TW561180B - Compositions containing a polyarylene ether and a dispersible reactive solvent and articles prepared therefrom - Google Patents
Compositions containing a polyarylene ether and a dispersible reactive solvent and articles prepared therefrom Download PDFInfo
- Publication number
- TW561180B TW561180B TW88103297A TW88103297A TW561180B TW 561180 B TW561180 B TW 561180B TW 88103297 A TW88103297 A TW 88103297A TW 88103297 A TW88103297 A TW 88103297A TW 561180 B TW561180 B TW 561180B
- Authority
- TW
- Taiwan
- Prior art keywords
- scope
- polyarylene ether
- tpu
- composition
- less
- Prior art date
Links
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
五、發明説明(1 ) 本發明係有關-種包含聚亞芳基鍵及可分散之反應性 溶劑之組成物。聚亞芳基越(PAE)係—種具有優異機械 及電性質、熱阻性、阻燃性、低濕氣吸收及尺寸穩定性之 熱塑性樹脂。此等樹脂被廣泛用於汽車内部,特別是儀表 板及電和電子應用上。 一 PAE因其相對於其氧化降解溫度而言之高炫融黏度及 其尚加工處理溫度之結果而難以處理(例如,藉由注模) 。結果,PAE-般與可相容之聚合物摻合,諸如,聚苯乙 稀(W0 97/21771及美國專利第4,8〇4,712號案);聚酿胺( 美國專利第3,379,792號案);聚烯烴(美國專利第3,351,851 號案),橡膠改質苯乙烯樹脂(美國專利第3,383,435及 3,959,211及Ger· 〇ffen·第2,047,613號案);及聚苯乙婦及聚 碳酸酯之混合物(美國專利第3,933,941及4,446,278號案) 。不幸地,加工處理之改良一般係於付出撓曲模量、撓曲 強度及熱變形溫度而獲得之。 環氧樹脂亦已被研究作為PAE之反應溶劑(參見 Venderbosch,R. W·,“使用反應性溶劑加工處理難處理之聚 合物’’,Ph.D·論文,Eindhoven(1995) ; Vanderbosch等人, 聚。物’第35冊’第 4349頁(1994);\^11(161*13〇8〇11等人, 聚合物’第36冊,第1167頁(1995a);及Vanderbosch等人 ,聚合物,第36冊,第2903頁(1995b)。於此例子中,PAE 係被先溶於環氧樹脂以形成較佳為均質之溶液。然後由該 溶液形成物件,溶液於升高溫度時固化,形成相分離,其 可產生具有散佈於其間之環氧化物之連續PAE相。最後物 本紙張尺度適用中國國家標準(_) A4規格(21〇><297公董) 561180 A7 B7 五、發明説明(2 件之性質主要係由PAE決定之;但是,使用環氧樹脂作為 PAE之反應溶劑於連續熔融方法(例如,注模)中係不實際, 因為環氧樹脂需固化劑固化之。固化劑會隨時間累積於^主 模桶内,而使機器堵塞。再者,固化及其後之相分離需發 生於至少150°C,其於鑄模環境係不實際。 基於業界中之缺失,所期望者係發現一種能解決於用 於PAE之某些反應溶劑内之加工處理問題之反應溶劑,而 不會對PAE之物理性質產生不利影響者。 本發明注重於業界之需求,其一方面藉由提供含有熔 融之t亞方基鍵及反應溶劑(其係熱塑性聚氨基甲酸酯或 環戊二烯)之組成物,其中該聚亞芳基醚以下述化學式表之 -(Ar-0)n- 其中,Ar係被取代或未被取代之芳族核,且n係至少 10之整數,但當反應溶劑為具有少於5〇tiTg之熱塑性聚 氨基f酸S旨時,聚亞芳基ϋ及反應溶劑包含該組成物之至 少60重量%。 於第二方面’本發明係一種包含a)可分散反應溶劑, 其係熱塑性聚氨基甲_旨或環戊二婦;及_下述化學式 表示之聚亞芳基醚之分散物: (Ar-0)n. 其中,域被取代或未被取代之芳族核,心係至少〆 整數’但當反應溶劑為具有少⑽1之私熱塑性聚氨基 甲酸醋時’聚亞芳基醚及反應溶劑包含該组成物之至 10之 少605. Description of the invention (1) The present invention relates to a composition comprising a polyarylene bond and a dispersible reactive solvent. Polyarylene (PAE) series—a thermoplastic resin with excellent mechanical and electrical properties, thermal resistance, flame retardancy, low moisture absorption, and dimensional stability. These resins are widely used in automotive interiors, especially in dashboards and electrical and electronic applications. A PAE is difficult to handle (for example, by injection molding) because of its high melt viscosity relative to its oxidative degradation temperature and its processing temperature. As a result, PAE-like blends with compatible polymers, such as polystyrene (WO 97/21771 and U.S. Patent No. 4,8,04,712); polyamines (U.S. Patent No. 3,379,792) Polyolefins (U.S. Patent No. 3,351,851), rubber modified styrene resins (U.S. Patent Nos. 3,383,435 and 3,959,211 and Ger · Offen · No. 2,047,613); and mixtures of polystyrene and polycarbonate (U.S. Patent Nos. 3,933,941 and 4,446,278). Unfortunately, improvements in processing are generally obtained by paying for flexural modulus, flexural strength, and heat distortion temperature. Epoxy resins have also been studied as reactive solvents for PAE (see Venderbosch, R.W., "Processing difficult polymers with reactive solvents", Ph.D. thesis, Eindhoven (1995); Vanderbosch et al. , Poly. "Vol. 35", p. 4349 (1994); \ ^ 11 (161 * 130081, et al., Polymers, Vol. 36, p. 1167 (1995a); and Vanderbosch et al., Polymerization Materials, Book 36, Page 2903 (1995b). In this example, PAE is first dissolved in epoxy resin to form a better homogeneous solution. Objects are then formed from this solution, and the solution solidifies at elevated temperatures , Forming a phase separation, which can produce a continuous PAE phase with epoxide interspersed between them. The final physical paper size applies the Chinese national standard (_) A4 specification (21〇 > < 297 public director) 561180 A7 B7 5 2. Description of the invention (The nature of the 2 pieces is mainly determined by PAE; however, it is not practical to use epoxy resin as a PAE reaction solvent in a continuous melting method (for example, injection molding), because epoxy resin requires a curing agent to cure. The curing agent will accumulate in the main mold barrel over time, and Machine clogging. In addition, curing and subsequent phase separation must occur at least 150 ° C, which is not practical in the mold environment. Based on the lack of the industry, the expectant is to find a solution that can be used for some PAE The reaction solvent for processing problems in the reaction solvent, which does not adversely affect the physical properties of the PAE. The present invention focuses on the needs of the industry, on the one hand, by providing a molten t-subunit bond and a reaction solvent (which is Thermoplastic polyurethane or cyclopentadiene) composition, wherein the polyarylene ether is represented by the following chemical formula-(Ar-0) n- wherein Ar is a substituted or unsubstituted aromatic core , And n is an integer of at least 10, but when the reaction solvent is a thermoplastic polyamino f acid S having less than 50 tiTg, the polyarylene fluorene and the reaction solvent include at least 60% by weight of the composition. In a second aspect, the present invention is a dispersion containing a) a dispersible reaction solvent, which is a thermoplastic polyurethane or cyclopentane; and a dispersion of a polyarylene ether represented by the following chemical formula: (Ar-0) n. Among them, the domain is replaced or not replaced Aromatic nucleus, heart 〆 an integer of at least 'the reaction solvent but having less of the private ⑽1 when the thermoplastic polyurethane vinegar' poly (arylene ether) and the reaction solvent containing the composition of matter at least 60 10
(請先閱讀背面之注意事項再填寫本頁) .、'^丨 :線丨 561180 A7 --—_____B7 ____ 五、發明説明(3 ) 重量%。 於另一方面,本發明係一種包含熔融之聚亞芳基醚及 熱塑性聚氨基甲酸酯之組成物,其具有不少於50°C之Tg , 其中該聚亞芳基醚係以如下所示化學式表之: -(Ar-0)n- 其令’ Ar係被取代或未被取代之芳族核,且η係至少1 〇之 整數。 TPU於高溫時係不可聚合,造成熔融黏度之重大降低 ’且於低溫時可再聚合。相似地,環戊二烯於高溫時從事 反式之Diels-Alder反應,而於冷卻及適當催化劑存在中, 建構分子量以再形成聚環戊二烯。因此,TPU及環戊二烯 可在無添加熱下有利地固化。再者,PAE/TPU或PAE/環戊 二婦之溶融摻合物有利者係均質,而冷卻物件係相分離者 。此特徵能使熔融物於低於PAE之降解溫度之溫度加工處 理,但保持未摻混pAE之性質。 一方面,本發明係一種包含PAE及TPU或環戊二烯之 溶融物,較佳係TPU。PAE係以下述化學式表示之: -(Ar-0)n- 其中,Αι*係被取代或未被取代之芳族核,且η係至少 1〇之整數。芳族核可為,例如,伸苯基、烷化伸苯基、氯 伸笨基、溴伸苯基及萘基。Αι·較佳係2,6-二曱基-1,4-伸苯 基、2-甲基-6-乙基·1,4-伸苯基、2,6-二乙基-1,4-伸苯基, 及2,3,6-三曱基-1,4-伸苯基;Ar更佳係2,6-二曱基-1,4-伸苯 基。較佳之ΡΑΕ係聚(2,6-二甲基-1,4-伸苯基)醚,且藉由 本紙張尺度適用中國國家標準(CNS) Α4規格(210X297公釐) (請先閲讀背面之注意事項再填寫本頁)(Please read the precautions on the back before filling this page)., '^ 丨: Line 丨 561180 A7 ---_____ B7 ____ 5. Description of the invention (3) Weight%. In another aspect, the present invention is a composition comprising a molten polyarylene ether and a thermoplastic polyurethane, which has a Tg of not less than 50 ° C, wherein the polyarylene ether is as follows The chemical formula table shows:-(Ar-0) n- which makes' Ar a substituted or unsubstituted aromatic nucleus, and η is an integer of at least 10. TPU is not polymerizable at high temperatures, causing a significant reduction in melt viscosity ′ and repolymerizable at low temperatures. Similarly, cyclopentadiene engages the trans-Diels-Alder reaction at high temperatures, and in the presence of cooling and a suitable catalyst, the molecular weight is constructed to re-form polycyclopentadiene. Therefore, TPU and cyclopentadiene can be favorably cured without adding heat. Furthermore, PAE / TPU or PAE / cyclopentanthyl fused blends are homogeneous, while cooling objects are phase separated. This feature enables the melt to be processed at a temperature below the degradation temperature of the PAE, but retains the properties of unblended pAE. In one aspect, the present invention is a melt comprising PAE and TPU or cyclopentadiene, preferably TPU. PAE is represented by the following chemical formula:-(Ar-0) n- wherein Aι * is a substituted or unsubstituted aromatic core, and η is an integer of at least 10. The aromatic core may be, for example, phenylene, alkylated phenylene, chlorophenylene, bromophenyl, and naphthyl. Aι · Preferably 2,6-Difluorenyl-1,4-phenylene, 2-methyl-6-ethyl · 1,4-phenylene, 2,6-diethyl-1,4 -Phenylene, and 2,3,6-trifluorenyl-1,4-phenylene; Ar is more preferably 2,6-diamidyl-1,4-phenylene. The preferred PAE is a poly (2,6-dimethyl-1,4-phenylene) ether, and according to this paper size, the Chinese National Standard (CNS) A4 specification (210X297 mm) is applied (please read the note on the back first) (Fill in this page again)
561180 A7 ~------- 57 五、發明説明(4 ) 2,6-一甲基酚及2,3,6-三甲基酚與聚(2,6_二甲基-伸苯 基)醚之聚合反應獲得之共聚物為更佳。 此處所用之”可分散反應溶劑,,一辭係指於高溫時成具 有PAE之溶液之物質,且其於冷卻時形成具有pAE之均質分 散物。此溶液較佳係均質溶液,且可分散之反應溶劑較佳 係分散相。此等可分散反應溶劑之例子包含熱塑性聚氨基 甲酸酯(TPU)及環戊二烯,且以TPU較佳。 TPU含有自聚異氰酸酯、多官能基鏈延伸劑及選擇性 之高分子量多元醇之反應形成之結構單元。用以形成TPU 之聚異氰酸酯較佳係二異氰酸酯,其可為芳族、脂族或環 脂族。此等較佳二異氰酸酯之代表性例子可被發現於美國 專利第4,385,133; 4,522,975及5,167,899號案。較佳之二異 氰酸酯包含4,4,-二異氰酸二苯基甲烷、對-伸苯基二異氰酸 醋、1,3-雙(異氰酸基曱基)環己烷、丨,‘二異氰基環己烧 、六伸甲基二異氰酸酯、1,5_萘基二異氰酸酯、3,3,_二甲 基4,4 -雙本基二異氰酸酯、4,4’-二異氰酸基環己基曱燒及 2,4-甲苯二異氰酸酯,或其等之混合物。更佳者係4,4, ·二 異氰酸基環己基甲烷及4,4,-二異氰酸二苯基甲燒。 此處所用之,,多官能基鏈延伸劑,,一辭係指低分子量多 元醇’較佳係具有不多於200之分子量之二元醇。較佳之鍵 延伸劑包含乙二醇、1,3_丙二醇、1,4-丁二醇,丨,^戊二醇 、1,6_己二醇、二乙二醇、三乙二醇、四乙二醇、新戊基 二醇、1,4·環己烷二曱醇及1.4-雙羥基乙基氫醌及其等之混 合物。特佳之二官能基鏈延伸劑包含1,6-己二醇及丨,4-丁二 本紙張尺度適用中國國家標準 (CNS) Α4規格(210X297公釐) 561180 A7 _ B7__ 五、發明説明(5 ) ㈣ ~' ~ 醇及二乙二醇之混合物、1,4_丁二醇及三乙二醇及丨,4_丁二 醇及四乙二醇。 TPU亦可包含衍生自芳族二元醇之反應而形成之單 元,較佳係於足夠濃度以降低剛性TPU可被熔融處理之溫 度。此等TPU被揭示於美國專利第5,574,092號案。適♦之 方族一元醇之例子包含間苯二紛、catechol、氫g昆、二經基 萘、二羥基鄰氨基苯烯、雙(羥基芳基)努、二羥基菲、 二羥基二苯及雙(羥基苯基)丙烷。較佳之芳族二係 包含氫醌、4,4、二羥基雙苯、9,9,_雙(‘羥基苯基)芴及 雙酚-A。 當芳族二元醇被使用時,芳族二元醇之量較佳不超過 造成TPU於斷裂時之抗張延伸率少於5%之量,其係以 ASTM D-638決定之。較佳者,芳族二元醇之濃度不少於〇 ι (更佳係不少於0.5,最佳係不少於丨)莫耳%,且較佳係 不多於20(更佳係不多於10,最佳係不多於5)莫耳%,其係 以用以製備TPU之二元醇之總莫耳數為基準。 此處所用之,,高分子量多元醇,,一辭係指多元醇,較佳 係具有少於約50〇amu之分子量之二元醇,較佳係不少於約 6〇〇amu,更佳係不少於約1〇〇〇amu,且較佳係不多於約 6000麵,更佳係不多於約3_咖,最佳係不多於約 2_咖。選擇性之高分子量二㈣之例子包含聚鱗二元 醇,諸如,聚丙二醇、聚乙二醇及聚四伸甲基二醇;及聚 酯二醇,諸如,聚己内酯二醇,及能由脂族二酯或二(酸 氯化物)與C2_CS之線性、分枝或環狀二醇或含醚之二醇^ 本紙張尺度適用中國國家標準(CNS) A4規格(210X297公釐) (請先閲讀背面之注意事項再填寫本頁) •、?1· :線丨 561180 A7 B7 五、發明説明(6 ) 之縮合反應製得之化合物,或其摻合物。更佳之高分子量 聚酉旨二醇包含聚己内醋二醇、聚伸乙基己二醋二醇及聚伸 丁基己二酯二醇。 TPU有利者係於適當催化劑存在中製備,諸如,美國 專利第5,068,306號案,第5攔第46行至第0攔第5行所揭示 者。較佳之催化劑包含辛酸亞錫、油酸亞錫。二辛酸二丁 基錫及二月桂酸二丁基錫。所用之催化劑量係足以增加異 氰酸酯基與ΟΗ基之反應性而且無不利影響最後產物性質 者,且較佳範圍係以反應物之總重量計係約〇 ·〇2至約2 ·〇重 量%。 反應物之異氰酸酯對ΟΗ之比例較佳係不少於〇.95:1 ,更佳係不少於0.975:1,最佳係不少於〇·985:1,且較佳係 不多於1.05:1,更佳係不多於L025:1,最佳係不多1〇15:1 〇 TPU可藉由諸如業界所知之批式或連續方法適當製 備之。較佳之連續混合方法係反應壓出,諸如,美國專利 第3,642,964號案所揭示之雙螺桿壓出方法。 適用於作為PAE反應溶劑使用之TPU可為剛性之τρυ 或軟式TPU。剛性TPU具有不少於50°C之玻璃轉移溫度, 且其進一步之特徵係具有硬區段(即,自聚異氰酸酯與二 官能基鏈延伸劑之聚合反應形成之結構單元),其較佳係以 TPU重量為基準係不少於約75重量%,更佳係不少於約9〇 重量%,及高至約100重量%。可購得之剛性TPU種類包含 isoplasttm聚氨基甲酸酯工程用熱塑性樹脂(陶氏化學 本紙張尺度適用中國國家標準(⑽)A4規格(21〇><297公釐) (請先閲讀背面之注意事項再填寫本頁)561180 A7 ~ ------- 57 V. Description of the invention (4) 2,6-monomethylphenol and 2,3,6-trimethylphenol and poly (2,6_dimethyl- benzene) The copolymer obtained by the polymerization reaction of a (based) ether is more preferred. As used herein, the term "dispersible reaction solvent" refers to a substance that forms a solution with PAE at high temperature and forms a homogeneous dispersion with pAE when cooled. This solution is preferably a homogeneous solution and is dispersible The reaction solvent is preferably a dispersed phase. Examples of such dispersible reaction solvents include thermoplastic polyurethane (TPU) and cyclopentadiene, and TPU is preferred. TPU contains self-polyisocyanate and polyfunctional chain extension A structural unit formed by the reaction of an agent and a selective high-molecular-weight polyol. The polyisocyanate used to form the TPU is preferably a diisocyanate, which may be aromatic, aliphatic, or cycloaliphatic. Representatives of these preferred diisocyanates Exemplary examples can be found in U.S. Patent Nos. 4,385,133; 4,522,975 and 5,167,899. Preferred diisocyanates include 4,4, -diisocyanate diphenylmethane, p-phenylene diisocyanate, 1 , 3-bis (isocyanatofluorenyl) cyclohexane, 丨, 'diisocyanocyclohexane, hexamethylidene diisocyanate, 1,5-naphthyl diisocyanate, 3,3, _dimethyl 4,4 -dibenzyl diisocyanate, 4,4'-diiso Acid-based cyclohexyl fluorene and 2,4-toluene diisocyanate, or a mixture thereof. More preferred are 4,4, · diisocyanatocyclohexylmethane and 4,4, -diisocyanate diphenyl. Melamine. As used herein, the term "multifunctional chain extender" refers to a low molecular weight polyol 'preferably a glycol having a molecular weight of not more than 200. A preferred bond extender includes ethylene diethylene glycol. Alcohol, 1,3-propanediol, 1,4-butanediol, pentamethylene glycol, 1,6-hexanediol, diethylene glycol, triethylene glycol, tetraethylene glycol, neopentyl diethylene glycol Alcohols, 1,4 · cyclohexanediethanol and 1.4-bishydroxyethylhydroquinone and mixtures thereof. Particularly preferred bifunctional chain extenders include 1,6-hexanediol and 1,4-butanediol. This paper size applies the Chinese National Standard (CNS) A4 specification (210X297 mm) 561180 A7 _ B7__ V. Description of the invention (5) ㈣ ~ '~ A mixture of alcohol and diethylene glycol, 1,4-butanediol and three Ethylene glycol and 丨 4-butanediol and tetraethylene glycol. TPU can also include units derived from the reaction of aromatic diols, preferably at a sufficient concentration to reduce rigidity. TPU can be melt processed. Temperature. These TPUs are disclosed in U.S. Patent No. 5,574,092. Examples of suitable square group monohydric alcohols include m-phenylene, catechol, hydrogen g-quinone, dibasic naphthalene, dihydroxy anthranilene, bis ( Hydroxyaryl) nu, dihydroxyphenanthrene, dihydroxydiphenyl, and bis (hydroxyphenyl) propane. Preferred aromatic secondary systems include hydroquinone, 4,4, dihydroxybisbenzene, 9,9, _bis (' Hydroxyphenyl) fluorene and bisphenol-A. When aromatic diols are used, the amount of aromatic diols is preferably not more than the amount that causes the tensile elongation of the TPU at break to be less than 5%, which It is determined by ASTM D-638. Preferably, the concentration of the aromatic diol is not less than 0 m (more preferably, not less than 0.5, most preferably not less than 丨) mole%, and more preferably not more than 20 (more preferably, no More than 10, the best is not more than 5) mole%, which is based on the total mole number of the glycol used to prepare the TPU. As used herein, the term high molecular weight polyol refers to a polyol, preferably a glycol having a molecular weight of less than about 500,000 amu, more preferably not less than about 600 amu, more preferably The line is not less than about 1,000 amu, and preferably is not more than about 6,000 noodles, more preferably is not more than about 3 coffee, and the best is not more than about 2 coffee. Examples of selective high molecular weight difluorenes include polyscale glycols such as polypropylene glycol, polyethylene glycol, and polytetramethylene glycol; and polyester glycols such as polycaprolactone glycol, and Can be linear, branched or cyclic diols or ether-containing diols from aliphatic diesters or bis (acid chlorides) and C2_CS ^ This paper size applies to China National Standard (CNS) A4 (210X297 mm) ( (Please read the precautions on the back before filling this page) •,? 1:: line 丨 561180 A7 B7 V. Compound prepared by the condensation reaction of the description of the invention (6), or its blend. More preferred high molecular weight polyglycol glycols include polycaprolactone glycol, poly (ethylene adipate) and poly (butylene adipate) glycol. TPU favors are prepared in the presence of a suitable catalyst, such as those disclosed in U.S. Patent No. 5,068,306, line 5 from line 46 to line 0, line 5. Preferred catalysts include stannous octoate and stannous oleate. Dibutyltin dioctanoate and dibutyltin dilaurate. The amount of the catalyst used is sufficient to increase the reactivity of the isocyanate group and the oxo group without adversely affecting the properties of the final product, and a preferred range is from about 0.02 to about 2.0% by weight based on the total weight of the reactants. The ratio of the isocyanate to 〇Η of the reactant is preferably no less than 0.95: 1, more preferably no less than 0.975: 1, most preferably no less than 0.985: 1, and more preferably no more than 1.05 : 1, more preferably no more than L025: 1, most preferably no more than 1015: 1. TPU can be appropriately prepared by, for example, batch or continuous methods known in the industry. A preferred continuous mixing method is reactive extrusion, such as the twin-screw extrusion method disclosed in U.S. Patent No. 3,642,964. The TPU suitable for use as a PAE reaction solvent may be a rigid τρυ or a soft TPU. The rigid TPU has a glass transition temperature of not less than 50 ° C, and its further feature is that it has a hard segment (ie, a structural unit formed from the polymerization reaction of a polyisocyanate and a difunctional chain extender), which is preferably Based on the weight of the TPU is not less than about 75% by weight, more preferably not less than about 90% by weight, and up to about 100% by weight. Available types of rigid TPU include isoplasttm polyurethane engineering thermoplastic resin (The Dow Chemical paper size applies Chinese National Standard (⑽) A4 specification (21〇 > < 297mm) (Please read the back first (Notes for filling in this page)
•、可I :線丨 9 561180 A7 _ _B7__ 五、發明説明(7 ) 公司之商標)。 軟式TPU具有少於50°c之Tg,較佳係少於25°C,其進 一步之特徵在於具有以TPU重量為基準為不多於75重量% 之硬區段。較佳之軟式TPU例子係PELLETHANEtm熱塑性 聚氨基甲酸酯(陶氏化學公司之商標)。 PAE/TPU摻合物之一非平常之特徵係混合物於熔融 物時係均質,但於熔融物冷卻時變成非均質。熔融物之均 質使摻合物可於低於PAE氧化降解溫度之溫度時加工處理 :當熔融物被冷卻,TPU相分離,且TPU於PAE連續相中形 成分散物,如此,最終物件之物理性質(例如,熱變形溫 度、撓曲模量及撓曲強度)更像未摻合之PAE。 熔融摻合物(及最終物件)内之PAE對TPU之重量對重 量之比例一般係大於1:1。其亦可能於PAE/TPU摻合物内包 含其它熱塑性聚合物,諸如,聚笨乙烯(PS)、間規PS或 聚乙烯基環己烷。PAE/TPU摻合物係特別有用於需要保持 PAE之高熱性質之注模應用。 下列範例僅係用以例示而非用以限制本發明之範圍。 範例1-6 聚(2,6-二甲基-1,4-伸苯基醚)(PPO 803,自 General Electric Plastics,Bergen op Zoom,荷蘭得之)之各種摻合物 以剛性TPU(ISOPLASTtm 2530聚氨基曱酸酯工程熱塑性 '樹脂,陶氏化學公司之商標名)或軟式TPU (PELLETHANEtm 2102-75A熱塑性聚氨基甲酸酉旨,P匈氏化 學公司之商標名)及選擇性之聚苯乙烯N5000樹脂(由Shell 10 (請先閲讀背面之注意事項再填寫本頁) :線丨 度適用中國國家標準(CNS) A4規格(210 X 297公釐) 561180 A7 ___B7_ 五、發明説明(8 ) 獲得,重量平均分子量係3〇5,000;Mw/Mn係2·37)製備。 ΡΡΟ樹脂及聚苯乙烯之樣品於245°C之單一螺桿壓出 機以50/50重量對重量之比例及於250°C以75/25之重量對 重量之比例製備之。此等樣品被顆粒化且與剛性TPU或軟 式TPU摻合,然後於Arburg 270M單一螺桿注模機内以不同 溫度模式、壓力及模製溫度(如第I表所示)混合之。PPO 樹脂及TPU之樣品於注模機内製備。PPO/軟式TPU摻合物 先於雙滚輪混合器内於245°C混合,其係因粉碎軟式TPU之 困難之故。 第I表-製備placque之模製條件 (請先閲讀背面之注意事項再填寫本頁) 樣品(w/w) 溫度模式(C) 壓力(巴) 模製溫度 (°〇 70PPE/30 剛性 TPU 235/240/245/250/250 1860 60 70(50PPE-50PS)30 剛性TPU 230/240/250/260/260 1700 30 70(50PPE-50PS)30 軟式TPU 230/240/250/260/260 1700 30 70(75PPE-25PS)30 軟式TPU 270/280/290/295/300 1860 30 70(75PPE-25PS)30 軟式TPU 240/250/260/265/270 1550 30 .訂丨 :線丨 各種樣品之T g使用動力機械熱分析分析之。二T g於每 一情況中觀察出。樣品被拋光至丨-爪㈤及3·111111厚度,及至 13-mm及25-mm厚度,且使用2°C /分鐘之加熱速率於抗張模 式分析。第II表例示各種樣品之Tg、撓曲模量及撓曲強度 11 本紙張尺度適用中國國家標準(CNS) A4規格(210 X 297公爱) 561180 A7 B7 五、發明説明(9 ) 第2表-PPE TPU摻合物之物理性質 樣品(w/w) Tg (°C) 撓曲模量 (MPa) 撓曲強度 (MPa) 70PPE/30 剛性 TPU 110,230 4.6 26 70(50PPE-50PS)30 剛性 TPU 110,164 3.3 32 70(50PPE-50PS)30 軟式 TPU -40,164 2.0 16 70(75PPE-25PS)30 軟式 TPU 110,190 3.1 35 70(75PPE-25PS)30 軟式 TPU -40,191 2.8 21 (請先閱讀背面之注意事項再填寫本頁)• 、 可 I: line 丨 9 561180 A7 _ _B7__ V. Description of Invention (7) Trademark of the company). The soft TPU has a Tg of less than 50 ° C, preferably less than 25 ° C. It is further characterized by having a hard segment of not more than 75% by weight based on the weight of the TPU. A preferred example of a soft TPU is PELLETHANEtm thermoplastic polyurethane (trademark of The Dow Chemical Company). One unusual feature of PAE / TPU blends is that the mixture is homogeneous when melted, but becomes heterogeneous when the melt cools. The homogeneity of the melt allows the blend to be processed at a temperature below the oxidative degradation temperature of the PAE: When the melt is cooled, the TPU phase separates, and the TPU forms a dispersion in the continuous phase of the PAE. In this way, the physical properties of the final object (Eg, heat distortion temperature, flexural modulus, and flexural strength) are more like unblended PAE. The weight-to-weight ratio of PAE to TPU in the melt blend (and the final article) is generally greater than 1: 1. It is also possible to include other thermoplastic polymers in PAE / TPU blends, such as polyethylene (PS), syndiotactic PS or polyvinylcyclohexane. PAE / TPU blends are particularly useful in injection molding applications where the high thermal properties of PAE need to be maintained. The following examples are only for illustration and not for limiting the scope of the present invention. Example 1-6 Various blends of poly (2,6-dimethyl-1,4-phenylene ether) (PPO 803, available from General Electric Plastics, Bergen op Zoom, the Netherlands) with rigid TPU (ISOPLASTtm 2530 Polyurethane Engineering Thermoplastic 'Resin, Trade Name of The Dow Chemical Company) or Soft TPU (PELLETHANEtm 2102-75A Thermoplastic Polyurethane Purpose, Trade Name of P Hungarian Chemical Company) and Selective Polystyrene N5000 resin (by Shell 10 (please read the precautions on the back before filling in this page): the line applies the Chinese National Standard (CNS) A4 specification (210 X 297 mm) 561180 A7 ___B7_ V. Description of the invention (8) , Weight average molecular weight is 35,000; Mw / Mn is 2.37). Samples of PPO resin and polystyrene were prepared in a single screw extruder at 245 ° C in a 50/50 weight to weight ratio and at 250 ° C in a 75/25 weight to weight ratio. These samples were pelletized and blended with rigid TPU or soft TPU, and then mixed in an Arburg 270M single screw injection molding machine in different temperature modes, pressures, and molding temperatures (as shown in Table I). Samples of PPO resin and TPU were prepared in an injection molding machine. The PPO / soft TPU blend was mixed at 245 ° C before the double-roller mixer, which was due to the difficulty in crushing the soft TPU. Table I-Molding conditions for preparing placque (please read the notes on the back before filling this page) Sample (w / w) Temperature mode (C) Pressure (bar) Molding temperature (° 〇70PPE / 30 Rigid TPU 235 / 240/245/250/250 1860 60 70 (50PPE-50PS) 30 Rigid TPU 230/240/250/260/260 1700 30 70 (50PPE-50PS) 30 Soft TPU 230/240/250/260/260 1700 30 70 (75PPE-25PS) 30 Soft TPU 270/280/290/295/300 1860 30 70 (75PPE-25PS) 30 Soft TPU 240/250/260/265/270 1550 30. Order 丨: Line 丨 T of various samples g using thermal mechanical thermal analysis. Two T g were observed in each case. The samples were polished to 丨 -claws and 3 · 111111 thickness, and to 13-mm and 25-mm thickness, and used 2 ° C / The heating rate of minutes is analyzed in the tensile mode. Table II illustrates the Tg, flexural modulus, and flexural strength of various samples. 11 This paper size applies to China National Standard (CNS) A4 (210 X 297 public love) 561180 A7 B7 V. Description of the invention (9) Table 2-Physical properties of PPE TPU blend samples (w / w) Tg (° C) Flexural modulus (MPa) Flexural strength (MPa) 70PPE / 30 Rigid TPU 110,230 4.6 26 70 (50PPE -50PS) 30 Rigid TPU 110,164 3.3 32 70 (50PPE-50PS) 30 Soft TPU -40,164 2.0 16 70 (75PPE-25PS) 30 Soft TPU 110,190 3.1 35 70 (75PPE-25PS) 30 Soft TPU -40,191 2.8 21 (Please first (Read the notes on the back and fill out this page)
本紙張尺度適用中國國家標準(CNS) A4規格(210 X 297公爱) 12 申4曰崩 ................................................ .—______ 案 號 ^ ju ^ ή 類 別 (以上各欄由本局填註)This paper size applies to China National Standard (CNS) A4 specification (210 X 297 public love) 12 Shen 4 said collapse ............... ............ ______ Case No. ^ ju ^ priced category (the above columns are filled out by this bureau)
C4 561180 經濟部中夬榡隼局貝工消費合作、杜印t •第 88103297 號 ^ 專利説明書. 稱 中 文 含有聚亞芳基醚與可分散的反應溶劑之組成物以及由之 所製備之物件 英 文 COMPOSITIONS CONTAINING A POLYARYLENE ETHER AND A DISPERSIBLE REACTIVE SOLVENT AND ARTICLES PREPARED THF.RRFROM 姓 名 (1) 愛德華L·胡吉 (2) 吉諾•庫加 一發明, 國 籍 (1)美國(2)荷蘭 BrnBeSj 住、居所 特·史汀希迪克街56號 (2)美國南卡羅萊納州斯巴运堡美麗森林路9011號 姓 名 (名稱) … 圓···丨 --------—一- ---—_ 1 美商·陶氏全球科技股份有限公司 國 籍 美國 三、申請人 住 '居所 (事務所) 美國後西根州密德蘭市•華盛頓衔丨79〇號大樓 代表人 姓 名 諾雷恩D·瓦瑞克 訂 線 本紙i尺度適用中關家標準(CNS〉A4g72丨〇><297公廣) 裝C4 561180 Shellfish Consumer Cooperation, Duyin t • No. 88103297 of the Ministry of Economic Affairs ^ Patent specification. It is said that the Chinese composition containing polyarylene ether and a dispersible reaction solvent and articles prepared therefrom COMPOSITIONS CONTAINING A POLYARYLENE ETHER AND A DISPERSIBLE REACTIVE SOLVENT AND ARTICLES PREPARED THF.RRFROM 56 St. Hidwick Street (2) 9011 Beautiful Forest Road, Spartanburg, South Carolina, USA Name (Name) ... -—_ 1 American Business · Dow Global Technology Co., Ltd. Nationality US III. Applicant's Residence (Office) Midland City, Post-Western United States • Washington Title 丨 No. 79 Representative of Building No. D · Warik's i-size paper applies Zhongguanjia standard (CNS> A4g72 丨 〇 > < 297)
Claims (1)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US7687598P | 1998-03-05 | 1998-03-05 |
Publications (1)
Publication Number | Publication Date |
---|---|
TW561180B true TW561180B (en) | 2003-11-11 |
Family
ID=32391970
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
TW88103297A TW561180B (en) | 1998-03-05 | 1999-03-04 | Compositions containing a polyarylene ether and a dispersible reactive solvent and articles prepared therefrom |
Country Status (1)
Country | Link |
---|---|
TW (1) | TW561180B (en) |
-
1999
- 1999-03-04 TW TW88103297A patent/TW561180B/en not_active IP Right Cessation
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4728693A (en) | Impact-resistant thermoplastic molding compounds based on polyphenylene ethers, polyoctenylenes and polyamides | |
White et al. | Poly (hydroxyaminoethers): a new family of epoxy‐based thermoplastics | |
EP2366728B1 (en) | Polymeric material | |
US20130217834A1 (en) | Polyarylene composition | |
JPH0264150A (en) | Composition containing polyphenylene ether/ polyester copolymer obtained from polyphenylene ether capped with epoxytriazine | |
JPS58141240A (en) | Polyphenylene ether resin composition | |
CN1986639A (en) | Thermosetting resin-base composite material and its preparing | |
JPH0514740B2 (en) | ||
JPS63289057A (en) | Compatible polyphenylene ether-linear polyester blend having improved thermal expansion rate | |
JPH01103653A (en) | Compatible polyphenylene ether-linear polyester compound containing mica reinforcing agent | |
JP5101782B2 (en) | Low molecular weight engineering thermoplastic polyurethanes and blends thereof | |
US5049615A (en) | Polyindanes as processing aid for engineering thermoplastics | |
TW561180B (en) | Compositions containing a polyarylene ether and a dispersible reactive solvent and articles prepared therefrom | |
EP1673412B1 (en) | Poly(arylene ether) composition and method of molding | |
JPS6322855A (en) | Shock resistant thermoplastic molding composition based on modified polyphenylene ether, polyoctenylene and polyamide | |
US6117943A (en) | Compositions containing a polyarylene ether and a dispersible reactive solvent and articles prepared therefrom | |
JPS63199753A (en) | Polystyrene modified in impact resistance by rubber and polyphenylene ether resin containing the same | |
Zhang et al. | Synthesis of novel polycarbonate‐based thermoplastic polyurethane elastomers compatibilizers with octadecyl side chains and their application in PC/PP blends | |
JPH02155951A (en) | Polyethylene sulfide resin composition | |
JPH02187455A (en) | Composition containing both polyphenylene ether resin and polyamide | |
US5886099A (en) | Thermoplastic polyester resin composition | |
MXPA00008693A (en) | Compositions containing a polyarylene ether and a dispersible reactive solvent and articles prepared therefrom | |
JPH0493352A (en) | Thermoplastic polyurethane having improved flowing | |
JPH03153757A (en) | Polyphenylene sulfide resin composition | |
JPH0711113A (en) | Thermoplastic molding material based on polyphenylene ether and polyester |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GD4A | Issue of patent certificate for granted invention patent | ||
MM4A | Annulment or lapse of patent due to non-payment of fees |