TW200835708A - Soluble polymers with high conversion of acid from aromatic epoxy resins and diacids and crosslinked coatings prepared therefrom - Google Patents

Soluble polymers with high conversion of acid from aromatic epoxy resins and diacids and crosslinked coatings prepared therefrom Download PDF

Info

Publication number
TW200835708A
TW200835708A TW96134399A TW96134399A TW200835708A TW 200835708 A TW200835708 A TW 200835708A TW 96134399 A TW96134399 A TW 96134399A TW 96134399 A TW96134399 A TW 96134399A TW 200835708 A TW200835708 A TW 200835708A
Authority
TW
Taiwan
Prior art keywords
epoxy
resin
acid
molecular weight
polymer
Prior art date
Application number
TW96134399A
Other languages
Chinese (zh)
Inventor
Maurice J Marks
Roy V Snelgrove
Original Assignee
Dow Global Technologies Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Dow Global Technologies Inc filed Critical Dow Global Technologies Inc
Publication of TW200835708A publication Critical patent/TW200835708A/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G59/00Polycondensates containing more than one epoxy group per molecule; Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups
    • C08G59/18Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups ; e.g. general methods of curing
    • C08G59/182Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups ; e.g. general methods of curing using pre-adducts of epoxy compounds with curing agents
    • C08G59/186Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups ; e.g. general methods of curing using pre-adducts of epoxy compounds with curing agents with acids
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D163/00Coating compositions based on epoxy resins; Coating compositions based on derivatives of epoxy resins

Landscapes

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

Abstract

An uncrosslinked, soluble, epoxy terminated high molecular weight epoxy ester resin having an acid number of less than about 5 comprising the reaction product of a low molecular weight epoxy resin and a dicarboxylic acid; and a coating produced from the uncrosslinked, soluble, epoxy terminated high molecular weight epoxy ester resin.

Description

200835708 九、發明說明: 【發明所屬之技術領域】 本發明關於自低分子量芳香族環氧樹脂與二竣酸類而 衣備之未經交聯之可溶性高分子量環氧酯樹脂。 二之可溶性高分子量環氧酯樹脂有利地用於製備來自該产 氧樹脂之經交聯塗層。 Λ哀 【先前技術】 肇 用於金屬之保護塗層為環氧樹脂的最先應用之一,而 ^彼等作為金屬食品及飲料容器之内部塗層的用途為彼= 最大市場之一。典型地,用於金屬食品及飲料容器之内部 保護塗層係自高分子量環氧樹脂而製得。而且典型地 等高分子量環氧樹脂係藉由低分子量環氧樹脂(如雙酚1 之二環氧丙基醚)與含羥基之單體(如雙酚Α)反應而製得。 雙酚Α與雙酚a二環氧丙基醚之環族反應產物,又稱=環 族二聚物,時常自塗層調配溶液沉澱,造成加工設備的: • 木’且伴隨生產力損失及廢物產生。食品及飲料罐工業始 尋找一種技術,可以從製造環氧熱固性内部容器塗層之^ 法來減低或消除該等問題。 一绩SiL類代表一廣泛類別之潛在有效材料,其可使用 於和低分子量環氧樹脂之反應中,以製備較高的分子量環 氧酯樹脂。然而,根據已知用於製備高分子量環氧樹脂之 方法,使用二羧酸類會引導經交聯之不可溶性聚合物的形 成。工業上需要的是使二羧酸作為共單體與環氧樹脂單體 反應的方法,而導致未經交聯之可溶性環氧官能性聚合 5 200835708 物0 有許多已知方法敎示使用二羧酸類及環氧樹脂,如美 國專利第4,722,981號,美國專利公開第2〇〇2〇128428A1 號及歐洲專利公開第0501575A2號。然而,美國專利第 4,722,981號及美國專利公開第2〇〇2〇128428ai號未敎示 使用一羧酸類作為共單體;而且在〇5〇15乃八2中所揭 示之方法只使用二羧酸類作為催化劑,不作為共單體。因 此,在上述先丽技藝中敎示的方法未製造以環氧基為末端 的未經交聯之可溶性高分子量環氧酯樹脂。 許多其他已知的方法敎示二環氧化物及二羧酸類的使 用,如在美國專利第5,962,621號,第5,8S2,163號及第 5,780,582號中所揭示之方法。然而,該等文獻未揭示以環 氧基為末端之羥基官能性聚酯類。 其他的文獻,如 Suzuki,Akira; Kameyama,Atsushi; Nishikubo, Tadatomi, Kobunshi Ronbunshu (1996), 53(9), 522-529; Alvey5 Francis B.? Journal of Polymer Science, 及 Dusek, K, Matejka, L; Advances in Chemistry Series 1984, 208, 15 教示自環氧樹脂及二羧酸合成高分子量聚醋。然而,在該 等文獻中所揭示之方法使用等莫耳量之環氧化物及二魏 酸’因此,以該等已知方法所獲得的樹脂產物:(1)不具有 環氧官能性,(2)包括大量的未反應之二羧酸,或(3)經歷膠 凝化。 美國專利第4,829,M1號及第45302,574號;及加拿大 6 200835708 專利第1091690號捃-址m 它卜、 -不使用環氧樹脂與羧酸類的反應,但 疋该寺文獻未敎示以環轰 心 一 分子量環氧酯樹脂。 合性同 其他的文獻可能姐- , 献j靶揭不二羧酸類的使用,但 用二羧酸作為共單體盥芸 破不使 為末端之未經交聯之八P 表備^%虱基 < j /合性鬲分子量環氧樹脂之 如,美國專利第3,864 316 斤 η 你〆 ,旎及弟4,474,935號揭示用於製 備氯化,即非芳香族環轰 、衣 號揭示用於製備含有_取I ,171,820 "有經甲基之經基官能性聚酯之方法·及 WO 0001779A1揭示含右俨 > 取 万法,及 、 衣虱_聚酯嵌段共聚物及交聯劑之 塗覆組成物,其中環句MSk 性。 中衣私、醋後段#聚物全部具有酸官能 希望猎由低分子量苦悉# 徂一插去^ 香私衣乳树脂與二羧酸反應而提 ; 父聯之可溶性環氧基為末端之高分子量環氧醋 樹脂,其中該等未經交聯之可溶性環氧基為末端:::; 量環氧醋樹脂可接著與交聯劑反應,形成塗層。-刀 【發明内容】 =_點_於新賴的未經交聯之可溶性環 2為末端之高分子量環氧酯樹脂,其具有環氧基末端及 鬲的幾酸基團轉化率。 在一個具體貫例中,本發明雜μ + μ明新頭的未經交聯之可溶性 衣乳基為末端之高分子量環氧酯樹脂係藉由低分子量芳夭 族環氧樹脂與二竣酸類反應而製得。由於環氧醋樹脂的: 平飞g能度,故可將該樹脂用作環氧熱固物之前驅體,包括 7 200835708 藉由與交聯劑, 之塗層。 如可_路樹脂(沖咖HCresoles)交聯 本發明的另-個觀點係、關於 的新穎環氧醋塗芦,m 有則土的性質平衡 樹脂與各式夂樣;^ 猎由上述可溶性高分子量環氧醋 的-個主要:的為:::反應而形成。新穎的環氧S旨塗層 的為用於食品或飲料罐及/或罐蓋的内部。 【貫施方式】200835708 IX. Description of the Invention: [Technical Field of the Invention] The present invention relates to a solvent-free high-molecular-weight epoxy ester resin which has been uncrosslinked from a low molecular weight aromatic epoxy resin and a diterpenic acid. A soluble high molecular weight epoxy ester resin is advantageously used to prepare a crosslinked coating from the oxygen generating resin.先前 【 【Prior Art】 保护 Protective coatings for metals are one of the first applications of epoxy resins, and their use as internal coatings for metal food and beverage containers is one of the largest markets. Typically, internal protective coatings for metal food and beverage containers are made from high molecular weight epoxy resins. Moreover, typically high molecular weight epoxy resins are prepared by reacting a low molecular weight epoxy resin such as diglycidyl ether of bisphenol 1 with a hydroxyl containing monomer such as bisphenolphthalein. The cyclic reaction product of bisphenol hydrazine and bisphenol a diglycidyl ether, also known as = cyclodimer, often precipitates from the coating solution, causing processing equipment: • wood' with productivity loss and waste produce. The food and beverage can industry is looking for a technology that can reduce or eliminate such problems from the manufacture of epoxy thermoset internal container coatings. A class SiL class represents a broad class of potentially effective materials that can be used in the reaction with low molecular weight epoxy resins to produce higher molecular weight epoxy ester resins. However, according to the known methods for preparing high molecular weight epoxy resins, the use of dicarboxylic acids leads to the formation of crosslinked insoluble polymers. What is needed in the industry is a method of reacting a dicarboxylic acid as a comonomer with an epoxy resin monomer, resulting in a non-crosslinked soluble epoxy functional polymerization. 5 200835708 0 There are many known methods for the use of dicarboxylic acid. Acids and epoxies, such as U.S. Patent No. 4,722,981, U.S. Patent Publication No. 2,128,428 A1, and European Patent Publication No. 0501575 A2. However, the use of monocarboxylic acids as comonomers is not indicated in U.S. Patent No. 4,722,981 and U.S. Patent No. 2,128,428, the disclosure of which is incorporated herein by reference. As a catalyst, it is not used as a comonomer. Therefore, the method disclosed in the above-mentioned prior art does not produce an uncrosslinked soluble high molecular weight epoxy ester resin terminated with an epoxy group. A number of other known methods are used to illustrate the use of diepoxides and dicarboxylic acids, such as those disclosed in U.S. Patent Nos. 5,962,621, 5,8,2,163, and 5,780,582. However, such documents do not disclose hydroxy-functional polyesters terminated with an epoxy group. Other literature, such as Suzuki, Akira; Kameyama, Atsushi; Nishikubo, Tadatomi, Kobunshi Ronbunshu (1996), 53(9), 522-529; Alvey5 Francis B.? Journal of Polymer Science, and Dusek, K, Matejka, L Advances in Chemistry Series 1984, 208, 15 teaches the synthesis of high molecular weight polyesters from epoxy resins and dicarboxylic acids. However, the methods disclosed in these documents use an equimolar amount of epoxide and diveric acid. Thus, the resin product obtained by these known methods: (1) does not have epoxy functionality, ( 2) including a large amount of unreacted dicarboxylic acid, or (3) undergoing gelation. U.S. Patent Nos. 4,829, M1 and 45,302,574; and Canada 6 200835708 Patent No. 1091690 - address m - do not use epoxy resin and carboxylic acid reactions, but the temple literature does not show The ring is a molecular weight epoxy ester resin. Synergy and other literature may be sister--, the purpose of the use of dicarboxylic acid, but the use of dicarboxylic acid as a co-monomer to break the end of the uncrosslinked eight P table preparation ^%虱The base < j / conjugated ruthenium molecular weight epoxy resin, for example, U.S. Patent No. 3,864,316 jin η, 〆, 旎 and 4, 474, 935, discloses the preparation of chlorination, that is, non-aromatic ring bombardment, and the coating number is disclosed for preparation. a method comprising _ taking I, 171, 820 " a methyl group-based functional polyester; and WO 0001779 A1 discloses a right 俨 取 method, and, 虱 _ polyester block copolymer and A coating composition of a crosslinking agent, wherein the ring sentence is MSk. In the middle of the private, vinegar after the #polymer all have acid function hope to hunt from the low molecular weight of the pain of the # 徂 一 inserted ^ Xiang private clothing milk resin and dicarboxylic acid reaction; the father's soluble epoxy is the end of the high A molecular weight epoxy vinegar resin in which the uncrosslinked soluble epoxy groups are terminal:::; The amount of the epoxy vinegar resin can then be reacted with a crosslinking agent to form a coating. - Knife [Summary of the Invention] =_点_ The uncrosslinked soluble ring 2 of Xinlai is a terminal high molecular weight epoxy ester resin having an epoxy group terminal and a few acid group conversion ratio of ruthenium. In a specific example, the uncrosslinked soluble lacquer base of the present invention is a high molecular weight epoxy ester resin based on a low molecular weight linalyl epoxy resin and a diterpenic acid. Produced by reaction. Because of the epoxy resin's ability to use the resin, it can be used as a precursor for epoxy thermosets, including 7 200835708 by coating with a crosslinking agent. For example, _Lu resin (Chongdu HCresoles) cross-linking another aspect of the invention, the novel epoxy vinegar coated reed, m has the nature of the balance of the resin and various types of sputum; ^ hunting by the above soluble high The molecular weight of the epoxy vinegar is mainly formed by::: reaction. The novel epoxy S coating is for use in the interior of food or beverage cans and/or can ends. [Continuous application method]

本發明包括-種新穎的組成物,其含有具有環氧 端及南㈣酸基團轉化率或低的酸值之產物。本發明: =藉由低分子量環氧樹脂與二羧酸類反應而製 t、經父聯之可溶性環氧基為末端之高分子量環氧醋樹 脂,:於該樹脂的環氧官能度’故可將彼等用作環氧熱固 物之刚驅體,包括藉由與可溶酚酸樹脂交聯之塗層。本發 日:的未經交聯之可溶性環氧基為末端之高分子量^氧醋樹 脂組成物在本文被稱為、\固體環氧酯樹脂/7或、、seer〃 , 以區別本發明的環氧樹脂與得自低分子量環氧樹脂及雙酚 A之熟知的、、固體環氧樹脂"或、、SER/,。 v、未經交聯〃意指組成物具有限定的黏度及沒有顯著 的凝膠狀反應產物。 可洛性意指組成物溶解在適合的有機溶劑中。 ^高分子量〃意指組成物具有的分子量為開始的環氧 樹脂之至少約2倍,較佳為至少約3倍。 、、酸值"意指根據ASTM D 1639-83所述之步驟用於 中和1公克(g)樣品所必需的ΚΟΗ量(以毫克(mg)計)。 8 200835708 ''高的羧酸基團轉化率"意指二羧酸的_部分及中 間物貫質上完全反應,如以組成物的酸值所测量,使得酸 值小於約5。 " 本發明的環氧樹脂可藉由各種方法製備,包括例如在 與其-天提出中請之美國專利中請案,代理人案號65彻 中所述之方法,將其以引用方式納入本文中。The present invention includes a novel composition comprising a product having an epoxy terminal and a south (tetra) acid group conversion or a low acid value. The present invention: = a high molecular weight epoxy vinegar resin which is prepared by reacting a low molecular weight epoxy resin with a dicarboxylic acid to form a terminal, and a soluble epoxy group having a reactive epoxy group as a terminal: in the epoxy functionality of the resin They are used as rigid conductors for epoxy thermosets, including coatings that are crosslinked with a soluble phenolic resin. The present invention is a high molecular weight oxyacetate resin composition which is not crosslinked and has a soluble epoxy group as a terminal. It is referred to herein as a solid epoxy ester resin/7 or a seer® to distinguish the present invention. Epoxy resins and well-known, solid epoxy resins derived from low molecular weight epoxy resins and bisphenol A, or SER/. v. Uncrosslinked 〃 means that the composition has a defined viscosity and no significant gelatinous reaction product. Coulomb means that the composition is dissolved in a suitable organic solvent. By high molecular weight 〃 means that the composition has a molecular weight of at least about 2 times, preferably at least about 3 times, of the starting epoxy resin. , acid value " means the amount of ruthenium (in milligrams (mg)) necessary to neutralize 1 gram (g) of the sample according to the procedure described in ASTM D 1639-83. 8 200835708 ''High carboxylic acid group conversion rate" means that the _ moiety and the intermediate of the dicarboxylic acid are completely reacted qualitatively, as measured by the acid value of the composition, such that the acid value is less than about 5. " The epoxy resins of the present invention can be prepared by a variety of methods, including, for example, the method described in U.S. Patent Application Serial No. 65, the entire disclosure of which is incorporated herein by reference. in.

例如,在美國專利申請案,代理人案號05280中所述 之方法包含將低分子量環氧樹脂與二羧酸視需要在另一種 二官能性單體,如錢A的存在下反應,該反應係在催化 劑存在下的溶液中以至多約22(rc之反應溫度下進行,以 形成本發明的未經交聯之可溶性高分子量環氧酯樹脂。 較佳地,二羧酸與環氧樹脂組份的反應係在溶液中及 在惰性反應稀釋劑的存在下進行。反應稀釋劑較佳為用於 環氧樹脂或與其可混溶之溶劑。可使用可溶解單體至適當 私度及在大氣壓、低大氣壓或超大氣壓力下可被加熱至適 田的反應μ度並且不干擾羧酸部分與環氧化物部分反應 的任何惰性有機溶劑。實質上希望沒有雜質的溶劑,雜質 曰IV低催化刈,如過氧化氫或未錯合之過渡金屬離子的反 應性。 適合的溶劑實例包括„比咬,三乙胺或其混合物;Ν_ 基吡咯烷酮(ΝΜΡ) ’苯甲酸甲醋,苯甲酸乙醋,苯甲1 丁醋,環戊酮’環己酮,環庚酮,環辛酮,?衰己基吡咯 酮;及醚類或羥基醚類,如二腭烷,二甘醇二曱醚,三 醇二曱醚,二甘醇乙醚,二甘醇甲醚’二丙二醇曱醚, 9 200835708 丙二酵二曱醚,丙二醇苯醚,丙二醇甲醚乙酸酯,丙二醇 甲鱗及三丙二醇甲醚;甲苯,均三甲苯,二甲苯,苯,二 丙二醇單甲醚乙酸酯,鹵化溶劑,如二氯苯,碳酸丙烯酯, 奈’二苯_,丁内酯,二甲基乙醯胺,二甲基曱醯胺,酯 類’如乙酸乙酯或乙酸丁酯及其混合物。其他適合的稀釋 劑為有機化合物者,其在反應溫度下對反應物具有惰性, 例如’各種乙二醇醚類,如乙二醇乙鱗,乙二醇或丙二醇 單甲醚及其酯類,如乙二醇單乙醚乙酸酯;酮類,如甲基 異丁酮,甲基乙酮(ΜΕΚ)及丙酮;及芳香族烴類,如甲 笨一甲苯,環己烷或其混合物。較佳的溶劑為環己酮及 丙二醇甲醚乙酸酯。溶劑通常係以所有反應物的總重量為 :準计彳丈、’々5至約300%之量被使用。如果所得樹脂產物 係以塗佈為目的而被使用時,則溶劑典型地被保留在反應 混合物中。另外,溶劑係藉由任何方法移除,&蒸館或類 似方法。For example, in U.S. Patent Application Serial No. 05,280, the method of reacting a low molecular weight epoxy resin with a dicarboxylic acid as needed in the presence of another difunctional monomer such as money A, the reaction It is carried out in a solution in the presence of a catalyst at a reaction temperature of up to about 22 (rc) to form the uncrosslinked soluble high molecular weight epoxy ester resin of the present invention. Preferably, the dicarboxylic acid and epoxy resin group The reaction is carried out in solution and in the presence of an inert reaction diluent. The reactive diluent is preferably used as an epoxy resin or a solvent miscible with it. The soluble monomer can be used to the appropriate degree of inertia and at atmospheric pressure. At low atmospheric pressure or superatmospheric pressure, it can be heated to the reaction range of the field and does not interfere with any inert organic solvent in which the carboxylic acid moiety reacts with the epoxide moiety. Substantially desirable solvents without impurities, impurities 曰IV low catalytic enthalpy Reactivity such as hydrogen peroxide or unaltered transition metal ions. Examples of suitable solvents include „Bite, triethylamine or mixtures thereof; Ν_pyrrolidone (ΝΜΡ) 'benzoic acid A Vinegar, benzoic acid ethyl vinegar, benzoic acid 1 butyl vinegar, cyclopentanone 'cyclohexanone, cycloheptanone, cyclooctanone, ?-hexyl pyrrolidone; and ethers or hydroxy ethers, such as dioxane, digan Alcohol dioxime ether, triol dioxime ether, diethylene glycol ethyl ether, diethylene glycol methyl ether 'dipropylene glycol oxime ether, 9 200835708 propylene diacetate, propylene glycol phenyl ether, propylene glycol methyl ether acetate, propylene glycol methyl scale And tripropylene glycol methyl ether; toluene, mesitylene, xylene, benzene, dipropylene glycol monomethyl ether acetate, halogenated solvent, such as dichlorobenzene, propylene carbonate, naphthene, butyrolactone, dimethyl Ethyl amide, dimethyl decylamine, esters such as ethyl acetate or butyl acetate and mixtures thereof. Other suitable diluents are organic compounds which are inert to the reactants at the reaction temperature, for example ' Various glycol ethers, such as ethylene glycol scales, ethylene glycol or propylene glycol monomethyl ether and esters thereof, such as ethylene glycol monoethyl ether acetate; ketones such as methyl isobutyl ketone, methyl ethyl Ketones and acetonides; and aromatic hydrocarbons such as methyl benzene, cyclohexane or mixtures thereof. The agent is cyclohexanone and propylene glycol methyl ether acetate. The solvent is usually used in an amount of from about 5 to about 300% based on the total weight of all the reactants. If the obtained resin product is coated When used for the purpose, the solvent is typically retained in the reaction mixture. Alternatively, the solvent is removed by any method, & steaming or the like.

一,八w "貝甲便用的單體濃度係依 據各種因素而$,包括特殊的單體、所使料溶劑及欲製 ::聚合物。通常’使用0·60: i 〇至〇95: i 〇之羧酸對 環氧之化學計量比的單體。 在本發明中所使用的低分 里衣乳树月曰包括聚環氧化 物,其為母一分子具有一個以上 工岫近的%乳基團之化合 ,即母一分子具有一個以上的 ^ 1U衣氧基團。該奪;帶撰 虱化物為飽和或不飽和芳香族聚 、Λ ..^ 衣乳化物,若必要時,立 被热干擾物質,如鹵素原子,羥, … 二土,醚基及類似物取代。 10 200835708 ''低分子量"環氧樹脂意 Λ认队 〜和具有數量平均分子量(Μη) 、;、力10,000之芳香族環氧 巩树脂珂驅體,較佳地小於約 ,〇〇〇,而更佳的地小於約 的、、你八工旦通常,在本發明中有用 、 低刀子里環氧樹脂前驅體且古/Μ 觀具有從約200至約10 〇〇〇 之數量平均分子量,較佳地 攸、、勺2〇〇至約8,000,而更佳 地從約250至約4,0〇〇。 較佳的低分子量環氣椒Η匕生 虱树月曰為液體聚環氧化物,其包括 例如多元酚之液體環氧丙基臂 曰 & *蜒類。更佳的是具有平均分 子量介於約340至約900夕Ώ而 之間及%氧化物當量介於約17〇 至約500之間的2,2-雙(4-_ 1 |、二a 、 又1匕本基)丙烷之環氧丙基聚醚類。 尤其較佳的是具有平均分+吾人 J刀于里)丨於約340至約900之間, :氧化物當量介於約170至約5〇〇之間及含有從約〇 〇1重 里^至約1·0重或更兩的可皂化之氯的2,2•雙(4_羥苯 基)丙烷之環氧丙基聚_類。如本文所使用的術語、環氧化 物畜里及、'每一環氧化物計之重量U聚環氧化物分 子之平均分子量除以存在於分子中的環氧乙烷基團之平均 數0 可在本發明的實施中使用的二環氧化物包括二元酚之 二環氧丙基醚類,如在美國專利第5,246,751號,第 5,115,〇75 號,第 5,089,588 號,第 4,480,082 號及第 4,438,254 號中所述者,將全部以引用方式納入本文中,或芳香族二 魏酸之二環氧丙基酯類,如在美國專利第5,171,82〇號中 所述者,將其以引用方式納入本文中。其他適合的二環氧 化物包括市售已知為D.E.R·⑯300及6〇〇系列環氧樹脂及 11 200835708 市售取自 The Dow Chemical Company 之以 α 一 甘-* ’ -一環氧丙 基氧基異亞丙基-雙酚為主之環氧樹脂。較佳的― 展氧化物 為具有環氧當量從約1〇〇至約4000之環氧樹脂。最彳土、 二環氧化物為雙酚A之二環氧丙基醚類,4,4入績酿基一酶 4,4-氧基二酚,4,4,·二羥基二苯甲酮,間笨二酚,氫酉昆,9 9,· 雙羥苯基)第,4,4,-二羥基聯苯或4,4,-二羥美田’ 一— 工土 曱基 二本乙烯及先前所述之二羧酸之二環氧丙基酯類。該等芳 香族二環氧化物趨向二羧酸類的反應性更甚於非芳香族一 環氧化物,並因此更傾向於交聯或膠凝。在本發明中,驚 訝的是未經交聯之可溶性樹脂產物係使用該等芳香族二^ 氧化物而製備。 、 4 所使用的環氧樹脂量係依據目標分子量及環氧官能度 而疋通吊,環氧樹脂係以反應物重量為基準計從約3〇 重置%至約85重量%之量被使用,更佳地從約40重量% 至約75重量%,而最佳地從約45重量%至約重量%。 ^ =本發明中所使用的羧酸類可為例如飽和,不飽和, 月曰肪無’ %脂肪族,芳香族或雜環族。該等酸類的實例尤 其包:丁二酸,戊二酸,己二酸(AA),庚二酸,辛二酸, 尸I力一酸,草酸,松脂酸,順丁烯二酸,烏頭酸, f橋酉夂(ehl〇rendle aeid),苯二甲酸(pA),對苯二甲 :一(PA),異苯二甲酸(IPA),2,6-萘二叛酸,3,4,-聯 苯羧西文4,4 -聯苯二羧酸,丙二酸,込和環己烷二羧酸, 1,10,癸炫二薄醅 _ 環s夂 m十二烷二羧酸,13-環己烷二羧酸 (1,3 CIIDA) ’ l4·環己烷二幾酸(1,4-CHDA),酒石酸, 12 200835708 払J齩及搜基戊二酸。更佳的羧酸類包括對苯二甲酸,異 苯二曱酸,己二酸及其混合物。 錄在=發明中所使用的羧酸量可以在廣泛的範圍中改 通常’在本發明中所使用的賴量係以反應物重量為 〇土準汁攸約1重量%至約50重量%,更佳地從約5重量 %至約45重量%,而最佳地從約1〇重量%至約4〇重量 —▲低分子量環氧化物與羧酸之反應混合物可視需要在二 官能性單體,如含羥基或硫醇基之化合物,如酚或硫酚的 :在下進行。較佳的視需要之含羥基之化合物為具有至少 ^個搜基連接於芳香族核之身類。賴可為單it或多元酚 類’亚可經取代或未經取代。聚合多㈣類可藉由縮合單 凡或多元酚類與甲醛而獲得。 夕較佳的視需要之酚類為含有從2至6個OH基團及至 夕30個石反原子之多元酚類,包括以下式代表者:The monomer concentration used in the first and eighth w " beetle is based on various factors, including special monomers, solvent and desired polymer. Typically, a monomer that uses 0. 60: i 〇 to 〇 95: i 〇 carboxylic acid to epoxy stoichiometric ratio. The low-division Lactobacillus sinensis used in the present invention comprises a polyepoxide which is a combination of more than one % of the emulsion groups of the parent molecule, that is, the parent molecule has more than one ^ 1U Alkoxy groups. The sputum is a saturated or unsaturated aromatic poly-, Λ.. clothing emulsion, if necessary, the vertical is replaced by thermal interference substances, such as halogen atoms, hydroxyl, ... soil, ether and analog . 10 200835708 ''Low Molecular Weight'' Epoxy Resin ~ and an aromatic epoxy scavenger having a number average molecular weight (Μη),; 10,000, preferably less than about 〇〇〇, More preferably, it is less than about, and it is generally useful in the present invention that the epoxy resin precursor in the low knife has an average molecular weight of from about 200 to about 10 Å. Preferably, 攸, scoop 2 〇〇 to about 8,000, and more preferably from about 250 to about 4,0 。. The preferred low molecular weight cyclic sorghum eucalyptus is a liquid polyepoxide comprising, for example, a liquid epoxy propyl arm of the polyhydric phenol & More preferably, 2,2-bis(4-_1 |, a a, having an average molecular weight of between about 340 and about 900 及 and between % and/or 500 equivalent of an oxide equivalent. Another 1 匕 base) propane epoxy propyl polyether. It is especially preferred to have an average score of + about 340 to about 900, and an oxide equivalent of between about 170 and about 5 Å and containing from about 1 to about Epoxypropyl poly-type of 2,2•bis(4-hydroxyphenyl)propane of about 1. 0 weight or more of saponifiable chlorine. As used herein, the term epoxide and the average molecular weight of the weight of each polyepoxide molecule per epoxide divided by the average number of oxirane groups present in the molecule is 0. The diepoxides used in the practice of the present invention include diglycidyl ethers of dihydric phenols, such as in U.S. Patent Nos. 5,246,751, 5,115, 〇75, 5,089,588, 4,480,082 and U.S. Patent No. 4,438,254, the entire disclosure of which is incorporated herein by reference in its entirety, in its entirety, in Incorporate this article by reference. Other suitable diepoxides include commercially available DER·16300 and 6〇〇 series epoxy resins and 11 200835708 commercially available from The Dow Chemical Company as α-Gan-* '--epoxypropyloxy An epoxy resin based on isopropylidene-bisphenol. Preferred oxides are those having an epoxy equivalent weight of from about 1 Torr to about 4,000. The most bauxite, the diepoxide is the di-epoxypropyl ether of bisphenol A, 4,4 is the base of the enzyme, 4,4-oxydiphenol, 4,4,·dihydroxybenzophenone , stupid phenol, hydroquinone, 9 9, · bishydroxyphenyl), 4,4,-dihydroxybiphenyl or 4,4,-dihydroxy-meta-'-- Diethylene propyl esters of dicarboxylic acids previously described. These aromatic bis-epoxides tend to be more reactive toward dicarboxylic acids than non-aromatic monoepoxides and are therefore more prone to cross-linking or gelation. In the present invention, it is surprising that the uncrosslinked soluble resin product is prepared using the aromatic bisoxide. 4 The amount of epoxy resin used is entangled according to the target molecular weight and epoxy functionality. The epoxy resin is used from about 3 〇 to % 85% by weight based on the weight of the reactants. More preferably, it is from about 40% by weight to about 75% by weight, and most preferably from about 45% by weight to about 3% by weight. ^ = The carboxylic acid used in the present invention may be, for example, saturated, unsaturated, and oligo-% aliphatic, aromatic or heterocyclic. Examples of such acids include, in particular, succinic acid, glutaric acid, adipic acid (AA), pimelic acid, suberic acid, cadaveric acid, oxalic acid, rosin acid, maleic acid, aconitic acid. , f 酉夂 (ehl〇rendle aeid), phthalic acid (pA), p-xylene: one (PA), isophthalic acid (IPA), 2,6-naphthalene diteric acid, 3, 4, -biphenylcarboxy-mes 4,4-diphenyldicarboxylic acid, malonic acid, hydrazine and cyclohexanedicarboxylic acid, 1,10, fluorene dioxime _ ring s夂m dodecanedicarboxylic acid, 13-cyclohexanedicarboxylic acid (1,3 CIIDA) 'l4·cyclohexanedicarboxylic acid (1,4-CHDA), tartaric acid, 12 200835708 払J齩 and serotonic acid. More preferred carboxylic acids include terephthalic acid, isophthalic acid, adipic acid, and mixtures thereof. The amount of carboxylic acid used in the invention can be varied in a wide range. The amount used in the present invention is about 1% by weight to about 50% by weight based on the weight of the reactants. More preferably from about 5% by weight to about 45% by weight, and most preferably from about 1% by weight to about 4% by weight - ▲ a reaction mixture of a low molecular weight epoxide and a carboxylic acid may optionally be in a difunctional monomer For example, a compound containing a hydroxyl group or a thiol group, such as a phenol or a thiophenol: is carried out below. Preferably, the optionally hydroxyl group-containing compound is one having at least one of a group attached to an aromatic nucleus. The lysole may be substituted or unsubstituted with a single or polyphenolic phenol. The poly(4) group can be obtained by condensing mono- or polyphenols with formaldehyde. Preferably, the preferred phenol is a polyhydric phenol having from 2 to 6 OH groups and up to 30 stone anti-atoms, including the following formulae:

其中X為多價成員或基,且每一個R獨立選自氫,鹵 2及烴基。以X代表的較佳的基為氧,硫,_s〇…, :有至多1〇個碳原子之二價烴基及含氧,矽,硫或氮之 ^基。較佳的齡為2,2_雙(4_羥苯基)丙烷(雙盼_幻,其 中每一個反為》及X為異亞丙基。 八 13 200835708 可在本發明實施使用之用於製備本發明的樹脂的較佳 二元酚類包括4,4,-異亞丙基雙酚(雙酚A) ,4,4、二經基 二苯基乙基曱烷,3,3’-二羥基二苯基二乙基甲烷,3,4,_二 羥基二苯基-曱基丙基甲烷,雙酚,4,4’-二羥基-二苯,4,4,_ 二羥基二苯基氰基甲烷,4,4,-二羥基聯苯,4,4、二羥基二 苯甲酮,4,4、二羥基二苯硫醚,4,4,-二羥基二苯碾,2,6-二羥萘,1,4、二羥萘,酚,間苯二酚,鄰-二曱酚,間_二 甲酚,對-二曱酚,氯酚,硝苯酚,氫醌,2,2-雙(4-羥苯基) 丙院’ 2,2-雙(4-羥苯基)戊烷,兒茶酚,!|化雙酚,如四溴 基雙酚Α及在美國專利第3,395,118號,第4,43 8,254號及 第4,480,082號中所列之其他二元酚類,將彼等以引入方 式納入本文中。此外,可使用不同的二元酚類之混合物。 在該等二元酚類之中,以雙酚A,氫醌及其混合物最佳。 在本發明中所使用的酚量係依據酚的分子量、環氧化 物的分子量、與SEER之目標當量及支化程度而定。通常, 紛係以反應物重量為基準計從約1重量%至約6〇重量% 之量被使用,更佳地從約5重量%至約5〇重量%,而最 佳地從約20重量%至約45重量%。 通常,低分子量環氧樹脂與二羧酸的反應需要催化劑 或能夠催化反應的任何材料。在製備本發明的環氧樹脂 時,將二羧酸與環氧樹脂組份在一種用於在二羧酸之羧酸 基團與環氧樹脂之環氧基團之間的反應之催化劑存在下及 在足以形成所欲樹脂的條件下接觸。 在本發明中有用的催化劑包括(但不限於此)膦,胺, 14 200835708 四級銨及銷鹽,如氯化四乙基銨,溴化四乙基銨,碘化四 乙基銨,氫氧化二乙基銨,氯化四(正丁基)銨,溴化四(正 丁基)銨(ΊΈΑΒ),蛾化四(正丁基)銨,氫氧化四(正丁基) 銨,氯化四(正辛基)銨,溴化四(正辛基)銨,碘化四(正辛 基)鉍,氫氧化四(正辛基)銨,氯化甲基參(正辛基)銨,氯 化雙(四苯基亞磷烷基)銨,乙酸乙基三_對_甲苯基鱗/乙酸 錯合物,乙酸乙基三苯基鱗/乙酸錯合物,N_甲基嗎啉, _ 2_苯基咪唑或其組合物及如在美國專利第5,208,317號,第 5,109,099 #u及帛4,981,926號中所述之類似物,將彼等以 丨方式、、内入本文中。最佳的催化劑包括溴化四丁基鱗 (TBPB),溴化四乙基銨,氫氧化四乙基銨,乙酸乙基三 甲苯基鱗,乙酸乙基三苯基鱗及N_甲基嗎啉,2_苯基咪唑 (2-Phlm) 〇 雖然可使用能夠催化反應的任何材料,但是較佳的催 化劑為鑌鹽催化劑。較佳的鑌鹽催化劑包括鱗或錢鹽催化 • 劑。更佳的鑌鹽催化劑包括溴化四丁基銨,溴化四丁基鱗 (TBPB ),碘化乙基三苯基鱗,溴化四苯基鱗及溴化肆(正 丁基)銨及對應之氯化物,碘化物,溴化物,乙酸鹽,甲酸 鹽,磷酸鹽,硼酸鹽,三氟乙酸鹽,草酸鹽及碳酸氫鹽, 以漠化四丁基鱗(TBPB )最佳。 所使用的催化劑量係依據催化劑分子量、催化劑活性 及意欲進行聚合的速度而定。在本發明的方法中所使用的 催化J里可在寬廣的範圍内改變,只要有催化的量存在即 可。通常,在本發明中所使用的催化劑量係落在以全部反 15 200835708 應物重里5十從1勺0·〇〇ι%至約ίο%之範圍θ,較佳地從約 0 · 0 01 % 至約 5 ^ ’更佳地從約〇·〇〇2%至約2%,而最佳地 以反應物重量計從約0.03%至約1%。 通¥ ’本發明的環氧樹脂組成物可藉由低分子量芳香 無I氧树知與二羧酸在催化劑的存在下及在溶劑的存在下 以足以形成未交聯之可溶性高分子量環氧酯樹脂的條件下 反應而製備。 _ 雨分子量”環氧樹脂意指具有數量平均分子量(Μη ) ; 〇’⑽0之環氧樹脂產物,較佳地小於約1 〇,〇〇〇,而 更么的地小於約8,000。通常,在本發明中有用的、、高分 子里J衣氧樹脂具有從約1,000至約20,000之數量平均分 較"ί土地攸約1,〇 Q 〇至約1 〇,⑼〇,而更佳地從約1,2 〇 〇 至約8,0〇〇。 用於製備本發明的SEER之反應可使用在反應擠壓器 斤進行的批_人法或連續法完成,如在歐洲專利第Ep • 0193 809號中所述。本發明的方法可在開放式容器中或在 播壓器中或在注射成型機中進行。 最有利於進行聚合反應的條件係依據各種因素而定, 包括所使用的特殊反應物、所使用的溶劑及所使用的催化 劑。通常,反應係在非氧化氛圍,如氮氣或其他惰性氣體 s下進行。希望使用對反應物而言的惰性有機溶劑,以確 保均勻的反應混合物及調節在該等溫度下的放熱反應。 在本發明的方法中所使用的反應條件可改變。最有利 於使用的時間及溫度係依據所使用的特殊單體、特別為彼 16 200835708 等的反應性、特殊的寡聚物及有機液體而改變。然而,通 常形成聚酿之反應的合宜速度係在從約5 至約3 〇 〇 °c之 範圍内的反應溫度下、在從約大氣壓力至約15〇 psig為範 圍之反應壓力下及從約30分鐘至約24小時之反應時間下 獲得。 壞氧樹脂與羧酸之反應有利地在提升溫度下進行。反 應溫度較佳地為從約6(rc至約22〇t ’更佳地從約i〇(rcWherein X is a polyvalent member or group, and each R is independently selected from the group consisting of hydrogen, halogen 2 and a hydrocarbon group. Preferred groups represented by X are oxygen, sulfur, _s〇..., : a divalent hydrocarbon group having up to 1 carbon atom and a group containing oxygen, hydrazine, sulfur or nitrogen. Preferably, the age is 2,2-bis(4-hydroxyphenyl)propane (double hops, each of which is reversed) and X is isopropylidene. VIII 13 200835708 can be used in the practice of the present invention. Preferred dihydric phenols for preparing the resin of the present invention include 4,4,-isopropylidene bisphenol (bisphenol A), 4,4, di-diphenylethyl decane, 3,3'- Dihydroxydiphenyldiethylmethane, 3,4,-dihydroxydiphenyl-mercaptopropylmethane, bisphenol, 4,4'-dihydroxy-diphenyl, 4,4,-dihydroxydiphenyl Cyanomethane, 4,4,-dihydroxybiphenyl, 4,4, dihydroxybenzophenone, 4,4, dihydroxydiphenyl sulfide, 4,4,-dihydroxydiphenyl milling, 2, 6-Dihydroxynaphthalene, 1,4, dihydroxynaphthalene, phenol, resorcinol, o-diphenol, m-xylenol, p-quinol, chlorophenol, nitrophenol, hydroquinone, 2, 2-bis(4-hydroxyphenyl) propyl compound 2,2-bis(4-hydroxyphenyl)pentane, catechol, bisphenol, such as tetrabromobisphenol quinone and in the US patent Other dihydric phenols listed in 3,395,118, 4,43,254 and 4,480,082, which are incorporated herein by reference. a mixture of dihydric phenols. Among these dihydric phenols, bisphenol A, hydroquinone and mixtures thereof are preferred. The amount of phenol used in the present invention is based on the molecular weight of the phenol, the epoxide The molecular weight, the target equivalent of SEER, and the degree of branching. Generally, it is used in an amount of from about 1% by weight to about 6% by weight based on the weight of the reactants, more preferably from about 5% by weight to About 5% by weight, and most preferably from about 20% by weight to about 45% by weight. In general, the reaction of a low molecular weight epoxy resin with a dicarboxylic acid requires a catalyst or any material capable of catalyzing the reaction. In the case of an oxy resin, the dicarboxylic acid and the epoxy resin component are present in a catalyst for the reaction between the carboxylic acid group of the dicarboxylic acid and the epoxy group of the epoxy resin, and are sufficient to form a desired Contact under resin conditions. Catalysts useful in the present invention include, but are not limited to, phosphines, amines, 14 200835708 quaternary ammonium and pin salts, such as tetraethylammonium chloride, tetraethylammonium bromide, iodide Tetraethylammonium, diethylammonium hydroxide, tetrachloride Ammonium, tetra(n-butyl)ammonium bromide (ΊΈΑΒ), molybdenum tetra(n-butyl)ammonium, tetra(n-butyl)ammonium hydroxide, tetrakis(n-octyl)ammonium chloride, brominated tetra N-octyl)ammonium, tetrakis(n-octyl)phosphonium iodide, tetrakis(n-octyl)ammonium hydroxide, methyl chloroformate (n-octyl)ammonium chloride, bis(tetraphenylphosphinoalkyl) chloride Ammonium, ethyl acetate tri-p-tolyl scale/acetate complex, ethyl triphenyl scale/acetate complex, N-methylmorpholine, _ 2_phenylimidazole or combinations thereof and The analogs described in U.S. Patent Nos. 5,208,317, 5,109,099, and U.S. Patent No. 4,981,926, the disclosures of which are incorporated herein by reference. The most preferred catalysts include tetrabutylammonium bromide (TBPB), tetraethylammonium bromide, tetraethylammonium hydroxide, ethyltrimethylamine acetate, ethyltriphenyl scale and N-methyl acetate. Porphyrin, 2-Phenylimidazole (2-Phlm) Ruthenium Although any material capable of catalyzing the reaction can be used, a preferred catalyst is a phosphonium salt catalyst. Preferred phosphonium salt catalysts include scale or money salt catalysts. More preferred ruthenium salt catalysts include tetrabutylammonium bromide, tetrabutyl bromide (TBPB), ethyltriphenyl sulfonate iodide, tetraphenyl bromide and ruthenium bromide (n-butyl) ammonium and Corresponding chloride, iodide, bromide, acetate, formate, phosphate, borate, trifluoroacetate, oxalate and bicarbonate are best optimized for desertification of tetrabutyl scale (TBPB). The amount of catalyst used depends on the molecular weight of the catalyst, the activity of the catalyst, and the rate at which polymerization is desired. The catalyzed J used in the process of the present invention can be varied within a wide range as long as a catalytic amount is present. In general, the amount of the catalyst used in the present invention falls within the range of 50 from 1 scoop of 0·〇〇ι% to about ίο%, preferably from about 0 · 0 01. From about 0% to about 2%, more preferably from about 2% to about 2%, and most preferably from about 0.03% to about 1% by weight of the reactants. The epoxy resin composition of the present invention can be formed by the low molecular weight aromatic non-oxygen and dicarboxylic acid in the presence of a catalyst and in the presence of a solvent to form an uncrosslinked soluble high molecular weight epoxy ester. It is prepared by reacting under the conditions of a resin. _ Rain molecular weight "epoxy" means an epoxy resin product having a number average molecular weight (Μη); 〇'(10)0, preferably less than about 1 〇, 〇〇〇, and more preferably less than about 8,000. Usually, In the present invention, the amount of J-oxyl resin in the polymer has an average number of from about 1,000 to about 20,000, more preferably from about 1, 〇Q 〇 to about 1 〇, (9) 〇, and more preferably. The ground is from about 1,2 Torr to about 8,0. The reaction for preparing the SEER of the present invention can be carried out using a batch-man method or a continuous process carried out in a reaction extruder, as in the European patent Ep. • described in 0193 809. The process of the invention can be carried out in an open vessel or in a pressurer or in an injection molding machine. The conditions most favorable for the polymerization are determined by various factors, including The specific reactants, the solvent used and the catalyst used. Usually, the reaction is carried out in a non-oxidizing atmosphere such as nitrogen or other inert gas s. It is desirable to use an inert organic solvent for the reactants to ensure uniformity. Reaction mixture and adjustment in these Exothermic reaction under the conditions. The reaction conditions used in the method of the present invention may be changed. The time and temperature which are most advantageous for use are based on the specific monomers used, especially the reactivity of the 16 200835708, etc. The polymer and the organic liquid are varied. However, the optimum rate for the reaction to form the polymerization is generally from a reaction temperature in the range of from about 5 to about 3 Torr, from about atmospheric pressure to about 15 psig. The reaction is carried out under the reaction pressure of the range and from about 30 minutes to about 24 hours. The reaction of the bad oxygen resin with the carboxylic acid is advantageously carried out at elevated temperature. The reaction temperature is preferably from about 6 (rc to about 22). 〇t 'better from about i〇(rc

至約150 c,而最佳地從約120°C至約140°C。 反應時間較佳地從約i小時至約24小時,而最佳地從 約2小時至約8小時。 持續反應,i到達成所欲之轉化率為丨,其係藉由以 酸值(AN)滴定所測量之樹脂的酸轉化率而決定的,並在 達成樹脂的目標分子量或歸冑,在此點下有效地終止 反應。 在一個具體實例中,反應通常係藉由在約l〇(rc至約 1 2 0 C之開始溫唐、、日入取t /1 一 下此5 ♦壞乳化物與二綾酸反應物及允 許反應經約1小日聋$ % 1 士 寸至、、、勺2小日守的忪間放熱至約i 6〇。 2 0 0 C之溫度而進行。 ::物:相對量係依據特性而定’特別為所欲之產物 二r: 乂具有環氧化物當量介於、約600至約4,_之 間的車父佳咼分子| p $ 辰乳基為末^0之聚酯樹脂產物士 約0.60至〇 95哲甘 i物而5,將 ”介於約170 : 叛酸與每一莫耳之具有環氧化物 ^。、、” Μ 之間的雙酴·Α之:環氧丙基醚反 17 200835708 本毛明的反應可以-步驟完成,其中將液體芳香族環 氧樹脂(LER)、二羧酸與催化劑反應,並在膠凝之前, 在得以獲得目標環氧反應產物的時點終止反應。 另-選擇地,如果使用視需要之二官能性單體,如二 元紛,則可將液體芳香族環氧樹脂與二元盼先反應及接著 可將二竣酸加入反應混合物中;或可將遍與二叛酸先反 應及接著可將二元紛加入反應混合物中;並在膠凝之前, _ 在反應產物包括目標環氧當量時的時點終止反應。 在聚合物合成期間,聚合物係藉由慣例的方法自反應 混合物回收。例如,可將含有成為沉殿物之聚合物的反應 混合物過渡,以移除固體聚合物。接著可將固體單體以水、 曱醇及驗或對聚合物而言為非溶劑,但是就雜質而言為好 溶劑的其他溶劑沖洗。聚合物也可藉由將反應混合物倒入 聚合物的非溶劑之中,再收集經沉澱之產物來予以分離。 另外,產物聚合物可藉由真空蒸餾、刮膜 _ 壓來移除溶劑而分離。 谭^柑 —可將本發明的環氧酯樹脂以各種環氧固化劑,如酚類, 私’竣酸’紛曱搭樹脂及針’與經由經基或環氧基團固化。 可將本發明的樹脂與硬化劑,例如以胺為末端之聚合物, =羧基為末端之聚合物,以酚為末端之聚合物,能性 胺、羧酸或酚,或可溶酚醛樹脂聚合物反應。 此 ♦用中本!=SEE"用在各種工業應用中或其他環氧應 一、積層板及複合層。工業塗層為塗覆於基板 表面保4塗層(塗料塗層),並典型地被固化或交聯, 18 200835708 以形成以裝飾為目的的連續膜與保護基板。保護塗層一般 包3有機聚合黏結劑、顏料及各種塗料添加劑,其中聚合 站、、、"劑充當顏料的流體媒液及給予流體塗料流變性質。在 一經固化或交聯時,聚合黏結劑會硬化且具有作為顏料之 黏結劑的功能,並提供乾燥之塗料膜至基板的黏著性。顏 料可為有機或無機的,並且在功能上除了耐久性及硬度之 2,避提供不透明性及色彩。保護塗層的製造包含製備聚Up to about 150 c, and most preferably from about 120 ° C to about 140 ° C. The reaction time is preferably from about i hours to about 24 hours, and most preferably from about 2 hours to about 8 hours. Sustained reaction, i to achieve the desired conversion rate, which is determined by the acid conversion of the resin measured by acid number (AN) titration, and at the target molecular weight or blame of the resin, here Stop the reaction effectively at the point. In a specific example, the reaction is usually carried out by reacting at about 1 〇 (rc to about 120 ° C, and taking t / 1 for 5 ♦ bad emulsion with diruthenic acid and allowing The reaction is carried out for about 1 hour 聋 $ % 1 士至至 , , , 2 日 忪 放 放 放 放 放 放 放 放 放 放 放 放 放 放 放 放 放 放 放 放 :: :: :: :: :: :: :: :: :: :: :: :: :: :: :: :: :: :: The product of the special product, r: 乂, having a epoxide equivalent of between about 600 and about 4, _, is a polyester resin product of the end ^0士约0.60至〇95哲甘i物5, will be "between about 170: tick and each ole with epoxide ^.,," 酴 between the two 酴: 环氧The reaction of the present invention can be carried out in a step-by-step process in which a liquid aromatic epoxy resin (LER), a dicarboxylic acid is reacted with a catalyst, and before the gelation, the desired epoxy reaction product is obtained. Termination of the reaction. Alternatively - if a difunctional monomer, such as a binary, is used as desired, the liquid aromatic epoxy resin can be reacted with the binary reaction. Dioxanoic acid may then be added to the reaction mixture; or the reaction may be first reacted with diremediation followed by addition of the binary to the reaction mixture; and prior to gelation, _ when the reaction product includes the target epoxy equivalent The reaction is terminated at a point in time. During polymer synthesis, the polymer is recovered from the reaction mixture by conventional methods. For example, a reaction mixture containing a polymer that becomes a sink can be transitioned to remove the solid polymer. The solid monomer is washed with water, sterol and other solvents which are non-solvent for the polymer, but which are good solvents for impurities. The polymer can also be poured into the non-solvent of the polymer by pouring the reaction mixture into a polymer. In addition, the precipitated product is collected and separated. In addition, the product polymer can be separated by vacuum distillation, wiped film to remove the solvent. Tan citrus - the epoxy ester resin of the present invention can be various rings Oxygen curing agents, such as phenols, private 'tannic acid', and resin and needles are cured with via groups or epoxy groups. The resin of the present invention can be polymerized with a hardener such as an amine. , a carboxyl-terminated polymer, a phenol-terminated polymer, an amine, a carboxylic acid or a phenol, or a resol phenolic polymer. This ♦ uses the medium! = SEE " for various industrial applications. Medium or other epoxy, laminated and composite layers. Industrial coatings are applied to the surface of the substrate to protect the coating (coating) and are typically cured or crosslinked, 18 200835708 to form a decorative The continuous film and the protective substrate. The protective coating generally comprises 3 organic polymeric binders, pigments and various coating additives, wherein the polymerization station, the "agent acts as a fluid vehicle for the pigment and imparts rheological properties to the fluid coating. Once cured Or when cross-linked, the polymeric binder hardens and functions as a binder for the pigment and provides adhesion of the dried coating film to the substrate. The pigment can be organic or inorganic, and in addition to its durability and hardness, it can provide opacity and color. The manufacture of protective coatings includes the preparation of poly

合黏結劑、混合組份材料、研磨在聚合黏結劑中的顏料及 變成商業標準的薄度。 1文用如本文所述 據ASTM 4147-99所述之條件下製備 节^合黏結劑可包括各種廣泛的其他添加劑,例如硬化 :’染料,顏料及流動改質劑,阻燃劑,自動熄滅劑,乾 ^劑及在本文就彼等已知的目的而使用的所有方式的添加 阻燃劑的實例包括:磷酸單銨,填酸二銨及三水合銘。 二等添加劑可具有液體或顆粒形式,只要黏結劑仍為固 可。、具有所欲之顆粒尺寸及不給予黏結劑任何反效果即 可獲得含有本發明的樹0與適合的顏料、催化劑及添 加劑之液體塗層組成物。由苴 古 田八所件之塗層具有令人意外的 =視之性質的良好組合。依據聚合物、交聯劑、催化 ::其:組份的選擇及量而定,可獲得例如具有良好的流 社认 间的先澤度,高的耐刮傷性,良 好的機械性質,良好的 、 t久性及良好的色彩穩定性的 19 200835708 組成物。 含有本發明的樹脂之水分散性塗覆組成物為罐頭及鋼 捲塗覆組成物所高度希望的。 為了提供更多對本發明的瞭解,包括其代表性的優點, 故提出下列的實施例。 在下列的實施例中所使用的各種用於原料的術語,縮 寫及命名被解釋如下: "EEW"代表環氧當量。 ⑩ 、、AN,,代表酸值。 D.E.R.™3 31 ( EEW= 188) > D.E.R. 3 83 ( EEW= 180)Adhesives, mixed component materials, pigments ground in polymeric binders and become thinner than commercial standards. Preparation of a bonding agent as described herein according to ASTM 4147-99 may include a wide variety of other additives, such as hardening: 'dye, pigment and flow modifier, flame retardant, auto-extinguish Examples of agents, dry agents, and all types of added flame retardants used herein for their known purposes include: monoammonium phosphate, diammonium phosphate, and trihydrate. The second additive may be in liquid or particulate form as long as the binder is still solid. A liquid coating composition comprising the tree 0 of the present invention and a suitable pigment, catalyst and additive can be obtained with any desired particle size and without any adverse effect of the binder. The coatings from the eight pieces of Gutian have a surprisingly good combination of properties. Depending on the choice of the polymer, the crosslinking agent, and the catalysis: the composition and the amount of the component, it is possible to obtain, for example, a good visibility of the fluid, high scratch resistance, good mechanical properties, and good 19 200835708 Composition of t, t long and good color stability. The water-dispersible coating composition containing the resin of the present invention is highly desirable for can coatings and coil coating compositions. In order to provide a further understanding of the present invention, including its representative advantages, the following embodiments are presented. The various terms, abbreviations and nomenclature used in the materials used in the following examples are explained as follows: "EEW" represents epoxy equivalent. 10, AN, and represent the acid value. D.E.R.TM3 31 ( EEW= 188) > D.E.R. 3 83 ( EEW= 180)

及 D.E.R. 354LV ( EEW=170 )為液體芳香族環氧樹脂 (LER) 。D.E.R. 661 ( EEW= 534 ) 、D.E.R. 667 ( EEW = 1 850 )及 D.E.R· 669E(EEW= 3290 )為固體環氧樹脂 (SER)。該等產品為取自 The Dow Chemical Company 之 市售品。 、、A1"為取自 Morton Chemical Company 之催化劑(在 曱醇中的70重量%之n-Bu4POAc / HOAc )。 TBAB、TBPB、2-Phlm、TPA、AA、PA、1,4-CHDA、 1,3-CHDA、二甘醇二甲醚、環己酮、Dowanol™PMA( PMA)、 Dowanol PM ( PM)及二(丙二醇)甲醚乙酸酯(DPMA)為 取自Aldrich之市售化學品。 異苯二甲酸(IPA )為取自 Aldrich 或 MB Biomecidals, Inc,之市售酸。And D.E.R. 354LV (EEW=170) is a liquid aromatic epoxy resin (LER). D.E.R. 661 (EEW=534), D.E.R. 667 (EEW = 1 850) and D.E.R. 669E (EEW=3290) are solid epoxy resins (SER). These products are commercially available from The Dow Chemical Company. , A1 " is a catalyst from Morton Chemical Company (70% by weight of n-Bu4POAc / HOAc in decyl alcohol). TBAB, TBPB, 2-Phlm, TPA, AA, PA, 1,4-CHDA, 1,3-CHDA, diglyme, cyclohexanone, DowanolTM PMA (PMA), Dowanol PM (PM) and Di(propylene glycol) methyl ether acetate (DPMA) is a commercially available chemical from Aldrich. The isophthalic acid (IPA) is a commercially available acid from Aldrich or MB Biomecidals, Inc.

Methylon 75 108 為市售取自 Occidental Chemical Co· 20 200835708 之羥甲基苯基烯丙醚。 超磷酸(105% )、甲基乙酮(ΜΕκ)、乳酸及2_丁 氧基乙醇(DowanolTMEB)為取自 Aldrich Chemical c〇 之 市售化學品。 、HPLC〃代表高壓液相層析法。 HPLC等級水、乙腈(ACN )及四氫呋喃(THF )為取 自EMD之市售化學品。 BYK-310石夕氧界面活性劑為取自Byk Chemie之市隹 品 ° 在實施例中用於測量某些性質的各種標準試驗方法及 步驟如下: 環氧化物當量(EEW )滴定係根據相當於ASTM D-1652-97之步驟得以完成。 酸值(AN)分析係根據相當於ASTM D 1639-83之步 驟得以完成。 環族二聚物分析係藉由使用水/ ACN梯度溶析程序以Methylon 75 108 is a methylol phenyl allyl ether commercially available from Occidental Chemical Co. 20 200835708. Superphosphoric acid (105%), methyl ethyl ketone (ΜΕκ), lactic acid, and 2-butoxyethanol (DowanolTM EB) are commercially available chemicals from Aldrich Chemical c〇. HPLC 〃 represents high pressure liquid chromatography. HPLC grade water, acetonitrile (ACN) and tetrahydrofuran (THF) are commercially available chemicals from EMD. BYK-310 Shiyang Oxygen Surfactant is a product from Byk Chemie. Various standard test methods and procedures for measuring certain properties in the examples are as follows: Epoxide equivalent (EEW) titration is based on equivalent The steps of ASTM D-1652-97 are completed. The acid number (AN) analysis was carried out according to the procedure equivalent to ASTM D 1639-83. Cyclic dimer analysis is performed by using a water/ACN gradient elution procedure

Agilent 1100 LC系統的HPLC得以完成。 數里平均为子里(Μη)分析係使用viscotek GPC分 析系統得以完成。 下列的實施例係以說明為目的而已,並不意欲限制本 發明的範圍。除非有其他另外的指示,所有份量及百分比 係以重量計。 1 —榭脂產物的 溶液樹脂進階反應係使用下列的步驟得以完成:7-類 21 200835708 型之D.E.R. 661 — AA SEER的製備被敘述如下。將100公 克(g) D.E.R. 661 SER (事先在1〇〇卞下經18小時真空乾 丈本)、9.22公克AA及11〇公克二甘醇二甲鱗加入配備機 械擾拌器、冷凝器、加熱套及與可程式控制器連接之熱電 偶的1公升(L )樹脂壺中。將反應器充填n2,同時使用 溫和混合方式加熱至110它,在此時加入在1〇 1#(mL) 二甘醇二甲醚中的〇·77公克TBAB。(在約60°C下觀察全HPLC of the Agilent 1100 LC system was completed. The average number of tens of analyses was done using the viscotek GPC analysis system. The following examples are for illustrative purposes and are not intended to limit the scope of the invention. All parts and percentages are by weight unless otherwise indicated. 1 — The solution resin of the rouge product advanced reaction was carried out using the following procedure: 7-class 21 D.E.R. 661 of Model 200835708 - The preparation of AA SEER is described below. Add 100 grams (g) DER 661 SER (previously dried under 18 hours for 18 hours), 9.22 grams of AA and 11 gram grams of diethylene glycol dimethyl scales with mechanical stirrer, condenser, heating A 1 liter (L) resin kettle with a thermocouple connected to a programmable controller. The reactor was filled with n2 while heating to 110 with gentle mixing, at which time 〇77 g of TBAB in 1 〇 1 # (mL) diglyme was added. (view all at about 60 ° C)

部的固體溶解)將反應混合物在約112它下維持32〇分鐘 的時間’在此期間,偶而取出樣品用於EEw滴定。 將該實施例1的結果顯示在下列表1中。 施例2 —樹脂產物的_備 實施例2係如以上實施例丨中所述而進 ⑽公克己二酸(AA)之外。 除了使用The solids of the fractions were dissolved. The reaction mixture was maintained at about 112 for a period of 32 Torr. During this time, samples were occasionally taken for EEw titration. The results of this Example 1 are shown in Table 1 below. Example 2 - Preparation of Resin Product Example 2 was carried out in addition to (10) grams of adipic acid (AA) as described in the above Examples. In addition to use

班較性實施例A 比較性實施例A係如以上實施例!中所述般、在反應 溫度下使用26.7公克雙酚A、32 7公克已二酸、〇 : 克D.E.R. 331環氧樹脂及〇16公克A·〗催化劑、但沒有使 用溶劑之下進行,如表1中所示者。 —义Comparative Example A Comparative Example A is as in the above example! As described above, 26.7 grams of bisphenol A, 32 7 grams of adipic acid, hydrazine: gram DER 331 epoxy resin and 公16 grams of A· catalyst were used at the reaction temperature, but without using a solvent, as shown in the table. The one shown in 1. - meaning

_比較性實施例B 比較性貫施例B係如以上實 1见般、在反 _·— -V w 丨/ J , / 温度下使用24.3公克雙酚A、29.8公克己二醆、15〇 〇 克D.E.R. 331環氧樹脂及〇15公克A]催化_Comparative Example B Comparative Example B is as in the above, using 24.3 grams of bisphenol A, 29.8 grams of hexamethylene, 15 在 at the inverse _·- -V w 丨 / J , / temperature 〇 DER 331 epoxy resin and 〇 15 g A] catalysis

田、〜兔丨> T…’但沒有> 用浴劑之下進仃,如表1中所示者。 达較性實施例C 22 200835708 比較性實施例c係如以上實施例丨中所述般、在反應 溫度下使用33.3公克己二酸、150.0公克D.E.R· 331環氧 樹脂及0 · 1 4公克A-1催化劑、但沒有使用溶劑之下進行, 如表1中所示者。Field, ~ rabbit 丨 > T...' but not > Under the bath, as shown in Table 1. Comparative Example C 22 200835708 Comparative Example c used 33.3 grams of adipic acid, 150.0 grams of DER·331 epoxy resin and 0·14 g of A at the reaction temperature as described in the above Examples. -1 Catalyst, but not using a solvent, as shown in Table 1.

比較性實施你丨D 比較性實施例D,部分1係如以上實施例1中所述般、 在反應溫度下使用33·3公克己二酸、150.0公克D.E.R. 331 環氧樹脂及0 · 1 4公克A-1催化劑、但沒有使用溶劑之下進 行,如表1中所示者。比較性實施例D的部分2係在反應 溫度下使用得自部分1的產物及26.1公克雙酚a與〇 16 公克A-1催化劑來完成,如表1中所示。 表I.液體環氧樹脂(LER)或固體環氧樹脂(SER)與aa 的反應 實施例 反應物 催化劑 條件 目標 實際 之EEW 實施例1 D.E.R. 661 + AA TBAB 110〇C, 50 % 在二 甘醇二甲 醚中 1800 1592 實施例2 D.E.R. 661 + AA TBAB 110〇C, 50 % 在二 甘醇二甲 醚中 3200 3115 I比較性實 LER + A-1 130-180〇C _1800 —凝膠 23 200835708Comparative Example 比较D Comparative Example D, Part 1 is as described in Example 1 above, using 33. 3 grams of adipic acid, 150.0 grams of DER 331 epoxy resin and 0 · 1 4 at the reaction temperature. The gram of the A-1 catalyst was carried out without using a solvent as shown in Table 1. Part 2 of Comparative Example D was carried out using the product from Part 1 and 26.1 g of bisphenol a and 〇 16 g of A-1 catalyst at the reaction temperature, as shown in Table 1. Table I. Reaction of liquid epoxy resin (LER) or solid epoxy resin (SER) with aa Example reactants Catalyst conditions Target actual EEW Example 1 DER 661 + AA TBAB 110〇C, 50 % in diethylene glycol Dimethyl ether in 1800 1592 Example 2 DER 661 + AA TBAB 110〇C, 50 % in diethylene glycol dimethyl ether 3200 3115 I comparative real LER + A-1 130-180〇C _1800 — gel 23 200835708

施例A BA+ AA --—_____ 比較性實 LER + A-1 130-180〇C —------ 1150 -—-—— 凝膠 施例B BA+ AA --_____ 比較性實 LER + A-1 160°C ---——__ 530 ----— 凝膠 施例C AA 比較性實 LER + A-ι 130°C ——~·-—_ 530 ---— 533 施例D- AA 部分1 ------— 比較性實 比較性實 " 1 ---—一 A-1 160°C ——~~~·-—-_ 1800 -----—〜 凝膠 施例D- 施例D- 部分2 部分1 + 者丈& /nl -> BA 3ΐΑί列3-20 —谢脂產物 使用兩種方法製備SEER樹脂。在兩種方法中,在反 ㈣始時產生不均句的“,當所使用的二顧(DCA) ^經加熱完全轉時,_成澄清溶液。將髮定期取樣, =追縱EEW A AN的變化。當進階反應結束時,允許咖汉 液~。卩至低於90 C及接著快速轉移至玻璃罐中。 LER、DCA、溶劑及催化㈣ 载至配備回流冷凝H、N2人口、與空氣驅動馬達連接之擾 ,棒及與溫度控制器連接之熱電偶及加熱套的刚毫升玻 离树月曰亞中。將反應混合物以小A i小時加熱至指定的溫 度及接著維持恒溫’直到達到目帛EER為止。在該方法A 中,反應所花的時間為在所欲之溶液溫度起的時間與達到 24 200835708 所欲之EEW之後的時間之間的持續期間。 方法I-的通用逢^LER、DCA及部分溶劑(約9〇 重量% )加入配備如上述方法A的5〇〇毫升玻璃樹脂罐中。 將反應混合物以小於1小時加熱至指定的溫度。接著加入 催化劑及剩餘的溶劑(約10重量%)或溶解在剩餘溶劑 (〜10重量% )中的催化劑。將溶液維持在指定的溫度下, 直到達到目標EER為止。反應時間係從催化劑加入的時間 至達到目標EEW的時間。Example A BA+ AA --______ Comparative Real LER + A-1 130-180〇C —------ 1150 ——————— Gel Example B BA+ AA --_____ Comparative Real LER + A-1 160°C ---——__ 530 ----- Gel Example C AA Comparative Real LER + A-ι 130°C ——~·-__ 530 --- 533 Example D-AA Part 1 -------Comparative Real Comparison " 1 ----A-1 160 °C ——~~~·---_ 1800 -----~ Gel Example D - Example D - Part 2 Part 1 + zhang & /nl -> BA 3 ΐΑ ί 3-20 - The chelating product The SEER resin was prepared using two methods. In both methods, the "uneven sentence" is generated at the beginning of the inverse (four), when the used double-handed (DCA) ^ is heated completely, _ becomes a clear solution. Regular sampling will be performed, = EEW A AN Changes. When the advanced reaction is over, allow the yam liquid ~. 卩 to below 90 C and then quickly transfer to the glass jar. LER, DCA, solvent and catalysis (4) to the population with reflux condensation H, N2, and The air-driven motor connection is disturbed, the rod and the thermocouple and the heating sleeve connected to the temperature controller are in the milliliter glass. The reaction mixture is heated to a specified temperature in a small A i hour and then maintained at a constant temperature until The target EER is reached. In the method A, the reaction takes a period of time between the time of the desired solution temperature and the time after the desired EEW of 24 200835708 is reached. ^LER, DCA and part of the solvent (about 9% by weight) were added to a 5 cc glass resin jar equipped with Method A as above. The reaction mixture was heated to the specified temperature in less than 1 hour. Then the catalyst and the remaining solvent were added. (about 10 weights ) Or dissolved in the remaining solvent (~ 10 wt%) catalyst. The solution is maintained at a specified temperature, the EER until it reaches the target. The reaction time-based catalyst is added from time to time to reach the target EEW.

將用於製備樹脂的反應條件顯示在表II中,並將樹月旨 產物的分析結果顯示在表III中。 表II.用於製備榭脂的反應條件 實 LER DCA 溶劑 催>1 匕劑C 溫 施 D.E. (公克) 酸 (公克) 催化劑 (公克) 度 例a R.d (°C ) 3 383 200.03 IPA 79.30 二甘醇 TBPB 1.9700 110 二曱醚 4 354LV 200.00 IPA 84.70 二甘醇 TBPB 2.0100 110 二曱醚 5 354LV 200.08 IPA 90.40 二甘醇 TBPB 2.0500 110 二曱鱗 6 383 199.97 IPA 84.90 PMA TBPB 2.0108 1 1 Π 7 383 200.00 IPA 84.88 PMA TBPB 2.0100 i 1 U 140 8 383 25.07 IPA 10.61 二甘醇 TBPB 0.2493 160 —甲鱗 25 200835708The reaction conditions for preparing the resin are shown in Table II, and the results of the analysis of the product of Shushu are shown in Table III. Table II. Reaction conditions for preparing rouge LER DCA Solvents >1 Tanning agent C Warming DE (g) Acid (g) Catalyst (g) Example a Rd (°C) 3 383 200.03 IPA 79.30 II Glycol TBPB 1.9700 110 Diterpene ether 4 354LV 200.00 IPA 84.70 Diethylene glycol TBPB 2.0100 110 Diethylene ether 5 354LV 200.08 IPA 90.40 Diethylene glycol TBPB 2.0500 110 Diterpenoid scale 6 383 199.97 IPA 84.90 PMA TBPB 2.0108 1 1 Π 7 383 200.00 IPA 84.88 PMA TBPB 2.0100 i 1 U 140 8 383 25.07 IPA 10.61 Diethylene glycol TBPB 0.2493 160 — A scale 25 200835708

9 —---- 383 200.06 ΤΡΑ 84.91 PMA TBPB 2.0100 140 10 383 200.01 PA 84.91 PMA TBPB 2.0111 140 11 Ι_183 24.96 IPA 10.58 PMA TBPB 0.1252 140 12 60.05 IPA 25.51 PMA TBPB 0.1492 140 13 __183 179.98 IPA 76.39 環己酮 TBPB 1.8074 140 14 383 64.98 IPA 27.59 DPMA TBPB 0.0640 180 15b 383 121.87 1,4- 53.50 PMA TBPB 1.2353 140 CHD ---- A 使用方法A及50重量%之溶劑,除非有其他另外的註明。9 —---- 383 200.06 ΤΡΑ 84.91 PMA TBPB 2.0100 140 10 383 200.01 PA 84.91 PMA TBPB 2.0111 140 11 Ι_183 24.96 IPA 10.58 PMA TBPB 0.1252 140 12 60.05 IPA 25.51 PMA TBPB 0.1492 140 13 __183 179.98 IPA 76.39 Cyclohexanone TBPB 1.8074 140 14 383 64.98 IPA 27.59 DPMA TBPB 0.0640 180 15b 383 121.87 1,4- 53.50 PMA TBPB 1.2353 140 CHD ---- A Use Method A and 50% by weight of solvent unless otherwise stated.

/合劑· 1 8重量%。e催化劑之重量%係以lER、DCa及催 化劑之量為基準。溶液之重量%係以整個反應系統,即 LER、DCA、催化劑及溶劑之量為基準。dD E R•環氧樹脂 類型。 表Π (續)·用於製備樹脂的反應條件 實 施 例3 I ,ER DCA 溶劑 催d 七劑c 溫 度 (°C ) D.E. R.d (公克) 酸 (公克) 催化劑 (公克) 16 383 200.02 IPA 84.89 PMA TBPB 2.0123 140 17 331 199.97 IPA 81.19 環己酮 TBPB 1.9805 140 18 383 200.00 IPA 79.40 環己酮 2-Phlm 0.1975 140 19 383 200.02 TPA 42.45 PMA TBPB 2.0100 140 20 383 180.01 IPA 76.40 環己酮 TBPB 1.8080 140 a使用方法A及50重量%之溶劑,除非有其他另外的註明。 b溶劑·· 1 8重量%。e催化劑之重量%係以LER、DCA及催 26 200835708 化劑之量為基準。溶液之重量%係以整個反應系、统,# LER、DCA、催化劑及溶劑之量為基準。dDER•環氧汽月匕 類型。 表 IIL SEER 之 EEW、AN 及 Μη 實施 時間 LER 酸 ------ EEW ~ AN -----Ί Λ/Γ ^ 例a (分鐘) 實際 Μη 3 365 383 IPA 1,800 1,736 —~~~— 0.2 0 Q AC\ 4 500 354LV IPA 1,800 1,754 0.2 ^ 5 〇 U 3 6 1 S 5 470 354LV IPA 3,200 2,869 0.2 7 1 RA 6 515 383 IPA 3,2〇〇 3,265 0.1 / 5丄o外 4 fi〇〇 7 85 383 IPA 3,200 3,612 0.1 6 671 8 30 383 IPA 3,20〇 3,354 0.1 ^ \j / x ^ 1 1 Q 9 160 383 TPA 3,200 3,440 <0.1 J 5丄丄7 4 440 10 67 383 PA 3,20〇 3,607 0.5 7,25 1 11 149 383 IPA 3,200 3,156 1.6 5,191 12 285 383 IPA 3,200 3,234 1.2 6,194 13 45 383 IPA 3,200 3,628 0.1 14 83 383 IPA 3,20〇 4,110 0.1 1,778 15 78 383 1,4- CHDA 3,200 3,167 0.6 3,732 16 45 383 IPA 3,200 3,570 1 EEW及AN係在整體樹脂溶液冷卻至周圍溫度之後而測 里’除非有其他另外的註明。b將少量樣品(經常< 2 0公 克)自整體溶液取出及用於EEW與AN分析。 27 200835708 表 111 f 續)· SEER 之 EEW、AN 及 Μη/ mixture · 1 8 wt%. The weight % of the e catalyst is based on the amount of lER, DCa and the catalyst. The weight % of the solution is based on the total amount of the reaction system, i.e., LER, DCA, catalyst, and solvent. dD E R• Epoxy resin type. Table Π (continued) · Reaction conditions for preparing the resin Example 3 I, ER DCA Solvent d 7. Seven doses c Temperature (°C) DERd (g) Acid (g) Catalyst (g) 16 383 200.02 IPA 84.89 PMA TBPB 2.0123 140 17 331 199.97 IPA 81.19 Cyclohexanone TBPB 1.9805 140 18 383 200.00 IPA 79.40 Cyclohexanone 2-Phlm 0.1975 140 19 383 200.02 TPA 42.45 PMA TBPB 2.0100 140 20 383 180.01 IPA 76.40 Cyclohexanone TBPB 1.8080 140 a Use Method A And 50% by weight of solvent unless otherwise stated. b Solvent · · 18% by weight. The weight % of the e catalyst is based on the amount of LER, DCA, and chemistry. The weight % of the solution is based on the total amount of the reaction system, system, LER, DCA, catalyst and solvent. dDER• Epoxy steam moon type. Table IIL SEER EEW, AN and Μ Implementation time LER acid ------ EEW ~ AN -----Ί Λ / Γ ^ Example a (minutes) Actual Μ 3 365 383 IPA 1,800 1,736 —~~ ~— 0.2 0 Q AC\ 4 500 354LV IPA 1,800 1,754 0.2 ^ 5 〇U 3 6 1 S 5 470 354LV IPA 3,200 2,869 0.2 7 1 RA 6 515 383 IPA 3,2〇〇3,265 0.1 / 5丄o 4 fi〇〇7 85 383 IPA 3,200 3,612 0.1 6 671 8 30 383 IPA 3,20〇3,354 0.1 ^ \j / x ^ 1 1 Q 9 160 383 TPA 3,200 3,440 <0.1 J 5丄丄7 4 440 10 67 383 PA 3,20〇3,607 0.5 7,25 1 11 149 383 IPA 3,200 3,156 1.6 5,191 12 285 383 IPA 3,200 3,234 1.2 6,194 13 45 383 IPA 3,200 3,628 0.1 14 83 383 IPA 3,20〇4,110 0.1 1 , 778 15 78 383 1,4- CHDA 3,200 3,167 0.6 3,732 16 45 383 IPA 3,200 3,570 1 EEW and AN are measured after the entire resin solution has cooled to ambient temperature' unless otherwise stated. b A small amount of sample (often < 20 grams) was taken from the bulk solution and used for EEW and AN analysis. 27 200835708 Table 111 f continued) · SEER EEW, AN and Μη

aEEW及ΑΝ係在整體樹脂溶液冷卻至周圍溫度之後而測 量,除非有其他另外的註明。b將少量樣品(經常< 2〇公 克)自整體溶液取出及用於EEW與AN分析。 在表I-III中的結果顯示獲得具有所欲性質的未經交聯 之可溶性高分子量環氧酯樹脂。 較性實施例£二_^^鋼板的 將取自 Weirton steel Corporation 之市售 L 型,T4CA, 表面5〇的無錫鋼(TFS—以單一還原之電解質鉻塗佈之薄 板)用作在該實施例中的金屬基板。 根據在ASTM 4147_99中所述之步驟將塗層調配物取 出至TFS板上及固化,得到〇2〇+/_〇〇2密耳之塗層厚 度。將塗佈之板根據ASTM D 54()2_93進行mek阻抗性測 試、在塗佈不良之前的最多雙磨損(DR)數量測試及根據 ASTM D 328i -84進行楔形f曲撓性測試。乳酸巴斯德殺菌 (pasteurization)抗性係使用浸入含有2重量%之乳酸的 小瓶中及在12(TC之加壓爸中加熱3G分鐘的楔形彎曲板樣 品(〜m。之塗層彎曲的張力)得以完成。使用在下列表 28 200835708 0 A中所述之分級系統敘述塗層性能。 表A.乳酸巴斯德殺菌抗性試驗的分級系統 分級觀察The aEEW and tether are measured after the overall resin solution has cooled to ambient temperature unless otherwise noted. b A small amount of sample (often < 2 gram) was taken from the bulk solution and used for EEW and AN analysis. The results in Tables I-III show that an uncrosslinked soluble high molecular weight epoxy ester resin having the desired properties is obtained. A comparative example of a steel sheet of commercially available L-type, T4CA, surface 5 无 of tin-free steel (TFS - a sheet of single-reduced electrolyte chromium coated) is used in this embodiment. The metal substrate in the example. The coating formulation was taken to the TFS panel and cured according to the procedure described in ASTM 4147_99 to give a coating thickness of 〇2〇+/_〇〇2 mil. The coated panels were subjected to a mek resistance test according to ASTM D 54() 2_93, a maximum double wear (DR) quantity test before coating failure, and a wedge-shaped f flexibility test according to ASTM D 328i-84. The pasteurization resistance of the lactic acid is immersed in a vial containing 2% by weight of lactic acid and a wedge-shaped curved plate sample heated at 3G for 12 minutes in TC (Dm. The completion of the coating is described using the grading system described in the following list 28 200835708 0 A. Table A. Grading of the grading system of the pasteurization resistance test

在彎曲或平坦區段上沒有任何紅染或氣泡 在平坦區段上沒有任何紅染或氣泡 在平坦區段上有紅染,但是沒有氣泡 在平坦區段上有一些小氣泡的紅染 在平坦區段上有許多大氣泡的紅染 全部的塗層破壞 所有的试驗係重複執行,並在此係以結果的平均值報 告。 測量在實施例3-20中所製備的一些塗層的性質,並將 5亥專貫施例的結果顯示在下列表iv中。There are no red stains or bubbles on the curved or flat section. There is no red stain on the flat section or the bubbles are red-stained on the flat section, but there are no bubbles on the flat section. There are some small bubbles on the flat. The red dyed coating on the section with many large bubbles destroys all test lines and is repeated here and is reported as the average of the results. The properties of some of the coatings prepared in Examples 3-20 were measured and the results of the 5 Hai specific examples are shown in the following table iv.

29 200835708 表IV.以可溶酚醛樹脂硬化劑及H3P04催化劑在205 °c下 經1 0分鐘固化之樹脂塗層的性質 實施例 樹脂 硬化劑 (重量 % ) H3P〇4 (重量 %) 添加 劑a (重 量% ) MEK DR (最 多合格 數) 楔形 •彎曲 (不 良% ) LAP 試驗 比較性 實施例 E D.E.R. 669E 15 0.75 — 125 25 3 21 9T / 3 83 / IPA (實施例6) 15 0.75 --- 175 3 0 0 22 9T / 3 83 / IPA (實施例6) 25 0.75 — 200 41 4 23 9T / 3 83 / IPA (實施例6) 15 1.50 —— 125 33 4 24 7T / 383 / IPA (實施例3) 15 1.50 0.1 150 33 2 25 9T / 3 83 / TPA (實施例9) 15 0.75 0.1 150 3 0 2 30 20083570829 200835708 Table IV. Properties of resin coatings cured with phenolic resin hardener and H3P04 catalyst at 205 °c for 10 minutes Examples Resin hardener (% by weight) H3P〇4 (% by weight) Additive a ( Weight %) MEK DR (maximum number of passes) Wedge shape • Bending (% of bad) LAP test Comparative Example E DER 669E 15 0.75 — 125 25 3 21 9T / 3 83 / IPA (Example 6) 15 0.75 --- 175 3 0 0 22 9T / 3 83 / IPA (Embodiment 6) 25 0.75 — 200 41 4 23 9T / 3 83 / IPA (Embodiment 6) 15 1.50 —— 125 33 4 24 7T / 383 / IPA (Example 3 ) 15 1.50 0.1 150 33 2 25 9T / 3 83 / TPA (Example 9) 15 0.75 0.1 150 3 0 2 30 200835708

表IV·以可溶紛酸樹脂硬化劑及H3P〇4催化劑在2〇5。〇下 經10分鐘固化之樹脂塗層的性質 實施例Table IV. is a soluble acid resin hardener and a H3P〇4 catalyst at 2〇5. Properties of the resin coating cured under the arm for 10 minutes

aByk-31〇矽氧界面活性劑 在表IV中的該等結果顯示具有所欲 本發明的未經交聯之可溶性高 貝之塗層可自 雖然本發明已藉由參考特殊的呈 月曰獲件。 明,但是那些在所屬技術領域中具有、二敘述及說 發明本身可引導出不必 k * 0硪者將領會本The results of the aByk-31 antimony surfactant in Table IV show that the uncrosslinked soluble high shell coating of the present invention can be obtained from the present invention by reference to a particular Pieces. Ming, but those who have in the technical field, the second narrative and the invention itself can lead to the need to k * 0 硪 will understand this

^ ^ ^ t 仕本文中說明的變务麟 ^ ,考與決定本發明的真正範圍 化體。據此, 專利範圍。 的有關之所附之申請 【圖式簡單說明】 盖 【主要元件符號說明】 31^ ^ ^ t The syllabus explained in this article, test and determine the true scope of the invention. Accordingly, the scope of the patent. The attached application (simplified description of the drawing) cover [main symbol description] 31

Claims (1)

200835708 十、申請專利範圍: 物,=没有凝膠的含芳香族基團之環氧醋樹脂組成 且右二I3具有末端環氧基團、具有環氧官能度大於卜 :!=:於1及具有環氧當量(eew)為約繼或更大 、-又%之可溶性高分子量環氧醋樹脂;該未經交聯之 7性高分子量環氧@旨樹脂是直接衍生自⑷低分子量芳香 方矢%氧樹脂與(b)二羧酸之反應。200835708 X. Patent application scope: Material, = gel-free aromatic group-containing epoxy vinegar resin composition and right second I3 has terminal epoxy group, with epoxy functionality greater than Bu: !=: at 1 and A soluble high molecular weight epoxy vinegar resin having an epoxy equivalent (eew) of about or more, and a % by weight; the uncrosslinked 7-merity high molecular weight epoxy resin is directly derived from (4) a low molecular weight aromatic side The reaction of a bis-oxygen resin with (b) a dicarboxylic acid. 、2_:根㈣請專利範圍第1項之環氧S旨樹脂,其中該低 为子量芳香族環氧樹脂包含二切之二環氧丙基鍵。 3·根據中請專利範圍第2項之環氧S旨樹脂,其中該二 讀包含4,4,_異亞丙基雙盼,4,4,_二錄二苯基乙基甲 t,3’3 -一經基二苯基二乙基甲烷,3,4、二羥基二苯基-甲 基丙基甲烧’雙紛,4,4’·二經基_二苯鱗,4,4,-二經基二苯 基亂基甲烷,4,4,·二羥基聯苯’ 4,4、二羥基二苯甲酮,4,4,_ -經基二苯硫鍵’ 4,4,_二經基二苯石風,2,6_二經基葶,M,· 二經基萘’兒茶酚’間苯二酴’氫螺或四溴基雙盼A。 4·根據申請專利範圍第2項之環氧醋樹脂,其中該二 %乳丙基醚包含雙紛·Α之二環氣丙基醚,氫酿之二環氧丙 基鱗或間苯二酚之二環氧丙基醚。 32 1 ·根據中請㈣範圍第1項之環U旨樹脂,其中該二 竣酸包含己二酸,異苯二甲酸’對笨二甲酸或其混合物。 6.一種黏結劑組成物,其包含如申請專利範圍第ι項 之環氧酯樹脂。 7·-種黏結劑組成物’其包含如申請專利範圍第ι項 200835708 之環氧酯樹脂及硬化劑。 8_根據申請專利範圍第7項之黏結劑組成物,其中該 硬化劑包含以胺為末端之募聚物或聚合物,以羧基為末端 之寡聚物或聚合物,以酚為末端之寡聚物或聚合物,可溶 酚醛樹脂(phenolic resole )募聚物或聚合物,多官能性胺、 羧酸或酚。 9.根據申請專利範圍第8項之黏結劑組成物,其進一 步包含顏料,填充劑,流動改質劑,界面活性劑,潤滑劑 或溶劑。 10·-種液體塗料’其包含如申請專利範圍第7項之黏 結劑組成物。 1 1 ·種複a材料’其包含如申請專利範圍帛7項之黏 結劑組成物及基板。 12 ·根據申清專利餘| , s 、— 引乾圍弟11項之稷合材料,其中該基 板為金屬類。2_: Root (4) The epoxy S resin of the first aspect of the patent range, wherein the low-quantity aromatic epoxy resin comprises a di-cut diepoxypropyl bond. 3. The epoxy S resin according to item 2 of the scope of the patent application, wherein the second reading comprises 4,4,_isopropylidene double, 4,4,_di-diphenylethyl-t,3 '3 - mono-diphenyldiethylmethane, 3,4, dihydroxydiphenyl-methylpropyl-methyl-salt, 4,4'-di-diyl-diphenyl scale, 4,4, -di-diphenyldiphenyl-based methane, 4,4,-dihydroxybiphenyl '4,4, dihydroxybenzophenone, 4,4,_-pyridyl diphenyl sulfide bond 4,4,_ Di-based diphenyl stone, 2,6-di-pyridyl, M, · di-naphthalene 'catechol' meta-benzoquinone hydrogen snail or tetrabromo bis-A. 4. The epoxy vinegar resin according to item 2 of the patent application scope, wherein the bis-lactic propyl ether comprises a bicyclo propylene propyl ether of hydrogen bismuth, a diethylene oxide propyl squam or a resorcinol Di-epoxypropyl ether. 32 1 · Resin according to the first item of the fourth paragraph of the fourth paragraph, wherein the diterpene acid comprises adipic acid, isophthalic acid, p-dicarboxylic acid or a mixture thereof. A binder composition comprising an epoxy ester resin as claimed in the first item of the patent application. A binder composition comprising an epoxy ester resin and a hardener as described in the patent application No. 200835708. 8_ The binder composition according to claim 7, wherein the hardener comprises an amine-terminated polymer or a polymer, a carboxyl-terminated oligomer or polymer, and a phenol-terminated oligomer Polymer or polymer, phenolic resole polymer or polymer, polyfunctional amine, carboxylic acid or phenol. 9. The binder composition according to item 8 of the patent application, which further comprises a pigment, a filler, a flow modifier, a surfactant, a lubricant or a solvent. 10. A liquid coating material comprising a binder composition as in claim 7 of the patent application. 1 1 · A complex material a' which comprises a binder composition and a substrate as claimed in claim 7 of the patent application. 12 · According to the application of the patent, | s, - 引 围 围 围 11 11 11 11 11 11 11 11 11 围 围 围 围 围 围 围 11 11 11 11 11 11 11 無 圈式: 33Acyclic: 33
TW96134399A 2006-10-10 2007-09-14 Soluble polymers with high conversion of acid from aromatic epoxy resins and diacids and crosslinked coatings prepared therefrom TW200835708A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US85047506P 2006-10-10 2006-10-10

Publications (1)

Publication Number Publication Date
TW200835708A true TW200835708A (en) 2008-09-01

Family

ID=39046768

Family Applications (1)

Application Number Title Priority Date Filing Date
TW96134399A TW200835708A (en) 2006-10-10 2007-09-14 Soluble polymers with high conversion of acid from aromatic epoxy resins and diacids and crosslinked coatings prepared therefrom

Country Status (2)

Country Link
TW (1) TW200835708A (en)
WO (1) WO2008045882A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI779050B (en) * 2018-06-15 2022-10-01 達興材料股份有限公司 Resin composition and lamination method for semiconductor substrates by using the same

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8975343B2 (en) 2009-12-08 2015-03-10 Dow Global Technologies Llc Hydroxyl-functional polyester resins
CN103140531B (en) 2010-09-30 2016-05-04 蓝立方知识产权有限责任公司 Prepare the method for epoxy resin
US9371414B2 (en) 2010-09-30 2016-06-21 Blue Cube Ip Llc Epoxy resin adducts and thermosets thereof
CN103228694B (en) 2010-09-30 2016-04-27 蓝立方知识产权有限责任公司 Heat curable composition and the thermosetting material prepared by heat curable composition
BR112013005646A2 (en) * 2010-09-30 2019-09-24 Dow Global Technologies Llc epoxy polyester resin composition, curable epoxy polyester (epoxy ester) resin composition, cured resin, and process for preparing curable epoxy polyester (epoxy ester) resin composition
KR20130114117A (en) 2010-09-30 2013-10-16 다우 글로벌 테크놀로지스 엘엘씨 Coating compositions
US9080059B2 (en) 2010-09-30 2015-07-14 Blue Cube Ip Llc Coating compositions
EP2621994A1 (en) 2010-09-30 2013-08-07 Dow Global Technologies LLC Epoxy resin compositions

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CH532623A (en) * 1969-06-13 1973-01-15 Ciba Geigy Ag Process for the production of stable preparations of water-soluble or dispersible reaction products from epoxides and amines
US4778861A (en) * 1985-12-16 1988-10-18 E. I. Du Pont De Nemours And Company Coating composition containing hydroxy-functional epoxy-polyester graft copolymers
US4816528A (en) * 1986-06-23 1989-03-28 E. I. Dupont De Nemours And Company Chip resistant coating compositions containing epoxy-polyester graft copolymers
AU728883B2 (en) * 1996-12-31 2001-01-18 Shell Internationale Research Maatschappij B.V. Storage stable compatible curing agent compositions for epoxy resins self curable at sub-ambient temperatures

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI779050B (en) * 2018-06-15 2022-10-01 達興材料股份有限公司 Resin composition and lamination method for semiconductor substrates by using the same

Also Published As

Publication number Publication date
WO2008045882A1 (en) 2008-04-17

Similar Documents

Publication Publication Date Title
TW200835708A (en) Soluble polymers with high conversion of acid from aromatic epoxy resins and diacids and crosslinked coatings prepared therefrom
US5319004A (en) Hardener for epoxy resins comprising reaction products of polyamidoamines, secondary polyamines and epoxy-polyol adducts
US5908902A (en) Self-emulsifying aqueous epoxy resin dispersions
WO2008045894A1 (en) Soluble polymers with low conversion of acids from aromatic epoxy resins and diacids and crosslinked coatings prepared therefrom
JP5797759B2 (en) Coating composition
JP5795804B2 (en) Coating composition
CN102666634B (en) Aqueous epoxy resin dispersions
US20080081883A1 (en) Polyester Polyols Derived From 2,5-Furandicarboxylic Acid, and Method
EP0617726B1 (en) Water compatible amine terminated resin useful for curing epoxy resins
WO2008045889A1 (en) Process for preparing soluble polymers with low conversion of acid from aromatic epoxy resins and diacids and process for preparing crosslinked coatings therefrom
TW200838893A (en) Process for preparing soluble polymers with high conversion of acid from aromatic epoxy resins and diacids and process for preparing crosslinked coatings therefrom
JP2014173090A (en) Epoxy resin compositions, methods of making the compositions, and articles thereof
CN110408013A (en) A kind of polyester resin for powder coating and preparation method thereof
US6569959B1 (en) Modified phenolic hydroxyl-containing resin by reacting epoxy resin with difunctional phenol
JP2002097250A (en) Epoxy resin, its reaction product, and curable resin composition using the same
US6555628B2 (en) Epoxy resins and process for making the same
JPH0940759A (en) Curable epoxy resin composition
US20020042493A1 (en) Epoxy resins and process for making the same
JPH09111099A (en) Emulsifier system for epoxy resin system which can be diluted with water and of which the end of pot life can be recognized
TWI753171B (en) Epoxy resins, compositions containing epoxy resins and their hardened products
EP0941286B1 (en) Self-dispersing curable epoxy resins, dispersions made therewith, and coating compositions made therefrom
EP2510035B1 (en) Hydroxyl-functional polyester resins
CN102272199A (en) Hydroxyl-functional polyethers and a preparation process therefor
CN110494468B (en) Glycidylamine epoxy resins based on AMES negative amines
WO2021042285A1 (en) Self-emulsifying epoxy composition and the coating composition prepared from the same