圍之積分値 在室溫下將共聚物之白色粉末之切斷片壓縮成形,製 備厚度50~2 00 μπι之薄膜。該薄膜利用紅外線吸收光譜分 析,源自羧基[_(C = 0)0H]之羰基之峰出現在 1 630〜1 783CHT1 [v(C = 0)]之吸收波長,故測定其v(C = 0)峰 之吸光度,且以下述式(a)計算出羧基之組成。 羧基之含有率(莫耳%) = AW/(10 · edf) (a) A :源自羧基[_(C = 0)0H]之v(C = 0)峰之吸光度 ε:源自羧基[-(C = 0)0H]之v(C = 0)峰之莫耳吸光度係 數。來自模型化合物ε = 5 00( 1 . cm·1 . mol·1) W:由共聚物之組成計算之單體之平均分子量 由以上之結果,求得TFE、Et、HFP、含有羧基之單 體之4元組成比,且計算出含羧基之單體之組成(莫耳%) 作爲羧基之含有率。 -46 -Mo content ratio of Et = {2A + 3B}/{4A + 6B + 3C} HFP contains Moh ratio = 4A/{4A + 6B + 3C} Further, A = -82~- 61ppm of the range 値B = -l 17~-9 The integral of the range of 4PPm 値C = integral of the range of -147~-117ppm 压缩 The cut piece of the white powder of the copolymer is compression-molded at room temperature to prepare a film having a thickness of 50 to 200 μm . The film was analyzed by infrared absorption spectroscopy, and the peak of the carbonyl group derived from the carboxyl group [_(C = 0)0H] appeared at the absorption wavelength of 1 630~1 783 CHT1 [v (C = 0)], so the v (C = 0) The absorbance of the peak, and the composition of the carboxyl group is calculated by the following formula (a). The content of the carboxyl group (% by mole) = AW / (10 · edf) (a) A : The absorbance of the peak of v (C = 0) derived from the carboxyl group [_(C = 0)0H] ε: derived from the carboxyl group [- (C = 0) 0H] The v-absorbance coefficient of the v (C = 0) peak. From the model compound ε = 5 00 (1 . cm·1 . mol·1) W: the average molecular weight of the monomer calculated from the composition of the copolymer. From the above results, TFE, Et, HFP, carboxyl group-containing monomer were obtained. The composition ratio of 4 yuan was calculated, and the composition (monogen%) of the monomer having a carboxyl group was calculated as the content ratio of the carboxyl group. -46 -

S 201236867 [樹脂之熔點] 使用DSC裝置(Mettler公司製造),求得以10t/分鐘 之速度升溫時對應於熔解熱曲線中之極大値之溫度。 [MFR] 使用熔融係數測定儀(東洋精機製作所公司製造),測 定各溫度、5kg荷重下,每單位時間(10分鐘)自直徑2mm 、長度8mm之噴嘴流出之重量(g)〇 [接著強度] 自成形體切出長度5cm、寬度lcm之樣品,且剝離成 形體黏著最弱之部分,且使用萬能拉力試驗機(Orientec 製造)進行1 80度之剝離試驗,以N/cm爲單位測定黏著強 度。 [拉伸強度及拉伸伸長率] 使用萬能拉力試驗機(Orientec製造),在室溫以拉伸 速度100mm/分鐘拉伸微型亞鈴片,測定其最大點強度及 伸長度。 實施例、比較例中使用以下樹脂。 氟樹脂A(含環氧樹脂之TFE/Et/HFP共聚物) 合成方法 將純水lkg投入內容積4L之高壓釜中,充分進行氮 -47- 201236867 氣置換後,饋入八氟環丁烷884g及六氟丙烯316g,使系 統內部維持在35°C,攪拌速度5 80rpm。隨後,饋入四氟 乙烯147g、乙烯4.5g、烯丙基縮水甘油醚1.5g,隨後添 加15g之二正丙基過氧基二羧酸酯之50質量%甲醇溶液 ’開始聚合。聚合進行之同時系統內之壓力下降,故連續 供給四氟乙烯/乙烯/六氟丙烯=50.5/42.3/7.2莫耳%之混合 氣體,使系統內之壓力保持在l.OMPaG。接著,針對烯丙 基縮水甘油醚亦連續饋入合計量5.9g,持續攪拌24.3小 時。接著,釋壓恢復至大氣壓後,反應產物經水洗、甲醇 洗淨後,經乾燥獲得氟樹脂之粉末22 Og。聚合速度在反 應整體過程中幾乎固.定在9.1g/hr» 所得粉末具有以下之組成及物性》 TFE/Et/HFP/烯丙基縮水甘油醚(含環氧基之單體)= 49.9/41 · 1/7.5/1.4(莫耳 %)。S 201236867 [Melting Point of Resin] Using a DSC apparatus (manufactured by Mettler Co., Ltd.), the temperature at a temperature of 10 t/min is required to correspond to the maximum temperature in the heat of fusion curve. [MFR] Using a melt coefficient meter (manufactured by Toyo Seiki Seisakusho Co., Ltd.), the weight (g) 接着 [adequate strength] from a nozzle of 2 mm in diameter and 8 mm in length per unit time (10 minutes) at each temperature and 5 kg load was measured. A sample having a length of 5 cm and a width of 1 cm was cut out from the molded body, and the weakest part of the molded body was peeled off, and a peel test of 180 ° was performed using a universal tensile tester (manufactured by Orientec), and the adhesive strength was measured in units of N/cm. . [Tensile Strength and Tensile Elongation] Using a universal tensile tester (manufactured by Orientec), a micro-ring sheet was stretched at a stretching speed of 100 mm/min at room temperature, and the maximum point strength and elongation were measured. The following resins were used in the examples and comparative examples. Fluororesin A (TFE/Et/HFP copolymer containing epoxy resin) Synthetic method Pure water lkg was placed in an autoclave with an internal volume of 4 L, and after fully replacing with nitrogen-47-201236867, octadecacyclobutane was fed. 884 g and 316 g of hexafluoropropylene maintained the internal temperature of the system at 35 ° C and a stirring speed of 580 rpm. Subsequently, 147 g of tetrafluoroethylene, 4.5 g of ethylene, and 1.5 g of allyl glycidyl ether were fed, followed by the addition of 15 g of a 50% by mass methanol solution of di-n-propylperoxydicarboxylate to start polymerization. At the same time as the polymerization was carried out, the pressure in the system was lowered, so that a mixed gas of tetrafluoroethylene/ethylene/hexafluoropropylene = 50.5/42.3/7.2 mol% was continuously supplied, and the pressure in the system was maintained at 1.0 MPaG. Next, a total amount of 5.9 g was continuously fed to the allyl glycidyl ether, and stirring was continued for 24.3 hours. Then, after the pressure was released to atmospheric pressure, the reaction product was washed with water and washed with methanol, and dried to obtain 22 Og of a fluororesin powder. The polymerization rate is almost fixed at 9.1 g/hr» during the whole reaction. The obtained powder has the following composition and physical properties. TFE/Et/HFP/allyl glycidyl ether (epoxy group-containing monomer) = 49.9/ 41 · 1/7.5/1.4 (% by mole).

融點:190°C MFR : 22g/10min(210〇C,5kg) 官能基含有率:環氧基1.4莫耳% 氟樹脂B(主鏈末端具有碳酸酯基之CTFE/TFE/PPVE共聚 物) 合成方法 於可收容水175 kg之附套筒之攪拌式聚合槽中饋入純 水50kg,以純氮氣充分置換內部空間後,以真空排除氮 氣。接著壓入八氟環丁院 40.5kg、氯三氧乙稀 -48-Melting point: 190 ° C MFR : 22 g/10 min (210 ° C, 5 kg) Functional group content: epoxy group 1.4 mol % Fluoro Resin B (CTFE/TFE/PPVE copolymer having a carbonate group at the end of the main chain) Synthetic method 50 kg of pure water was fed into a stirred polymerization tank containing 175 kg of water, and the internal space was sufficiently replaced with pure nitrogen, and nitrogen was removed by vacuum. Then pressed into the octafluorocyclobutanin 40.5kg, chlorotrioxyethylene -48-

S 201236867 [CTFE]2.4kg、四氟乙烯[TFE]6.5kg、全氟(丙基乙烯基醚 )[PPVE] 4.5 kg,將溫度調節至35 °C,開始攪拌。於其中 添加〇.2kg之作爲聚合起始劑之二正丙基過氧基二羧酸酯 [NPP]之50質量%甲醇溶液,開始聚合。聚合中,以使槽 內壓力維持在〇.8MPa之方式邊追加饋入調製成與所需共 聚合物組成相同組成之混合單體邊聚合後,使槽內殘留之 氣體排氣且取出生成之聚合物,經脫無機物且以純水洗淨 ,並經乾燥,獲得19kg之粒狀粉末之CTFE共聚物。接 著,使用 φ50ιηιη短軸擠出機,在汽筒溫度28(TC下進行 熔融混練,獲得顆粒。接著在180°C下加熱所得顆粒狀之 CTFE共聚物24小時。 所得顆粒具有以下之組成及物性。 CTFE/TFE/PPVE = 3 4.5/63.4/2.1 (莫耳 %) 〇S 201236867 [CTFE] 2.4kg, tetrafluoroethylene [TFE] 6.5kg, perfluoro(propyl vinyl ether) [PPVE] 4.5 kg, adjust the temperature to 35 °C, start stirring. The polymerization was started by adding 2. 2 kg of a 50% by mass methanol solution of di-n-propylperoxydicarboxylate [NPP] as a polymerization initiator. In the polymerization, the mixed monomer which has the same composition as the desired copolymer composition is additionally fed while maintaining the pressure in the tank at 〇8 MPa, and then the gas remaining in the tank is exhausted and taken out. The polymer was demineralized and washed with pure water and dried to obtain 19 kg of a pelletized CTFE copolymer. Next, using a φ50ιηιη short-axis extruder, melt-kneading was carried out at a cylinder temperature of 28 (TC) to obtain pellets, and then the obtained pelletized CTFE copolymer was heated at 180 ° C for 24 hours. The obtained pellets had the following composition and physical properties. CTFE/TFE/PPVE = 3 4.5/63.4/2.1 (mole%) 〇

熔點:230°C MFR : 18g/10min(297〇C-5kg) 官能基含有率:羧酸酯基0.02莫耳% 氟樹脂C(含有羧基之TFE/Et/HFP共聚物) 合成方法 將純水1.83kg投入內容積6L之高壓釜中,充分進行 氮氣置換後,饋入八氟環丁烷848g及六氟丙烯414g,使 系統內部維持在35°C,攪拌速度600rpm。隨後,饋入四 氟乙烯143g、乙烯4.5g、Η--碳烯酸之50質量%甲醇溶 液〇.3g、環己烷O.lg,隨後添加21.5g之二正丙基過氧基 -49- 201236867 羧酸酯之50質量%甲醇溶液,開始聚合。聚合進行之同 時系統內之壓力下降,故連續供給四氟乙烯/乙烯/六氟丙 烯=51.2/42.1/6.7莫耳%之混合氣體,使系統內之壓力保 持在0.9 2MPaGf。接著,關於十一碳烯酸之50質量%甲醇 溶液亦連續饋入合計量3.6g,持續攪拌4.2小時。接著, 釋壓恢復至大氣壓後,反應產物經水洗、甲醇洗淨後,經 乾燥獲得白色粉末191g。 所得粉末具有以下之組成及物性。 丁?£心/町卩/十一碳烯酸=47.6/4 2.5/9.6/0.3(莫耳〇/〇)。Melting point: 230 ° C MFR : 18 g/10 min (297 〇 C-5 kg) Functional group content: carboxylate group 0.02 mol % Fluoro Resin C (TFE/Et/HFP copolymer containing carboxyl group) Synthetic method Pure water 1.83 kg was placed in an autoclave having an internal volume of 6 L, and after sufficiently replacing with nitrogen, 848 g of octafluorocyclobutane and 414 g of hexafluoropropylene were fed, and the inside of the system was maintained at 35 ° C, and the stirring speed was 600 rpm. Subsequently, 143 g of tetrafluoroethylene, 4.5 g of ethylene, 50% by mass of methanol solution of hydrazine-carbenoic acid, g.3 g, cyclohexane O.lg, and then 21.5 g of di-n-propylperoxy-49 were added. - 201236867 A 50% by mass methanol solution of a carboxylate starts polymerization. At the same time as the polymerization was carried out, the pressure in the system was lowered, so that a mixed gas of tetrafluoroethylene/ethylene/hexafluoropropylene = 51.2/42.1/6.7 mol% was continuously supplied, and the pressure in the system was maintained at 0.9 2 MPaGf. Next, a 50 mass% methanol solution of undecylenic acid was continuously fed into a total amount of 3.6 g, and stirring was continued for 4.2 hours. Then, after the pressure was released to atmospheric pressure, the reaction product was washed with water and methanol, and dried to obtain 191 g of a white powder. The obtained powder has the following composition and physical properties. Ding? £心/町卩/undecenoic acid=47.6/4 2.5/9.6/0.3 (mole/〇).

熔點:1 9 5 °C MFR : 3.0g/10min(230〇C,5kg) 官能基含有率:羧基0.3莫耳% 熱可塑性樹脂 改質聚乙烯 A[PE]:三井化學公司製造,商品名 ADMER HB030 改質聚乙烯C[PE]:國際公開第2007/04026 1號說明 書之藉由使聚烯烴與含碳二醯亞胺基之化合物反應所得之 亞胺基改質之聚乙烯 HDPE :日本聚烯烴公司製造,商品名HJ451 實驗例1 使用利用多層吹塑方式製備之氟樹脂A(厚度200μιη)/ 改質聚乙烯Α(厚度100pm)/HDPE薄膜(600μηι)之外形 20mm之管路,以熱密封將其單邊密封後,加入CE10(異Melting point: 1 9 5 ° C MFR : 3.0 g/10 min (230 〇 C, 5 kg) Functional group content: carboxyl group 0.3 mol % Thermoplastic resin modified polyethylene A [PE]: manufactured by Mitsui Chemicals, trade name ADMER HB030 modified polyethylene C[PE]: International Publication No. 2007/04026 No. 1 by the reaction of a polyolefin with a carbon-containing diimine-based compound to obtain an imine-based modified polyethylene HDPE: Japanese poly Manufactured by Olefin Co., Ltd., trade name HJ451 Experimental Example 1 A fluororesin A (thickness 200 μm)/modified polyethylene crucible (thickness 100 pm)/HDPE film (600 μηι) prepared by a multilayer blow molding method was used to form a tube of 20 mm. After sealing the seal on one side, add CE10 (different

-50- S 201236867 辛烷/甲苯/乙醇=45/45/ 1 0(體積%))且以熱密封另一邊予以 封口,放入60°C環境之防爆爐中168hr。又排出燃料後, 沖壓ASTM記載之微型亞鈴片,與自燃料浸漬前之薄膜沖 壓ASTM記載之微型亞鈴片之拉伸強度與伸長率進行比較 。又,拉伸強度與伸長率維持在7 5 %以上。 實驗例2 使用利用多層吹塑方式製備之氟樹脂C(厚度250μιη)/ 改質聚乙烯C(厚度150pm)/HDPE薄膜(600μιη)之外形 10mm之管路,以熱密封將其單邊密封後,加入CE 10(異 辛烷/甲苯/乙醇=4.5/45/10(體積%))且以熱密封另一邊予以 封口,放入60°C環境之防爆爐中168hr。又排出燃料後, 沖壓ASTM記載之微型亞鈴片,且與自燃料浸漬前之管路 沖壓ASTM記載之微型亞鈴片之拉伸強度與伸長率進行比 較。拉伸強度與伸長率維持在75%以上。成形體之氟樹脂 C之層與改質聚乙烯C層之初期黏著強度爲35N/cm,燃 料浸漬後成爲3 lN/cm。 實驗例3 使用利用多層吹塑方式製備之氟樹脂B(厚度200μιη)/ 改質聚乙烯C(厚度100pm)/HDPE薄膜(600μηι)之外形 2 0mm之管路,以熱密封將其單邊密封後,加入CE 10(異 辛烷/甲苯/乙醇=4 5/45/ 1 0(體積。/〇))且以熱密封另一邊予以 封口 ’放入60°C環境之防爆爐中168hr。又排出燃料後, 201236867 沖壓ASTM記載之微型亞鈴片,且與自燃料浸漬前之薄膜 沖壓ASTM記載之微型亞鈴片之拉伸強度與伸長率進行比 較。又,拉伸強度與伸長率維持在7 5%以上。成形體之氟 樹脂B之層與改質聚乙烯C層之初期黏著強度爲i 7N/cm ,燃料浸漬後成爲lON/cm。 [產業上之可能利用性] 本發明之層合物可較好使用作爲收容液體之容器、瓶 、槽、袋、管路、軟管、管線等。 【圖式簡單說明】 圖1爲經熔著之薄片端之加工樣態之一例。 【主要元件符號說明】 1 :加工前薄片 2 :加工厚薄片 3 :聚烯烴樹脂所形成之層(A) 4:改質聚烯烴樹脂所形成之層(B-1)或層(B-2) 5 :含黏著性官能基之氟樹脂所形成之層(C) -52--50- S 201236867 Octane/toluene/ethanol = 45/45/1 0 (% by volume)) and sealed on the other side of the heat seal, and placed in an explosion-proof furnace at 60 ° C for 168 hr. After the fuel was discharged, the micro-bells described in ASTM were punched and compared with the tensile strength and elongation of the micro-rings described in ASTM from the film impregnation before fuel impregnation. Further, the tensile strength and elongation were maintained at 75 % or more. Experimental Example 2 A fluororesin C (thickness 250 μm)/modified polyethylene C (thickness 150 pm)/HDPE film (600 μm) prepared by a multilayer blow molding method was used, and a 10 mm-shaped tube was sealed by a heat-sealing method. CE 10 (isooctane / toluene / ethanol = 4.5 / 45 / 10 (% by volume)) was added and sealed on the other side by heat sealing, and placed in an explosion-proof furnace at 60 ° C for 168 hr. After the fuel is discharged, the micro-ring sheet described in ASTM is punched and compared with the tensile strength and elongation of the micro-ring sheet described in ASTM before the fuel impregnation. Tensile strength and elongation are maintained above 75%. The initial adhesive strength of the layer of the fluororesin C of the molded body and the modified polyethylene C layer was 35 N/cm, and the fuel was immersed to 3 lN/cm. Experimental Example 3 A fluororesin B (thickness 200 μm)/modified polyethylene C (thickness 100 pm)/HDPE film (600 μηι) prepared by a multilayer blow molding method was used to form a 20 mm-shaped pipe, which was hermetically sealed by heat sealing. Thereafter, CE 10 (isooctane / toluene / ethanol = 4 5 / 45 / 10 (volume / 〇)) was added and sealed on the other side by heat sealing ' into an explosion-proof furnace at 60 ° C for 168 hr. After the fuel was discharged, the micro-bells described in ASTM were punched in 201236867 and compared with the tensile strength and elongation of the micro-bells described in the ASTM film before the fuel impregnation. Further, the tensile strength and elongation were maintained at 75% or more. The initial adhesive strength of the layer of the fluororesin B of the molded body and the modified polyethylene C layer was i 7 N/cm, and became 1 ON/cm after the immersion of the fuel. [Industrial Applicability] The laminate of the present invention can be preferably used as a container for accommodating a liquid, a bottle, a tank, a bag, a pipe, a hose, a pipe, and the like. BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is an example of a processing state of a sheet end which is fused. [Explanation of main component symbols] 1 : Pre-processed sheet 2 : Processed thick sheet 3 : Layer formed of polyolefin resin (A) 4 : Layer (B-1) or layer (B-2) formed by modified polyolefin resin 5 : Layer formed by fluororesin containing an adhesive functional group (C) -52-

Claims (1)

201236867 七、申請專利範圍: 1.一種層合物,其特徵爲,具有 改質聚烯烴樹脂所形成之層(B-1 ),及 B-1)上所形成之含有黏著性官能基之氟樹脂 (C). 二 構成層(B-1 )之改質聚烯烴樹脂爲,具 碳二醯亞胺基之改質聚烯烴, 構成前述層(C)之含有黏著性官能基之 主鏈末端及/或側鏈末端具有對構成前述層(E 聚嫌烴樹脂所具有之官能基顯示反應性之黏著 2·如申請專利範圍第1項之層合物,其中 具有亞胺基之改質聚烯烴爲,於自由基產 下’使聚烯烴與含有多數亞胺基之聚亞胺化合 理而得之亞胺改質聚烯烴, 具有碳二醢亞胺基之改質聚烯烴爲,具有 胺基反應之基的聚烯烴,與含有碳二醯亞胺基 於未改質聚烯烴之存在下進行反應而得之碳二 聚烯烴。 3 .如申請專利範圍第1或2項之層合物, 層(B-1 )上所形成之聚烯烴樹脂所形成之層( 4. 一種層合物,其特徵爲,具有 聚烯烴樹脂所形成之層(A)、改質聚烯 成之層(B-2),及,含有黏著性官能基之氟 之層(C ), ,前述層( 所形成之層 有亞胺基或 氟樹脂,於 5-1 )之改質 性官能基。 生劑之存在 物經接枝處 與碳二醯亞 之化合物, 醯亞胺改質 其尙具有於 A )。 烴樹脂所形 樹脂所形成 -53- 201236867 前述含有黏著性官能基之氟樹脂所形成之層(c), 爲最內層或最外層之至少任一側之層, 構成前述層(C)之含有黏著性官能基之氟樹脂,於 主鏈末端及/或側鏈末端具有對構成前述層(B-2)之改質 聚烯烴樹脂所具有之官能基顯示反應性之黏著性官能基, 前述黏著性官能基,相對於構成含有黏著性官能基之 氟樹脂的全聚合單位100莫耳%,爲0.2〜10莫耳%。 5. 如申請專利範圍第4項之層合物,其中,構成前述 層(B-2 )之改質聚烯烴樹脂所具有之官能基爲,由胺基 、醯胺基、胺甲醯基、羥基、羧基、羧酸鹵化物基 '酯基 、酸酐基、碳酸酯基、環氧基、腈基,及,異氰酸酯基所 成群中所選出之至少1種。 6. 如申請專利範圍第1、2、3、4或5之層合物,其 中,前述黏著性官能基,相對於構成含有黏著性官能基之 氟樹脂的全聚合單位100莫耳%,爲0.2〜5莫耳%。 7·如申請專利範圍第1、2、3、4、5或6項之層合物 ’其中’前述黏著性官能基,相對於構成含有黏著性官能 基之氟樹脂的全聚合單位100莫耳%,爲0.2〜2莫耳%。 8. 如申請專利範圍第1、2、3、4、5、6或7項之層 合物’其中,前述黏著性官能基爲,由胺基' 醯胺基、胺 甲醯基、羥基、羧基、羧酸鹵化物基、酯基 '酸酐基、碳 酸醋基、環氧基、腈基’及,異氰酸醋基所成群中所選出 之至少1種。 9. 如申請專利範圍第1、2、3、4、5、6、7或8項之 -54- 201236867 層合物’其中,前述黏著性官能基爲羧基。 1〇·如申請專利範圍第1、2、3、4、5、6、7、8或9 項之層合物’其中,前述含有黏著性官能基之氟樹脂之融 點爲120〜240°C。 1 1 ·如申g靑專利範圍第 1、2、3、4、5、6、7、8、9 或1〇項之層合物,其中,前述含有黏著性官能基之氟樹 脂之融點爲所含有之黏著性官能基的分解溫度以下。 12 ·如申請專利範圍第1、2、3、4、5、6、7、8、9 或1〇項之層合物,其爲藥液用容器或尿素水用容器。 1 3.如申請專利範圍第1、2、3、4、5、6、7、8、9 或10項之層合物,其爲燃料用容器、飮料用或食品用容 器。 14. 如申請專利範圍第1、2、3、4' 5、6、7、8、9 或10項之層合物,其爲埋設地下之管路或軟管。 15. 如申請專利範圍第1' 2、3、4、5、6' 7' 8、9 或10像之層合物,其爲漏斗頸(Filler Neck)軟管、燃 料軟管,或,燃料管路。 S -55-201236867 VII. Patent Application Range: 1. A laminate characterized by having a layer formed of a modified polyolefin resin (B-1) and a fluorine containing an adhesive functional group formed on B-1) Resin (C). The modified polyolefin resin of the second constituent layer (B-1) is a modified polyolefin having a carbodiimide group, and constitutes a main chain end of the layer (C) containing an adhesive functional group. And/or the end of the side chain has an adhesive which exhibits reactivity with the functional group which the above-mentioned layer (E polypoly hydrocarbon resin has). 2. The laminate of the first aspect of the patent application, wherein the modified polycondensation of the imine group The olefin is a modified polyolefin having a carbodiimide group and a modified polyolefin having a polyimination of a polyolefin and a polyimine group. a base-based polyolefin, which is obtained by reacting a carbodiimide based on an unmodified polyolefin. 3. A laminate according to claim 1 or 2, a layer formed of a polyolefin resin formed on the layer (B-1) (4 a laminate, The layer (A) having a polyolefin resin, the layer (B-2) modified with a polyolefin, and the layer (C) containing fluorine of an adhesive functional group, and the layer formed The layer has an imino group or a fluororesin, and a modifying functional group at 5-1). The presence of the biocide is grafted to the compound of the carbohydrazide, and the quinone imine is modified to have a ruthenium. A resin formed of a hydrocarbon resin-53-201236867 The layer (c) formed of the fluororesin containing an adhesive functional group is a layer of at least either side of the innermost layer or the outermost layer, and constitutes the layer (C). The fluororesin having an adhesive functional group has an adhesive functional group exhibiting reactivity with respect to a functional group of the modified polyolefin resin constituting the layer (B-2) at the end of the main chain and/or at the side of the side chain, The adhesive functional group is 0.2 to 10 mol% with respect to 100% by mole of the total polymerization unit constituting the fluororesin having an adhesive functional group. 5. The laminate according to claim 4, wherein the composition The functional group of the modified polyolefin resin of the above layer (B-2) has an amine group , at least 1 selected from the group consisting of amidoxime, an aminecarbamyl group, a hydroxyl group, a carboxyl group, a carboxylic acid halide group 'ester group, an acid anhydride group, a carbonate group, an epoxy group, a nitrile group, and an isocyanate group. 6. The laminate of claim 1, 2, 3, 4 or 5, wherein the adhesive functional group is 100% by mole relative to the total polymerization unit constituting the fluororesin containing the adhesive functional group. , which is 0.2 to 5 mol%. 7. The laminate of claim 1, 2, 3, 4, 5 or 6 wherein 'the aforementioned adhesive functional group is relative to the composition containing an adhesive functional group. The total polymerization unit of the fluororesin is 100 mol%, and is 0.2 to 2 mol%. 8. The laminate of claim 1, 2, 3, 4, 5, 6 or 7 wherein the aforementioned adhesive functional group is an amino group, an amino group, an amine group, a hydroxyl group, At least one selected from the group consisting of a carboxyl group, a carboxylic acid halide group, an ester group 'anhydride group, a carbonate group, an epoxy group, a nitrile group', and an isocyanate group. 9. The composition of claim 1, 2, 3, 4, 5, 6, 7, or 8 -54 - 201236867, wherein the aforementioned adhesive functional group is a carboxyl group. 1. A laminate of the first, second, third, fourth, fifth, sixth, seventh, eighth or ninth aspect of the patent application, wherein the fluororesin containing the adhesive functional group has a melting point of 120 to 240° C. 1 1 . The laminate of claim 1, 2, 3, 4, 5, 6, 7, 8, 9 or 1 wherein the melting point of the fluororesin containing the adhesive functional group It is below the decomposition temperature of the adhesive functional group contained. 12. A laminate according to claim 1, 2, 3, 4, 5, 6, 7, 8, 9, or 1 of the patent, which is a container for a chemical liquid or a container for a urea water. 1 3. A laminate according to claim 1, 2, 3, 4, 5, 6, 7, 8, 9, or 10, which is a container for fuel, a material for food, or a container for food. 14. A laminate of claim 1, 2, 3, 4' 5, 6, 7, 8, 9 or 10 which is a buried pipeline or hose. 15. For a laminate of patents 1' 2, 3, 4, 5, 6' 7' 8, 9 or 10, which is a funnel neck (Filler Neck) hose, fuel hose, or fuel Pipeline. S-55-
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