TW506973B - Transparent styrenic resin composition - Google Patents
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五Fives
、發明説明(1 ) B? "係有關於—種透明苯乙烯系樹脂組成物,尤指 合笨t:乙”樹脂中添加季戊四醇之醋類化合物,並配 加工f生“糸树月曰"寺定之低分子量含量,來得到透明性及 力工性良好,同時成型時 系樹脂組成物。 f不日產生模具 之透明苯乙烯 按,苯乙烯系樹脂是一種具有良好強度及加工成型性 之材料,尤其是透明的苯乙烯系樹脂更可被使用於透明食 包裝用材料等家庭用品、家電製品,以及〇a機器 ’惟由於目前苯乙烯系樹脂在加工上,其加工條 件對於成品的薄肉化以及大型化的需求曰益嚴苛,因此, 為了在不損及物性的前提下,提高樹脂成型品之加工性, 在已知的技藝中乃有業者在苯乙稀系樹脂中添加少量的滑 ^ ’以當作加卫成型時之輔助劑,藉以改善成型品之加工 流動性;而-般使用於苯乙稀系樹脂的加工輔助劑乃例如 :脂肪酸之金屬鹽類’其中,硬脂_、硬脂酸鋅、脂肪 酸之胺類(如乙烯雙硬脂醯胺)對於加工性確有改善的效果 如日本特公平第2-52923號發明專利中請案中曾述及, 在苯乙烯系樹脂製造時,於反應槽中加入丨“重量份的乙 烯雙硬脂醯胺溶液,可改善樹脂的加Π而日本=開昭 第63-33455號發明專利中請案中述及,在苯乙烯系樹脂中 加入硬脂酸鈣或硬脂酸鋅混練,可改善樹脂成型時之離模 性;另外,日本公開特許平7_82439號發明專利申請案中敘 述,在苯乙烯系樹脂中加入硬脂酸丁 _(butyl 及少 X- 經濟部中央標準局員工消費合作社印製 A7 -------- B7 發明説明g ) —_~一 里的二酸甘油酯(triglyceride),可改善樹脂的流動性及耐 衝擊性;然而在透明之苯乙烯系樹脂中添加入滑劑或離型 劑等添加物,雖可改善樹脂之加工性及離模性,但前述添 加物卻會造成樹脂之透明性變差,而無法得到具有良好透 明度之笨乙烯系樹脂;有些添加劑也會在射出成型時造成 杈具污染等情形,尤其是在高溫、薄肉化的射出成型時問 題將更為嚴重;本發明即欲解決上述先前技術所存在之缺 失。 因此’本發明係在提供一種透明性、加工性佳,且成 型時不會產生模具污染現象之透明苯乙烯系樹脂組成物。 而本發明之透明苯乙烯系樹脂組成物係由: < I >100重量份的透明苯乙烯系樹脂;及 < Π >0· 01〜5重量份的季戊四醇之酯類化合物所組成 j 其中,透明之苯乙烯系樹脂中二氣甲烷可溶物的分子 i小於350低分子量聚合物含量,佔全部可溶份的重量 %以下。 本發明之透明苯乙烯系樹脂係指具有透明性,一般而 言’係指尚未進一步加工著色前之光線穿透率在6〇%以上 者。 本每明之透明本乙浠糸樹脂可分為二類型,即經橡膠 改質之透明苯乙烯系樹脂及不含橡膠之透明苯乙烯系樹脂 。其中不含橡膠之透明苯乙烯系樹脂,係指含苯乙烯系單 體30重量%以上之苯乙烯系樹脂,亦即,苯乙烯系單體 -----14頁 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公t ) (請先閱讀背面之注意事項再填寫本頁)2. Description of the invention (1) B? &Quot; It is about a kind of transparent styrenic resin composition, especially Heben t: B "resin with pentaerythritol vinegar compound, and is processed with" Fangshu Yue Yue " " Temperature's low molecular weight content is used to obtain good transparency and mechanical properties. At the same time, it is a resin composition during molding. fThe transparent styrene button of the mold is not produced. The styrene resin is a material with good strength and processability. In particular, the transparent styrene resin can be used in household products and household appliances such as transparent food packaging materials. Products and 〇a machines'. Because of the current processing of styrenic resins, the processing conditions have strict requirements for thinning and large-sized products. Therefore, in order to improve the resin without compromising physical properties, In the known art, the processability of the molded product is to add a small amount of slip to the styrene resin to be used as an adjuvant during the molding process to improve the processing fluidity of the molded product; and- The processing aids generally used in styrene resins are, for example, metal salts of fatty acids, of which, stearin, zinc stearate, and amines of fatty acids (such as ethylene distearylamine) do have processability. The improvement effect is as described in the Japanese Patent Application No. 2-52923. When the styrene resin is manufactured, the reaction tank is filled with "丨 parts by weight of ethylene distearate" Solution, can improve the addition of resin. Japan = Kaizhao No. 63-33455 In the patent application, it is mentioned that adding calcium stearate or zinc stearate to styrene resin and kneading can improve the resin molding. In addition, it is described in Japanese Patent Application Laid-Open No. 7_82439 that butyl stearate is added to styrene resin (X-butyl and less X- Printed by A7, Consumer Cooperative of the Central Standards Bureau, Ministry of Economic Affairs- ------- B7 Description of the invention g) --- ~ Triglyceride, which can improve the fluidity and impact resistance of the resin; however, a slip agent is added to the transparent styrene resin Additives such as release agents and release agents can improve the processability and release properties of the resin, but the aforementioned additives will cause the resin's transparency to deteriorate, and stupid vinyl resins with good transparency cannot be obtained; some additives will also In the case of injection molding, the forks are contaminated and the like, especially in high temperature and thin meat injection molding. The problem will be more serious; the present invention intends to solve the shortcomings of the foregoing prior art. Therefore, the present invention is to provide A transparent styrenic resin composition that has good transparency and processability and does not cause mold contamination during molding. The transparent styrenic resin composition of the present invention is composed of: < I > 100 parts by weight of transparent Styrene resin; < Π > 0.01 to 5 parts by weight of pentaerythritol ester compound j Among which, the molecular weight i of the digas methane soluble matter in the transparent styrene resin is less than 350 and the low molecular weight polymerization The content of the transparent styrene-based resin of the present invention means that it has transparency, and generally, it means a light transmittance of 60% or more before further processing and coloring. Ben Mingming's transparent benzyl resin can be divided into two types, namely transparent styrene resin modified by rubber and transparent styrene resin without rubber. The transparent styrene-based resin without rubber refers to a styrene-based resin containing 30% by weight or more of a styrene-based monomer, that is, a styrene-based monomer ---- page 14 This paper is applicable to China Standard (CNS) A4 specification (210X297mmt) (Please read the precautions on the back before filling this page)
、1T 線·! 經濟部中央標準局員工消費合作社印製 Λ7 —_____ B7 五、發明説明(3 ) -- 购〇重量%,以及其他可共聚合單體〇〜7〇重量%所構成 者。上述其他可共聚合之單體並無特別限制,只要可與苯 乙稀糸單體共聚合且達成透明性者即可。 本發明不含橡膠之透明苯乙烯系樹脂的可共聚合單體 具體例可為:(甲基)丙烯酸酯系單體、丙烯腈系單體、馬 來醯亞胺系單體、(甲基)丙烯酸系、無水馬來酸及乙二醇 甲基丙烯酸酯,其中,(甲基)丙烯酸酯系單體可為:丙烯 酸甲酯、丙烯酸乙酯、丙烯酸丁酯、甲基丙烯酸甲酯、甲 基丙烯酸乙酯、甲基丙烯酸丙酯、甲基丙烯酸丁酯、甲基 丙烯酸苯甲酯、甲基丙烯酸己酯、甲基丙烯酸環己酯、甲 基丙烯酸十二烷基酯、甲基丙烯酸2-羥乙酯、甲基丙烯酸 縮水甘油酯,以及甲基丙烯酸二曱胺基乙酯等,其中以甲 基丙烯酸甲酯為較佳。 而丙烯腈系單體可為:丙烯腈或α -甲基丙烯腈,其中 ,以丙稀腈為較佳。 馬來醯亞胺系單體可選自:Ν-甲基馬來醯亞胺、Ν-異 丙基馬來醯亞胺、Ν- 丁基馬來醯亞胺、Ν-己基馬來醯亞胺 、Ν-辛基馬來醯亞胺、Ν_十二烷基馬來醯亞胺、Ν_環己基 馬來醯亞胺、Ν-苯基馬來醯亞胺、Ν-2,3-甲苯基馬來醯亞 胺、Ν-2,4-甲苯基馬來醯亞胺、Ν-2,3-乙苯基馬來醯亞胺、 Ν-2,4-乙苯基馬來醯亞胺、Ν-2,3-丁苯基馬來醯亞胺、Ν-2,4-丁苯基馬來醯亞胺、Ν-2,6-甲苯基馬來醯亞胺、Ν-2,3-氣苯 基馬來醯亞胺、Ν-2,4-氯苯基馬來醯亞胺、Ν-2,3-溴苯基馬 來酿亞胺、Ν-2,4 -漠苯基馬來酿亞胺等’其中’以Ν -本基 _____第 5 頁____ 本紙張尺度適用中國國家標準(CNS ) Α4規格(210Χ297公釐) (請先閱讀背面之注意事項再填寫本頁) 、1Τ 線·! 506973 A7 五、發明説明(4 ) 馬來醯亞胺為最佳。 而不含橡膠之透明苯乙烯系樹脂的具體例有··聚苯乙 烯系、苯乙烯系-丙烯腈系共聚物、苯乙烯系甲基)丙烯酸 ,系共聚物、苯乙烯系置換馬來醯亞胺系·丙烯腈系共 聚物、苯乙烯系置換馬來醯亞胺系共聚物、苯乙烯系一( 甲基)丙烯酸酯系-Ν-置換馬來醯亞胺系共聚物、苯乙烯系_ Ν-置換馬來醯亞胺系-丙料系_(甲基)丙烯酸酉旨系共聚物等 經濟部中央標準局員工消費合作社印製 (請先閲讀背面之注意事項再填寫本頁) 、1Τ 本發明透明苯乙稀系樹脂之另一類㉟:經橡膠改質之 透明苯乙烯系樹脂,較佳為經二稀系橡膠改質之透明苯乙 烯系樹脂。其可為橡膠與不含橡膠之透明苯乙烯系樹脂之 混合物’或橡膠與苯乙稀系單體及其他可共聚合單體進行 接枝聚合而得者,前述橡膠乃例如··丁二烯、丁二烯-苯乙 稀漸增或亂排或嵌段共聚物等。就接枝聚合而得之橡膠改 質的透明苯乙烯系樹脂而言,其較佳的構成為:由橡膠狀 聚合物形成之橡膠粒子分散相(A),以及單體合計1〇〇重量 份由··苯乙烯系單體12〜70重量份、(甲基)丙烯酸醋系單體 20〜80重量份、丙烯腈系單體〇〜2〇重量份,以及其他可共 聚合單體0〜40重量份所組成之共聚物連續相(以所組成。 月’J述之橡膠狀聚合物較佳係由··苯乙烯系單體5〜5〇重 夏%,以及二烯系單體95〜5〇重量%所構成;上述橡膠狀共 聚物係在有機溶劑存在下,使用有機鋰化合物當作起始劑 ,並與苯乙烯系單體、:烯系單體,以及適量之溶劑進行 陰離子聚合反應而成之嵌段共聚物,上述共聚物之木 本紙張尺度適用中國國家標準(CNS) 第 頁 210X297 公釐) /ό Λ7 B7 五、發明説明(5 (Moony)黏度(MLi+4)為2〇〜8〇,25。〇之5重量%的苯乙烯單 體溶液的黏度為3〜60cps,而二烯系單元中之a乙烯基結 構佔8重里%以上,聚苯乙烯嵌段之含量佔橡膠狀共聚物的 5〜35重里%,上述橡膠狀共聚物的結構可為:全部為均聚 物嵌段(block)構造、部份亂排嵌段之構造、組成份漸增之 肷段(taper-block)構造、線性構造以及分歧構造等,其代表 性構造可為: 1、 線性嵌段共聚物: d)(A-B)n (2) A-f-B-A) n(3) n 上式中,A為以苯乙烯系為主成份之聚合體嵌段 ’ B為以二烯系為主成份之聚合體嵌段,a嵌段與b嵌 段之界限不一定需要明確的區分,n=1或1以上之整數 2 (請先閱讀背面之注意事項再填寫本頁} 經濟部中央標準局員工消費合作社印製 分歧狀嵌段共聚物: (2) [(A-B t~7i-m_2 X (3) [(B-Ai—to~~X (4) [(A-B于丁^十。x 上式中,A、B同第1項說明,X為偶合劑殘基 (例如:四氣化矽、四氯化錫等)、,或為多官能之有 機鋰化合物殘基,η及m為1~ 10之整數。 則述第1項及第2項之任意形式的混合物。 第 頁 線·! 本紙張尺度通州T國國冬標準(CNS ) A4規格( 210X 297 公釐) 五、發明説明(6 另 造,或者為丁 之具體例子有 D-D/S-S D-S-D/S-S D-S-D/S-S-D S-D-D/S-S D/S-S-D-S S-D/S-S (S-D/S)n ,組成份漸増之嵌段構造 歸新增式嵌段構造, 可為苯乙稀漸增式散段構 上述漸增式嵌段構造1. Line 1T !! Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs Λ7 —_____ B7 V. Description of the Invention (3)-Purchase 0% by weight and other copolymerizable monomers 0 ~ 70% by weight. The above other copolymerizable monomers are not particularly limited as long as they can be copolymerized with styrene monomer to achieve transparency. Specific examples of the copolymerizable monomer of the rubber-free transparent styrene-based resin of the present invention may be: (meth) acrylate-based monomer, acrylonitrile-based monomer, maleimide-based monomer, (methyl ) Acrylic, anhydrous maleic acid, and ethylene glycol methacrylate, where (meth) acrylate monomers can be: methyl acrylate, ethyl acrylate, butyl acrylate, methyl methacrylate, methyl Ethyl acrylate, propyl methacrylate, butyl methacrylate, benzyl methacrylate, hexyl methacrylate, cyclohexyl methacrylate, dodecyl methacrylate, methacrylic acid 2 -Hydroxyethyl ester, glycidyl methacrylate, and diamidoethyl methacrylate, etc. Among them, methyl methacrylate is preferred. The acrylonitrile-based monomer may be acrylonitrile or α-methacrylonitrile. Among them, acrylonitrile is preferred. The maleimide-based monomer may be selected from: N-methylmaleimide, N-isopropylmaleimide, N-butylmaleimide, N-hexylmaleimide Amine, N-octylmaleimide, N-dodecylmaleimide, N_cyclohexylmaleimide, N-phenylmaleimide, N-2,3- Tolyl maleimide, N-2,4-tolyl maleimide, N-2,3-ethylphenylmaleimide, Ν-2,4-ethylphenylmaleimide Amine, N-2,3-butylphenylmaleimide, N-2,4-butylphenylmaleimide, N-2,6-tolylmaleimide, N-2, 3-Gaphenylmaleimide, N-2,4-chlorophenylmaleimide, N-2,3-bromophenylmaleimide, N-2,4-benzyl Malay imine, etc. 'where' is Ν-the base _____ page 5 ____ This paper size applies Chinese National Standard (CNS) A4 specifications (210 × 297 mm) (Please read the precautions on the back before filling in this Page), 1T line ·! 506973 A7 5. Description of the invention (4) Maleimide is the best. Specific examples of rubber-free transparent styrene-based resins include polystyrene-based, styrene-acrylonitrile-based copolymers, styrene-based methacrylic acid, copolymers, and styrene-based substituted maleic acid. Imine-acrylonitrile-based copolymer, styrene-based substituted maleimide-based imide-based copolymer, styrene-based (meth) acrylate-N-substituted maleimide-based imine-based copolymer, styrene-based _ Ν-Substituted maleimide-propylene-based materials _ (meth) acrylic acid-based copolymers and other printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs (please read the precautions on the back before filling this page), 1T Another type of transparent styrene-based resin of the present invention: transparent styrene resin modified by rubber, preferably transparent styrene resin modified by dilute rubber. It can be a mixture of rubber and transparent styrene resin without rubber 'or obtained by graft polymerization of rubber with styrene-based monomers and other copolymerizable monomers. The aforementioned rubbers are, for example, butadiene , Butadiene-styrene dilute or random or block copolymers. The rubber-modified transparent styrene-based resin obtained by graft polymerization has a preferable structure: a rubber particle dispersed phase (A) formed of a rubber-like polymer, and a total of 100 parts by weight of monomers. From 12 to 70 parts by weight of styrene-based monomer, 20 to 80 parts by weight of (meth) acrylic acid-based monomer, 0 to 20 parts by weight of acrylonitrile-based monomer, and 0 to 0 of other copolymerizable monomers 40 parts by weight of the continuous phase of the copolymer (consisting of the composition. The rubber-like polymer described in 'J' is preferably composed of 5 to 50% by weight of a styrene-based monomer and 95% of a diene-based monomer. ~ 50% by weight; the above-mentioned rubbery copolymer is an organic lithium compound as an initiator in the presence of an organic solvent, and is anionic with a styrene-based monomer, an olefin-based monomer, and an appropriate amount of a solvent A block copolymer produced by polymerization. The woody paper size of the above copolymers is in accordance with Chinese National Standard (CNS) page 210X297 mm. / Ό Λ7 B7 V. Description of the invention (5 (Moony) viscosity (MLi + 4) Viscosity of 5% to 5% by weight of styrene monomer solution The degree is 3 to 60 cps, and the a vinyl structure in the diene unit accounts for more than 8% by weight, and the content of the polystyrene block accounts for 5 to 35% by weight of the rubber-like copolymer. The structure of the rubber-like copolymer may be The structures are all: homopolymer block structure, partially disordered block structure, taper-block structure with increasing composition, linear structure, and branch structure. The representative structure can be : 1. Linear block copolymer: d) (AB) n (2) AfBA) n (3) n In the above formula, A is a polymer block with styrene as the main component, and B is a diene. The polymer block as the main component, the boundary between the a block and the b block does not necessarily need to be clearly distinguished, n = 1 or an integer 2 or more (please read the precautions on the back before filling this page) Standard Bureau staff consumer cooperative prints branched block copolymers: (2) [(AB t ~ 7i-m_2 X (3) [(B-Ai—to ~~ X (4) [(AB 于 丁 ^ 十. x In the above formula, A and B are the same as described in item 1. X is a coupling agent residue (for example, silicon tetraoxide, tin tetrachloride, etc.), or a polyfunctional organolithium compound residue, η and m 1 to 10 Integer. The mixture of any form of item 1 and item 2 is described. Page line ·! This paper size Tongzhou T country winter standard (CNS) A4 specification (210X 297 mm) 5. Description of the invention (6 separately created , Or specific examples are DD / SS DSD / SS DSD / SSD SDD / SS D / SSDS SD / SS (SD / S) n. The gradually increasing block structure belongs to the newly added block structure, which can be Styrene-based gradual discrete block structure
(S-D/S)n-S D/S - (S-D/S)n X-[(S-D/S)n]m+1 X-[(D/S-S)n]m+1 X-[(S-D/S)n-S]m+1 X-[(D/S-S)n-D/S]mH D-D/S-S - S-D/S-D 經濟部中央標準局員工消費合作社印製 、其中’ S為聚苯乙烯系嵌段,D為聚二烯系嵌段,D/s 為苯乙烯系或-稀系成份含量漸增之苯乙烯-二烯系共聚嵌 段,X為多官能性起始劑基或多官能性偶合劑基,㈣為u 的整數,上述具體例子中乃以D-D/s_s或D_S_D/S_S、D_ D/S-S-S-D/S’較佳。就本發明而言,乃以漸增式喪段構 造較適合。 前述苯乙烯系單體可為:苯乙烯、α_曱基苯乙烯、對 •甲基苯乙烯、間-曱基苯乙烯、鄰-甲基苯乙烯、乙基苯乙 烯、2,4-二曱基苯乙烯、對-第三丁基苯乙烯、α_甲基_對_ 甲基苯乙烯、溴-苯乙烯、二溴-苯乙烯、2,4,6_三溴苯乙稀 等,上述苯乙烯系單體可單獨使用或數種合併使用。 而二烯系單體乃選自:1,3· 丁二烯、2-甲基_1,3_ 丁二 烯、2-甲基-1,3-異戊二烯、2,3-二-甲基—1,3-丁 二烯、1,3-異戊二稀、己二稀專’上述化合物可單獨使用一種或 第 頁 本紙張尺度適用中國國家標準(CNS ) Α4規格(210Χ 297公釐) (請先閲讀背面之注意事項再填寫本頁}(SD / S) nS D / S-(SD / S) n X-[(SD / S) n] m + 1 X-[(D / SS) n) m + 1 X-[(SD / S) nS] m + 1 X-[(D / SS) nD / S] mH DD / SS-SD / SD Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs, where 'S is a polystyrene block and D is a poly Diene block, D / s is a styrene-diene copolymer block with increasing styrene- or dilute component content, X is a polyfunctional initiator group or a polyfunctional coupling agent group, ㈣ Is an integer of u. In the above specific examples, DD / s_s or D_S_D / S_S and D_D / SSSD / S 'are preferred. For the purposes of the present invention, it is more appropriate to construct a progressive funnel. The aforementioned styrene-based monomer may be: styrene, α-fluorenylstyrene, p-methylstyrene, m-fluorenylstyrene, o-methylstyrene, ethylstyrene, 2,4-bis Fluorenylstyrene, p-third-butylstyrene, α-methyl_p-methylstyrene, bromo-styrene, dibromo-styrene, 2,4,6-tribromostyrene, etc. These styrene-based monomers may be used alone or in combination. The diene monomer is selected from: 1,3 · butadiene, 2-methyl_1,3-butadiene, 2-methyl-1,3-isoprene, 2,3-di- Methyl-1,3-butadiene, 1,3-isoprene, hexamethylene. 'The above compounds can be used alone or on the page. This paper applies the Chinese National Standard (CNS) A4 specification (210 × 297 mm) Li) (Please read the notes on the back before filling in this page}
506973 經濟部中央標準局員工消費合作社印製 A7 B7 五、發明説明(7 ) 兩種以上混合使用,其中,又以1,3-丁二烯或1,3-異戊二烯 為較佳。 前述橡膠狀共聚物所使用之有機鋰化合物觸媒為分子 中含有一個以上鋰原子之化合物,其可選自:乙基鋰、正_ 戊基鋰、異丙基鋰、正-丁基鋰、次級丁基鋰、己基鋰、環 己基鐘、苯基經、苯甲基链、萘基裡、第三-丁基鐘、三亞 甲基二鋰、四亞甲基二鋰、丁二烯雙鋰及異戊二烯雙鋰等 一種或兩種以上混合使用。 前述橡膠狀共聚物在聚合時之聚合速率、1,2-乙稀基 含量,以及二烯系單體與苯乙烯系單體的反應性比及亂排 化狀態,可由極性化合物或亂排(random)化劑來調整,上 述極性化合物或亂排化劑乃選自:醚類、胺類(amine)、硫 醚胺、烷基苯、磺(sulfon)酸類、烷基氧化物之鉀或鈉鹽。 另外,本發明之共聚物連續相(B)係由12〜70重量份之 苯乙烯系單體、20〜80重量份之(甲基)丙烯酸酯系單體、〇〜20 重量份之丙烯腈系單體,以及0〜40重量份之其他可共聚合 單體所形成,其中,苯乙烯系單體之具體例子如前述橡膠 共聚物之苯乙烯系單體,在此不再重覆列舉說明。 而前述(甲基)丙烯酸酯系單體乃包含:曱基丙烯酸酯 類以及丙烯酸酯類,其中,甲基丙烯酸酯類可例如:甲基 丙烯酸甲酯、甲基丙烯酸乙酯、甲基丙烯酸丁酯等,而丙 烯酸酯類乃例如:丙烯酸曱酯、丙烯酸乙酯、丙烯酸正丁 酯、丙烯酸2-甲基戊基酯、丙烯酸2-乙基戊基酯、丙烯酸 辛酯等’其中,又以曱基丙烯酸甲酯及丙烯酸甲酯為較佳 _ 第9頁 本紙張尺度適用中國國家標準(CNS ) A4規格(210X 297公釐) (請先閱讀背面之注意事項再填寫本頁} 、1· 髮·!506973 Printed by the Consumers' Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs A7 B7 V. Description of the Invention (7) Two or more types are used in combination, of which 1,3-butadiene or 1,3-isoprene is preferred. The organolithium compound catalyst used in the aforementioned rubbery copolymer is a compound containing more than one lithium atom in the molecule, and may be selected from the group consisting of ethyl lithium, n-pentyl lithium, isopropyl lithium, n-butyl lithium, Secondary butyl lithium, hexyl lithium, cyclohexyl clock, phenylene chain, benzyl chain, naphthyl, third-butyl clock, trimethylene dilithium, tetramethylene dilithium, butadiene bis One or two or more of lithium and isoprene dilithium are used in combination. The polymerization rate of the aforementioned rubbery copolymer during polymerization, the ethylene content, and the reactivity ratio and disordered state of the diene monomer and the styrene monomer may be polar compounds or disordered ( random) chemical agents to adjust, the above polar compounds or disordering agents are selected from the group consisting of ethers, amines, thioetheramines, alkylbenzenes, sulfon acids, and potassium or sodium alkyl oxides salt. In addition, the copolymer continuous phase (B) of the present invention is composed of 12 to 70 parts by weight of a styrene-based monomer, 20 to 80 parts by weight of a (meth) acrylate-based monomer, and 0 to 20 parts by weight of acrylonitrile. And other copolymerizable monomers of 0 to 40 parts by weight. Specific examples of the styrene-based monomers are the styrene-based monomers of the aforementioned rubber copolymers, and are not repeated here. . The (meth) acrylate-based monomer includes fluorenyl acrylates and acrylates, and the methacrylates may be, for example, methyl methacrylate, ethyl methacrylate, or butyl methacrylate. Acrylates, etc., and acrylates are, for example: ethyl acrylate, ethyl acrylate, n-butyl acrylate, 2-methylpentyl acrylate, 2-ethylpentyl acrylate, octyl acrylate, etc. Phenyl methyl acrylate and methyl acrylate are better _ page 9 This paper size is applicable to China National Standard (CNS) A4 (210X 297 mm) (Please read the precautions on the back before filling out this page} 、 1 · hair·!
五、發明説明(8 ) 一~一…·———~一一一 — 經濟部中央標準局員工消費合作社印製 。而本發明之丙烯腈系單體可為:丙烯腈、α _甲基丙烯腈 等。 本發明共聚物連續相(Β)之可共聚合單體為〇〜40重量份 ’其單體種類並無特別限制,可依需要調整各共聚合單體 之含量比例、屈折率,使最後之樹脂組成物達成透明為必 要,上述可共聚合單體之具體例有:衣康酸、馬來酸、富 馬酸、丁烯酸、肉桂酸等之不飽和脂肪酸;Ν—甲基馬來醯 亞胺、Ν-乙基馬來醯亞胺、丁基馬來醯亞胺、Ν_辛基馬 來酿亞胺、Ν-異丙基馬來醯亞胺、Ν_苯基馬來醯亞胺、Ν_ 對-溴-苯基馬來醯亞胺、泳鄰—氣-苯基馬來醯亞胺、…環 己烷基馬來醯亞胺等之馬來醯亞胺類;馬來酸酐、衣康酸 酐、擰康酸酐之不飽和羧酸酐類;烯丙基胺、(甲基)丙婦 酸胺基乙酯、(甲基)丙烯酸胺基丙酯等含胺基之不飽和化 合物類,丙烯酿胺、Ν-甲基丙烯醯胺等之丙婦醯胺系化合 物。 本發明之樹脂組成物中共聚物連續相(Β)的重量平均分 子量並無特別的限制,一般為5〇,〇〇〇〜300,000,較佳為 60,000〜200,0〇〇,更佳為7〇,〇〇〇〜15〇,〇〇〇,當重量平均分子 ΐ低於50,000時,樹脂組成物之耐衝擊強度差,而當重量 平均分子量兩於300,000時,樹脂組成物的流動性會下降, 加工性差且透明性差;另外,本發明樹脂組成物之橡膠粒 子的重量平均粒徑亦無特別限制,一般在〇1~2 〇 # m,較 佳為0.1〜1.5//m’更佳為0.2〜l.〇//m,當橡膠粒子之重量平 均粒徑小於0.1/zm時,樹脂組成物之衝擊強度下降,若重 ________第 10 頁 本紙張尺度適用中國國家標準(CNS ) A4規格(210xT^f ) _--〜一 (請先閱讀背面之注意事項再填寫本頁)V. Description of the invention (8) One ~ one ... · ———— ~ One one one — Printed by the Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs. The acrylonitrile monomer of the present invention may be acrylonitrile, α-methacrylonitrile, or the like. The copolymerizable monomer in the continuous phase (B) of the copolymer of the present invention is 0 to 40 parts by weight. There is no particular limitation on the type of the monomer. The content ratio and inflection ratio of each copolymerizable monomer can be adjusted as needed to make the final It is necessary for the resin composition to achieve transparency. Specific examples of the above copolymerizable monomers include unsaturated fatty acids such as itaconic acid, maleic acid, fumaric acid, butenoic acid, and cinnamic acid; N-methyl maleic acid Imine, Ν-ethylmaleimide, butylmaleimide, N_octylmaleimide, Ν-isopropylmaleimide, Ν_phenylmaleimide Amines, N-p-bromo-phenylmaleimide, swimming o-gas-phenylmaleimide, ... cyclohexylmaleimide and other maleimides; maleic anhydride Unsaturated carboxylic acid anhydrides such as itaconic anhydride, scorconic anhydride; allylamines, (meth) aminoethyl ethyl methionate, aminopropyl (meth) acrylate and other unsaturated compounds , Propofolamine compounds such as acrylamine and N-methacrylamide. The weight average molecular weight of the copolymer continuous phase (B) in the resin composition of the present invention is not particularly limited, but is generally 50,000 to 300,000, preferably 60,000 to 200,000, and more preferably 7 〇〇〇〇〇〇〜10000〇, when the weight average molecular weight ΐ is less than 50,000, the impact strength of the resin composition is poor, and when the weight average molecular weight is less than 300,000, the fluidity of the resin composition will decrease Poor processability and poor transparency; In addition, the weight average particle diameter of the rubber particles of the resin composition of the present invention is also not particularly limited, and is generally 〇1 ~ 2〇 # m, preferably 0.1 ~ 1.5 // m ', more preferably 0.2 ~ l.〇 // m, when the weight average particle diameter of the rubber particles is less than 0.1 / zm, the impact strength of the resin composition decreases. If the weight is ________ page 10, the Chinese paper standard (CNS) A4 applies Specifications (210xT ^ f) _-- ~ 1 (Please read the precautions on the back before filling this page)
五、發明説明(9 ) ~~—~ ^ ϊ平均粒徑大於2.〇em,則樹脂組成物之透明性差。上述 橡膠粒子的重量平均粒徑乃以透過型電子顯微鏡之超薄切 片法所得之照片’此照片中最少3〇〇個粒子以上,並以 下式测得重量平均粒徑。5. Description of the invention (9) ~~-~ ^ ϊ If the average particle diameter is greater than 2.0em, the transparency of the resin composition is poor. The weight-average particle diameter of the rubber particles is a photograph obtained by an ultra-thin sectioning method of a transmission electron microscope. The photograph has a minimum of 300 particles or more, and the weight-average particle diameter is measured by the following formula.
EniD i4 重量平均粒徑=--EniD i4 weight average particle size =-
EniD i3 上式中ni為粒徑Di之橡膠粒子的個數。 本發明樹脂組成物中的凝膠含量,亦即甲苯/丙酮(重 里比1/1)之不溶份含量並無特別限制,一般為〕〜⑽重量% ,較佳為8〜35重量%,更佳為12〜3〇重量%。另外,本發明 之樹脂組成物中之膨潤指數並無特別限制,一般為2〜25, 較佳為3〜20,更佳為5〜15。 經濟部中央標準局員工消費合作社印製 本發明透明之苯乙烯系樹脂的二氯甲烷可溶份中,分 子量小於350低分子量聚合物佔全部可溶份的2〇重量%以 下,杈佳為1.0重量%以下,更佳為06重量%以下;當分子 里小於350之低分子量聚合物的含量大於2 〇重量%時,苯 乙烯系樹脂加工成型時容易產生模具污染的現象,並造成 產。口的瑕疵,此所謂苯乙烯系樹脂之二氯曱烷可溶份分子 量:於350之低分子量聚合物’乃指將苯乙烯系樹脂加入 二氯甲:¾之溶劑中’ #其中可溶解之部份(可溶份WGC-mass(氣相層析儀_質譜儀)測定其中分子量低於35〇以下之 低子量聚合物含量(以苯乙烯標準面積換算)。 本發明透明苯乙烯系樹脂組成物中所含之季戊四 本紙張尺錢财目 506973 Λ7 B7 五、發明説明(10 ) 經濟部中央標準局員工消費合作社印製 (請先閱讀背面之注意事項再填寫本頁) 酯類化合物為季戊四醇與羧酸化合物反應而成的酯類化合 物,其中,羧酸化合物可為:月桂酸(又稱十二烷酸,lauric acid)、棕摘酸(又稱十六烧酸,palmitic acid)、硬脂酸(又 稱十八烧酸,stearic acid)、花生四稀酸(arachidonic acid) 、山奋酸(又稱二十二烧酸,behenic acid)、木脂酸(lignoceric acid)、蟲躐酸(又稱二十七烧酸,cerotic acid)、褐煤酸(又稱 二十九烧酸,montanic acid)、油酸(又稱十八稀酸,oleic acid) 、反油酸(elaidic acid)、芥子酸(erucic acid)、亞麻仁油酸 (linoleic acid)、次亞麻仁油酸(linolenic acid)、草酸(又稱 乙二酸,oxalic acid)、丙二酸(malonic acid)、丁二酸(succinic acid)、戊二酸(glutaric acid)、己二酸(adipic acid)、庚二酸 (pimelic acid)、辛二酸(suberic acid)、壬二酸(azelaic acid) 、癸二酸(sebacic acid)、壬烧二魏酸(nonane dicarboxylic acid)、癸烧二叛酸(decane dicarboxylic acid)、十一烧二酸 (undecane dicarboxylic acid)、十四院雙酸(dodecane dicarboxylic acid)、二十二烧二酸(eicosane dicarboxylic acid)、順丁烯二酸(maleic acid)、反丁 婦二酸(fumaric acid) 、順丁 嫦二酸(citraconic acid)、甲基反丁 嫦二酸(mesaconic acid)、次甲基 丁二婦(itconic acid)、環丙烧叛酸(eyeloproane dicarboxylic acid)、環丁烧羧酸(cyclobutane dicarboxylic acid)、環十五烧魏酸(cyclopentadiane dicarboxylic acid)、 樟腦酸(camphor acid)、六氫鄰苯甲酸(hexahydrophthalic acid)、苯二曱酸(phthalic acid)、四苯二甲酸(terephthalic acid)、異苯二甲酸(isophthalic acid)、萘二甲酸(naphthalic ___第12頁 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 506973 Λ7 B? 五、發明説明(11 ) acid)、二苯基二叛酸(diphenyl_o,o’-dicarboxyl acid) 等。 而本發明透明苯乙烯系樹脂組成物之季戊四醇的酯類 化合物具體的例子有:季戊四醇三硬脂酸酯(pentaerythritol tristearate)、季戊四醇己二醯硬脂酸酯(pentaerythritol adipate stearate)、季戊四醇丁 二醯硬脂酸酯(pentaerythritol succinate stearate)、季戊四醇四硬脂酸醋(pentaerythritol tetrastearate),以及季戊四醇四月桂酸ϊ旨(pentaerythritol tetralaurate),其中,以季戊四醇四硬脂酸醋為較佳;上述 季戊四醇之酯類化合物的製造,可依據酯化反應程序,特 別可使用酯化程序之觸媒,例如:有機錫化合物,而反應 中醇類及羧酸化合物的使用量,依不同的種類及化學計量 而定。 本發明季戊四醇的酯類化合物之添加量乃相對於1〇〇 重量份透明苯乙烯系樹脂的0.01〜5重量份,較佳為0.02〜3 重量份,更佳為0.05〜1.5重量份,當添加量小於0.01重量份 時,苯乙稀系樹脂之成型加工性差,離模性差,而當添加 量大於5重量份時,容易產生模具污染,樹脂組成物之耐 熱性及透明性皆變差。 經濟部中央標準局員工消費合作社印製 (請先閲讀背面之注意事項再填寫本頁) 本發明之季戊四醇的酯類化合物添加方式並無特別的 限制,其可於苯乙烯系樹脂聚合時加入,或於聚合後加入 ,或以押出機或靜力混合器方式加入。 本發明透明苯乙烯系樹脂之製法可為乳化、懸濁、塊 狀(或溶液)聚合法,或者以上數種之組合的聚合法,較佳 ___第 13 頁_________ 本紙張尺度適用中國國家標準(CNS ) A4規格(210X 297公釐) A1 B? 五、發明説明(12 溶液聚合法 為乳化或塊狀(或溶液)聚合法,更佳為塊狀或 本發明經橡膠改質之透明苯乙稀系樹脂的製造方法之 一 ’乃在橡膠狀共聚物存在下,與苯乙烯系單體、(甲基 丙烯酸系早體'丙烯腈系單體及必要時添加其他可並聚a 單體進行批式或連料塊狀或溶賴«合反應;若以^ 縯式溶«合為例,首先將上述之橡膠狀共聚物及單體加 入適當的溶Μ成原料混合溶液,前述原料混合溶液可以 在傳統具有高剪應力、高㈣速度的溶解槽巾進行溶解, ^冷解&可使用·具有帶狀螺旋式擾拌葉、螺旋漿式擾掉 葉、或者其他可產生高剪應力之攪拌葉等,在足夠的時間 下’可以將上述橡膠狀共聚物完全溶解成橡膠溶液的狀能 ^方便泵浦輸送至反應器的作業進行;將前述原料料 或單體溶液分別連續的餵人第—反應器及/或第二反應器、 及/或其後續之反應器中,並配合需要在第一及/或第二及/ 或其後續之反應器添加鏈移轉劑、起始劑下進行接枝聚合 反應。 經濟部中央標準局員工消費合作社印製 上述反應槽可為連續攪拌式反應槽(CSTR),或栓塞流 式反應槽(Plug fl〇w reactor),或靜力混合式⑻吣幻反應器 之同一種或不同種類之組合;其反應溫度控制在7〇〜23〇它 ,最終單體轉化率可達30〜95%,但以50〜90%為較佳。 本發明透明苯乙烯系樹脂在聚合時,可使用的溶劑種 類有·芳香族碳氫化合物、酮類、酯類,其中,最好的芳 香族碳氫化合物乃例如··甲苯、乙苯及二曱苯,而酮類最 —-------第 14 頁 本紙張尺度適用中國國家標準(CNS) A4規格(21〇X 297公釐) 506973 Λ 7 B? 五、發明説明(13 ) 好的是丁酮,酯類則以醋酸乙酯為佳;此外,本發明亦可 使用正-乙烧、環己烧、正-庚烧等脂肪族碳氫化合物為溶 劑的一部份。 經濟部中央標準局員工消費合作社印製 (請先閱讀背面之注意事項再填寫本頁) 本發明透明苯乙烯系樹脂組成物在製造中,可使用之 起始劑有:過氧化二苯甲醯(benzoyl peroxide)、過氧化二 異丙基苯(dicumyl peroxide)、超過氧化二苯甲醯(di benzoyl superoxide)、過氧化第三丁基(t-butyl peroxide)、過氧化氫 第三丁基(t-butyl hydroxy peroxide)、過氧化氫異丙基苯 (cumene hydroperoxide)、過氧化第三丁基苯甲酸酉旨(t-butyl peroxy benzoate)、二-2-過氧化乙己基二碳酸酉旨(di-2_ ethylhexyl peroxy dicarbonate)過氧化第三丁基異丙基碳酸 S旨(tert,butyl peroxy isopropyl carbonate,簡稱BPIC)、過氧 化環己酬1 (cycolhexanoe peroxide) 、2,2’-偶氣-雙-異丁腈 (2,2’-azo-bis-isobutyronitrile)、1,1’-偶氮-雙-1-環己烧魏腈 (1,15-azo-bis-1-cyclohexane carbonitrile) 、2,2’-偶氮-雙-2-甲基丁腈(2,2’-azo-bis-2-methyl butyronitrile)、偶氮-雙-異 丁腈(&2〇-1)丨8-丨8〇13111)^011池丨16)、1,1-二過氧化第三丁基環己 烧(l,l-di-t-butyl peroxy cyclohexane,簡稱TX-22)、1,1-二 -過氧化第三丁基-3,3,5-三甲基環己烷 (l,l-di-t-butylperoxy-3,3,5-trimethyl cyclohexane,簡稱TX-29A)、2,5-二甲基-2,5-雙-(2-乙基過氧化己醯)己烷[2,5-dimethyl-2,5-bis-(2-ethylhexanoxy peroxy)hexane]、4-(過氧第三丁 基罗炭 基)-3-己基-6-[7-(過氧化第三丁基羰基)庚基]環己烷{4-( t-butyl peroxy carbonyl)-3-hexyl-6-[7-( t-butyl peroxy _ 第15頁 本紙張尺度適用中國國家標準(CNS ) A4規格(210X 297公釐) 506973 Λ7 B7 五、發明説明丨4 ) carbonyl)heptyl]cyclohexane}、二-第三丁基二過氧化壬二 酸(di-t-butyl-diperoxyazelate)、2,5-二甲基-2,5-雙(過氧化 苯甲醯)-己烧[2,5-dimethyl-2,5-bis-(benzoyl peroxy)hexane] 、二-過氧化第三丁基-六氫-對苯二酸酯(di-t-butyl peroxy-1^又211}^(11*〇-16代0]11:1^1316,簡稱8?11丁?)、2,2-雙(4,4-二-過氧 化第三丁基)環己基丙烷[2,2-bis-(4,4-di-t-butyl peroxy)cyclohexanyl propane]等 ° 本發明透明苯乙烯系樹脂組成物在製造中,可使用之 鏈移轉劑乃例如: 1) 硫醇(mercaptan)類:甲基硫醇、正-丁基硫醇、環己基硫 醇、正-十二烧基硫醇、硬脂醯基硫醇(stearyl mercaptan) 、第三-十二烧基硫醇(t-dodeyl mercaptan,簡稱TDM)、 正-丙基硫醇、正·辛基硫醇、第三-辛基硫醇、第三-壬基 硫醇等。 2) 烷胺(alkyl amines)類:單乙基胺、二乙基胺、三乙基胺 、單異丙基胺、二單丙基胺、單丁基胺、二-正丁基胺、 三-正丁基胺等。 經濟部中央標準局員工消費合作社印製 (請先閲讀背面之注意事項再填寫本頁) 其他例如:五苯基乙烷(pentaphenylethane)、α -曱基 苯乙稀二聚物(a -methyl styrene dimer)、萜基稀 (terpinolene) 〇 前述聚合反應之後,從反應器中取出經脫揮發裝置, 將未反應的單體、溶劑等低揮發份脫除,經聚合物回收之 後,即可製得透明苯乙烯系樹脂。 本發明之季戊四醇的酯類化合物亦可在苯乙烯系樹脂 __ 第16頁 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) ΑΊ --s-~~s_______ 五、發明説明(15) …——— ----------- 聚合完成後,與苯乙稀系樹脂—起混練,藉由布拉本德塑 性儀、班伯立混練機、捏合·混合機、滾塵機,以及一轴或 二輛押出機等之-般混合混練機混合·混練製得。通常藉這 些押出機等混合·混練後,再將押製出的押出物加以冷卻、EniD i3 In the above formula, ni is the number of rubber particles with a particle size Di. The gel content in the resin composition of the present invention, that is, the content of insolubles in toluene / acetone (weight ratio 1/1) is not particularly limited, and is generally [] to ⑽wt%, preferably 8 to 35wt%, more It is preferably 12 to 30% by weight. In addition, the swelling index in the resin composition of the present invention is not particularly limited, but is generally 2 to 25, preferably 3 to 20, and more preferably 5 to 15. Among the methylene chloride solubles of the transparent styrene resin printed by the employee's cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs, the low molecular weight polymer with a molecular weight of less than 350 accounts for less than 20% by weight of the total solubles, preferably 1.0 When the content of the low-molecular-weight polymer less than 350 in the molecule is more than 20% by weight, the phenomenon of mold contamination is likely to occur during processing and molding of the styrene-based resin, and production may occur. Mouth defects, the so-called dichloromethane-soluble molecular weight of the styrenic resin: low molecular weight polymer at 350 'refers to the addition of styrenic resin to the solvent of chloroform: ¾ Part (soluble fraction WGC-mass (gas chromatograph_mass spectrometer) measures the content of low-molecular-weight polymers with a molecular weight of less than 350 (in terms of styrene standard area). The transparent styrene resin of the present invention Four pentagrams of paper contained in the composition, paper rule, money account 506973 Λ7 B7 V. Description of the invention (10) Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs (please read the precautions on the back before filling this page) Ester The compound is an ester compound formed by the reaction of pentaerythritol with a carboxylic acid compound. Among them, the carboxylic acid compound can be: lauric acid (also known as lauryl acid), palmitic acid (also known as palmitic acid) ), Stearic acid (also known as steric acid), arachidonic acid, behenic acid (also known as behenic acid), lignoceric acid, Insecticidal acid Cerotic acid), montanic acid (also known as montanic acid), oleic acid (also known as oleic acid), elaidic acid, erucic acid, flax Linoleic acid, linolenic acid, linolenic acid, oxalic acid (also known as oxalic acid), malonic acid, succinic acid, glutaric acid ( glutaric acid), adipic acid, pimelic acid, suberic acid, azelic acid, sebacic acid, azelaic acid ( nonane dicarboxylic acid), decane dicarboxylic acid, undecane dicarboxylic acid, dodecane dicarboxylic acid, eicosane dicarboxylic acid, Maleic acid, fumaric acid, citraconic acid, mesaconic acid, itconic acid), eyeloproane dicarboxylic acid, cyclobutane Carboxylic acid (cyclobutane dicarboxylic acid), cyclopentadiane dicarboxylic acid, camphor acid, hexahydrophthalic acid, phthalic acid, tetraphthalic acid (Terephthalic acid), isophthalic acid, naphthalic acid ___ page 12 This paper size applies Chinese National Standard (CNS) A4 specification (210X297 mm) 506973 Λ7 B? 5. Description of the invention ( 11) acid), diphenyl_o, o'-dicarboxyl acid, and the like. Specific examples of the pentaerythritol ester compounds of the transparent styrene resin composition of the present invention include pentaerythritol tristearate, pentaerythritol adipate stearate, and pentaerythritol adipate stearate. Pentaerythritol succinate stearate, pentaerythritol tetrastearate, and pentaerythritol tetralaurate. Among them, pentaerythritol tetrastearate is preferred; the above-mentioned pentaerythritol ester The production of similar compounds can be based on the esterification reaction procedure, especially the catalysts of the esterification procedure, such as organic tin compounds, and the amount of alcohols and carboxylic acid compounds used in the reaction depends on the type and stoichiometry. . The addition amount of the pentaerythritol ester compound of the present invention is 0.01 to 5 parts by weight, preferably 0.02 to 3 parts by weight, and more preferably 0.05 to 1.5 parts by weight relative to 100 parts by weight of the transparent styrene resin. When the amount is less than 0.01 part by weight, the molding processability of the styrene resin is poor, and the mold release property is poor. When the amount is more than 5 parts by weight, mold contamination is liable to occur, and the heat resistance and transparency of the resin composition are deteriorated. Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs (please read the precautions on the back before filling this page) The pentaerythritol ester compound addition method of the present invention is not particularly limited, and it can be added when the styrene resin is polymerized. Or add it after polymerization, or add it by extruder or static mixer. The production method of the transparent styrene resin of the present invention may be an emulsification, suspension, block (or solution) polymerization method, or a combination of the above several polymerization methods, preferably ___ page 13 _________ This paper size is applicable to China National Standard (CNS) A4 specification (210X 297 mm) A1 B? V. Description of the invention (12 Solution polymerization method is emulsification or block (or solution) polymerization method, more preferably block or the rubber modified by the present invention One of the manufacturing methods of transparent styrene resin is to combine with styrene-based monomer, (methacrylic-based early body, acrylonitrile-based monomer, and other polymerizable polymers if necessary). The monomers are subjected to batch or continuous block or dissolving reactions; if the dissolving reaction is taken as an example, the above rubbery copolymer and monomers are first added to an appropriate solvent to form a raw material mixed solution. The raw material mixed solution can be dissolved in traditional dissolving towels with high shear stress and high velocity. ^ Cryolysis & can be used. It has ribbon-shaped spiral scrambled leaves, spiral pulp scrambled leaves, or other Shear stress of stirring blades, etc., in sufficient In between, the above-mentioned rubber-like copolymer can be completely dissolved into a rubber solution. It can be easily pumped to the reactor for operation; the aforementioned raw material or monomer solution is continuously fed to the first reactor and / or In the second reactor and / or a subsequent reactor, a graft polymerization reaction is performed under the condition that a chain transfer agent and an initiator are added to the first and / or second and / or subsequent reactors. The above-mentioned reaction tank printed by the Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs may be a continuous stirring type reaction tank (CSTR), a plug flow type reaction tank (Plug Flow reactor), or the same as a static mixing type magic reactor. One or a combination of different types; the reaction temperature is controlled between 70 and 23, and the final monomer conversion rate can reach 30 to 95%, but preferably 50 to 90%. The transparent styrene resin of the present invention is polymerized during polymerization. At this time, the types of solvents that can be used are aromatic hydrocarbons, ketones, and esters. Among them, the best aromatic hydrocarbons are, for example, toluene, ethylbenzene, and xylene, and ketones are the most --- ------ Page 14 This paper is applicable National Standard (CNS) A4 specification (21 × X 297 mm) 506973 Λ 7 B? 5. Description of the invention (13) The best is methyl ethyl ketone, and the best ester is ethyl acetate; In addition, the invention can also be used Aliphatic hydrocarbons such as n-ethane, cyclohexane, and n-heptane are part of the solvent. Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs (please read the precautions on the back before filling this page). In the production of the transparent styrenic resin composition of the present invention, the usable initiators include: benzoyl peroxide, dicumyl peroxide, and dibenzoyl peroxide ( di benzoyl superoxide), t-butyl peroxide, t-butyl hydroxy peroxide, cumene hydroperoxide, third butyl peroxide T-butyl peroxy benzoate, di-2_ ethylhexyl peroxy dicarbonate, tert, butyl peroxy isopropyl carbonate (BPIC), peroxide Cyclohexanoe peroxide, 2,2'-azo-bis-isobutyronitrile, 1,1'-azo-bis-1-cyclohexane Weinnitrile (1,15-azo-bis-1-cyclohexane carbonitrile), 2,2'-azo-bis-2-methylbutyronitrile (2,2'-azo-bis-2-methyl butyronitrile), even Nitro-bis-isobutyronitrile (& 2〇-1) 丨 8- 丨 8〇13111) ^ 011 pool 丨 16), 1,1-diperoxy third butyl cyclohexane (l, l-di -t-butyl peroxy cyclohexane (TX-22 for short), 1,1-di-peroxy third butyl-3,3,5-trimethylcyclohexane (l, l-di-t-butylperoxy-3 , 3,5-trimethyl cyclohexane (referred to as TX-29A), 2,5-dimethyl-2,5-bis- (2-ethylperoxyhexyl) hexane [2,5-dimethyl-2,5 -bis- (2-ethylhexanoxy peroxy) hexane], 4- (peroxy third butylcarbyl) -3-hexyl-6- [7- (third butylcarbonyl) heptyl] cyclohexane {4- (t-butyl peroxy carbonyl) -3-hexyl-6- [7- (t-butyl peroxy _ page 15) This paper size applies to Chinese National Standard (CNS) A4 specification (210X 297 mm) 506973 Λ7 B7 V. Description of the invention 丨 4) carbonyl) heptyl] cyclohexane}, di-third butyl Di-t-butyl-diperoxyazelate, 2,5-dimethyl-2,5-bis (benzidine peroxide) -hexane [2,5-dimethyl-2,5-bis -(benzoyl peroxy) hexane], di-t-butyl peroxy-1 ^ and 211} ^ (11 * 〇-16 代 0) 11: 1 ^ 1316, referred to as 8? 11 Ding? ), 2,2-bis (4,4-di-t-butylperoxy) cyclohexylpropane [2,2-bis- (4,4-di-t-butyl peroxy) cyclohexanyl propane], etc. The present invention In the production of transparent styrenic resin compositions, the chain transfer agents that can be used are, for example: 1) Mercaptans: methyl mercaptan, n-butyl mercaptan, cyclohexyl mercaptan, n-deca Dialkyl mercaptan, stearyl mercaptan, t-dodeyl mercaptan (TDM), n-propyl mercaptan, n-octyl mercaptan, Third-octyl mercaptan, third-nonyl mercaptan, and the like. 2) Alkylamines: monoethylamine, diethylamine, triethylamine, monoisopropylamine, dimonopropylamine, monobutylamine, di-n-butylamine, triamine -N-butylamine and the like. Printed by the Consumer Cooperatives of the Central Bureau of Standards of the Ministry of Economic Affairs (please read the notes on the back before filling this page) Others such as: pentaphenylethane, α-methyl styrene dimer (a-methyl styrene dimer), terpinolene 〇 After the aforementioned polymerization reaction, take out from the reactor through a devolatilization device, remove unreacted monomers, solvents and other low-volatile components, and after polymer recovery, it can be obtained Transparent styrene resin. The ester compounds of pentaerythritol of the present invention can also be used in styrene resins. __Page 16 This paper size applies Chinese National Standard (CNS) A4 specifications (210X297 mm) ΑΊ --s- ~~ s _______ V. Description of the invention ( 15)… ———— ----------- After the polymerization is completed, it is mixed with styrene resin and mixed with a Brabender plastic meter, a Banbury mixer, a kneading and mixing machine, It is made by mixing and kneading with a general dust kneading machine such as a roller duster and a shaft or two extruder. Usually, these extruder machines are used for mixing and kneading, and then the extruded objects are cooled,
造粒,上述混練一般係於16〇〜28(Γ(:下進行,而以18〇〜MO C之溫度為佳,前述混合·混練之各調配成份的順序並無特 別的限制。 在不顯著損及本發明樹脂組成物之效果的範圍内,可 凋配其他成份,此等其他成份乃例如··著色劑、填充劑、 難燃劑、難燃助劑(三氧化銻等)、光安定劑、熱安定劑、 可塑劑、滑劑、離型劑、增黏劑、帶電防止劑、氧化防止 劑、導電劑等之添加劑;上述添加劑可例如:礦物油、例 如:硬脂酸丁酯之酯系可塑劑、聚酯系可塑劑、例如聚二 甲基矽氧烷之有機聚矽氧烷、高級脂肪酸及其金屬鹽、位 阻胺系抗氧化劑、玻璃纖維等,其可單獨使用或混合使用 ’上述酯系可塑劑或礦物油的使用量乃基於1〇〇重量份樹 月曰組成物一般在〇〜5重量%,較佳為〇.〇5〜2重量%,而有機 聚矽氧烷之使用量一般在〇〜〇·5重量%,較佳為〇〇〇2〜〇2重 經濟部中央標準局員工消費合作社印製 量% 〇 [物性測試] 一、 透明性(霧度,Haze) ·•將樹脂組成物射出成型3mm厚之 試片,並依ASTM D-1003標準測定透明性,當Haze值 越高表示透明性越差。 二、 穿透率(Transmittance):依ASTM-1003規定測試厚度 ____% 17 頁 本紙張尺度適用中國國家標準(CNS ) A4規格(210x7^釐)— 經濟部中央標準局員工消費合作社印製 506973 Λ7 B7 五、發明説明(l6 ) 3mm試片,單位以%表示。 三、 加工性(Spiral flow):透明苯乙稀系樹脂組成物在東 芝ISIOOEN射出成形機中,於汽缸溫度220°C模具溫度 60°C、射出壓力600kg/cm2,使用旋流模具(2mmt)成形 之,並以流動長度評估其流動性。 四、 熔融指數(Melt index,MI):係以ASTM D-1238法測 試而得。 五、 加工成型模具污染:在280°C下連續成型50模後,觀 察污染物對成型品的影響。 ◎:表示模具沒有污染。 △:表示模具稍有污染。 X :表示模具污染嚴重。 六、 苯乙烯系樹脂之二氯甲烷可溶份分子量小於350之低 分子量聚合物含量(重量%)之測法:將苯乙烯系樹脂組 成物,以二氯甲烷溶劑溶解後,經遠心離心機分離, 取上層可溶份以氣相層析儀-質譜儀(GC-MASS)分析, 當氣相層析儀上以質譜儀定位分子量低於350以下之低 分子量聚合物例如:三聚物或二聚物,並以苯乙烯標 準面積換算;上述低分子量聚合物乃例如:AMS、MMS 、AS、MSS、SSS、MS等,其中A為丙烯腈單體,Μ 為(甲基)丙烯酸甲酯單體,S為苯乙烯單體,而氣相分 析儀為Hewlett Packard公司編號5890Α。 [實施例] 丨實施 __第 18 頁____ 本紙張尺度適用中國國家標準(CNS ) Α4規格(210X 297公釐) (請先閱讀背面之注意事項再填寫本頁) 、11 線‘ 經濟部中央標準局員工消費合作社印製 506973 Λ7 B7 五、發明説明(Π ) 使用容量為40公升之完全混合型反應槽四個串聯所構 成之連續聚合裝置來製造透明本乙細系樹脂組成物,將橡 膠狀共聚物8.4重量份(苯乙烯/丁二烯含量=25/75重量%, 1,2-乙烯基含量=15.4%, Mooney黏度45之漸增嵌段共聚 物),與苯乙烯23.4重量份、曱基丙烯酸甲酯38.2重量份、 乙苯30重量份、十二烧基硫醇0·08重量份、季戊四醇四硬 脂酸酯0.045重量份,以及過氧化二苯甲醯〇·〇8重量份形成 進料溶液,使用幫浦以35kg/hr之流量連續地供給至反應槽 中進行聚合,第一反應槽的溫度為109°C,第二反應槽的溫 度為114°C,第三反應槽的溫度為130°C,第四反應槽的溫 度為140°C,總聚合轉化率在60%。聚合後由反應槽經聚合 溶液連續供給至脫揮發裝置,控制其脫揮發的真空度在2〇〇 Torr,將未反應單體及有機溶劑等之揮發性物質分離,而 後經由擠壓機將樹脂丸粒化。 其組成之連續相中含有苯乙烯構造單體36重量份、甲 基丙烯酸甲酯64重量份,透明苯乙烯系樹脂組成物之季戊 四醇四硬脂酸酯含量為0.1重量份(基於1〇〇重量份之透明苯 乙烯系樹脂),分散相橡膠粒子之重量平均粒徑為〇.42μιη, 二氯曱烧可溶份中分子量低於350之低分子量聚合物含量 佔全部可溶份的0.62重量%。 |實施例2丨 使用容置為40公升之完全混合型反應槽四個串聯所構 成之連續聚合裝置來製造透明笨乙烯系樹脂組成物,將橡 膠狀共聚物8.4重量份(苯乙稀/ 丁二稀含量=25/75重量%, ______第 19 頁 ^紙張尺度適用中國國家標準(CNS ) Α4規格(21〇 ---- (請先閱讀背面之注意事項再填寫本頁) 、1Τ 線· 經濟部中央標準局員工消費合作社印製 506973 A7 _____ B7 五、發明説明(18 ) 1,2-乙烯基含量=15.4%, Mooney黏度45之漸增嵌段共聚 物),與笨乙烯23.4重量份、甲基丙烯酸甲酯38 2重量份、 乙苯30重量份、十二烷基硫醇〇.09重量份、季戊四醇四硬 脂酸酯0.14重量份,以及過氧化二苯甲醯〇〇9重量份形成 進料溶液,使用幫浦以35kg/hr之流量連續地供給至反應槽 中進行聚合,第一反應槽的溫度為丄们它,第二反應槽的溫 度為107°C,第三反應槽的溫度為122它,第四反應槽的溫 度為132 C,總聚合轉化率在60%。聚合後由反應槽經聚合 溶液連續供給至脫揮發裝置,控制其脫揮發的真空度在13〇 Torr,將未反應單體及有機溶劑等之揮發性物質分離,而 後經由擠壓機將樹脂丸粒化。 其組成之連續相中含有苯乙烯構造單體36重量份、甲 基丙烯酸甲酯64重量份,透明苯乙烯系樹脂組成物之季戊 四醇四硬脂酸酯含量為〇·3重量份(基於1〇〇重量份之透明苯 乙稀糸樹脂),分散相橡膠粒子之重量平均粒徑為0.41 , 二氯甲烷可溶份中分子量低於35〇之低分子量聚合物含量 佔全部可溶份的0.43重量%。 束施例3| 使用容量為40公升之完全混合型反應槽四個串聯所構 成之連續聚合裝置來製造透明苯乙烯系樹脂組成物,將橡 膠狀共聚物8.4重量份(苯乙烯/丁二烯含量=25/75重量%, 1,2-乙烯基含量==15.4%, Mooney黏度45之漸增嵌段共聚 物),與苯乙烯22.8重量份、甲基丙烯酸甲酯37.0重量份、 丙烯腈1_8重量份、乙苯3〇重量份、十二烷基硫醇〇φ1重量 ——r—___第 20 頁 本紙張尺度適用中國國家標準(CNS ) Α4規格(210x297公摄) 一"" (請先閱讀背面之注意事項再填寫本頁)For granulation, the above kneading is generally performed at 160 ~ 28 (Γ (:, and preferably at a temperature of 180 ~ MO C.) There is no particular limitation on the order of the ingredients of the aforementioned mixing and kneading. Not significant To the extent that the effect of the resin composition of the present invention is impaired, other ingredients may be blended. These other ingredients are, for example, colorants, fillers, flame retardants, flame retardant additives (antimony trioxide, etc.), and light stability. Additives, heat stabilizers, plasticizers, lubricants, release agents, tackifiers, antistatic agents, oxidation inhibitors, conductive agents, etc .; the above additives can be, for example: mineral oil, such as: butyl stearate Ester-based plasticizers, polyester-based plasticizers, such as polydimethylsiloxane-organopolysiloxanes, higher fatty acids and their metal salts, hindered amine-based antioxidants, glass fibers, etc., which can be used alone or mixed The amount of use of the above-mentioned ester-based plasticizer or mineral oil is based on 100 parts by weight of the tree. The composition is generally 0 to 5 wt%, preferably 0.05 to 2 wt%, and the organic polysiloxane The amount of alkane used is generally from 0 to 0.5% by weight. It is better to print the amount% printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs. 〇 [Physical property test] 1. Transparency (haze) · • Inject the resin composition into a 3mm thick test piece , And measure transparency according to ASTM D-1003 standard, the higher the Haze value, the worse the transparency. 2. Transmittance: according to ASTM-1003 test thickness ____% 17 pages This paper size applies to China Standard (CNS) A4 size (210x7 ^ cent)-printed by the Consumers Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 506973 Λ7 B7 V. Description of the invention (16) 3mm test piece, the unit is expressed in%. III. Processability (Spiral flow): The transparent styrene resin composition was molded in a Toshiba ISIOOEN injection molding machine at a cylinder temperature of 220 ° C, a mold temperature of 60 ° C, and an injection pressure of 600 kg / cm2, and was formed using a swirl mold (2mmt), and the flow length was evaluated. Flowability. 4. Melt index (MI): measured by ASTM D-1238 method. 5. Pollution of processing molds: After continuously molding 50 molds at 280 ° C, observe the pollutants on the molded products. Impact: ◎: indicates There is no pollution. △: indicates that the mold is slightly polluted. X: indicates that the mold is seriously polluted. 6. The content of the low molecular weight polymer (wt%) in the dichloromethane-soluble molecular weight of the styrene resin is less than 350. The styrene resin composition was dissolved in a dichloromethane solvent and separated by a telecentric centrifuge. The upper soluble fraction was taken and analyzed by a gas chromatography-mass spectrometer (GC-MASS). Mass spectrometer locates low-molecular-weight polymers with molecular weights below 350, such as terpolymers or dimers, and uses the standard area conversion of styrene; the above-mentioned low-molecular-weight polymers are, for example: AMS, MMS, AS, MSS, SSS, MS Etc., where A is acrylonitrile monomer, M is methyl (meth) acrylate monomer, S is styrene monomer, and the gas phase analyzer is Hewlett Packard Company No. 5890A. [Example] 丨 Implementation __ page 18 ____ This paper size applies the Chinese National Standard (CNS) A4 specification (210X 297 mm) (please read the precautions on the back before filling this page), 11 lines' Ministry of Economic Affairs Printed by the Consumer Standards Cooperative of the Central Bureau of Standards 506973 Λ7 B7 V. Description of the Invention (Π) Using a continuous polymerization device composed of four serially connected fully-mixed reaction tanks with a capacity of 40 liters to produce transparent resin components 8.4 parts by weight of a rubbery copolymer (styrene / butadiene content = 25/75% by weight, 1,2-vinyl content = 15.4%, Mooney viscosity 45 increasing block copolymer), and 23.4 weight by styrene Parts, 38.2 parts by weight of methyl methacrylate, 30 parts by weight of ethylbenzene, 0.08 parts by weight of dodecyl mercaptan, 0.045 parts by weight of pentaerythritol tetrastearate, and dibenzoyl peroxide 0.08 A part by weight is formed into a feed solution, which is continuously supplied to the reaction tank at a flow rate of 35 kg / hr using a pump for polymerization. The temperature of the first reaction tank is 109 ° C, the temperature of the second reaction tank is 114 ° C, and the third The temperature of the reaction tank was 130 ° C. The fourth reaction The temperature is 140 ° C, total polymerization conversion rate of 60%. After the polymerization, the reaction tank was continuously supplied to the devolatilization device through the polymerization solution, and the vacuum degree of devolatilization was controlled to 200 Torr. The volatile substances such as unreacted monomers and organic solvents were separated, and then the resin was extruded through an extruder. Pellets. The continuous phase of the composition contains 36 parts by weight of a styrene structural monomer and 64 parts by weight of methyl methacrylate. The pentaerythritol tetrastearate content of the transparent styrene resin composition is 0.1 part by weight (based on 100 parts by weight). Parts of transparent styrene resin), the average particle size of the dispersed phase rubber particles is 0.42 μm, and the content of low-molecular-weight polymers with a molecular weight of less than 350 in the dichloropyrene solubles accounts for 0.62% by weight of the total solubles. . Example 2 丨 A continuous polymerization device composed of four serially connected complete mixing reaction tanks containing 40 liters was used to manufacture a transparent stupid vinyl resin composition. 8.4 parts by weight of a rubbery copolymer (styrene / butylene) Second dilute content = 25/75% by weight, ______ page 19 ^ Paper size applies Chinese National Standard (CNS) Α4 specifications (21〇 ---- (Please read the precautions on the back before filling this page), 1T line · Printed by the Consumers' Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 506973 A7 _____ B7 V. Description of the invention (18) 1,2-vinyl content = 15.4%, Mooney viscosity 45 increasing block copolymer), and stupid ethylene 23.4 weight Parts, 38 parts by weight of methyl methacrylate, 30 parts by weight of ethylbenzene, 0.09 parts by weight of dodecyl mercaptan, 0.14 parts by weight of pentaerythritol tetrastearate, and dibenzoyl peroxide 009 A part by weight is formed into a feed solution, which is continuously supplied to the reaction tank at a flow rate of 35 kg / hr using a pump to perform polymerization. The temperature in the first reaction tank is ,, the temperature in the second reaction tank is 107 ° C, and the third The temperature of the reaction tank was 122 ° C. The temperature of the fourth reaction tank The degree is 132 C, and the total polymerization conversion rate is 60%. After polymerization, the polymerization solution is continuously supplied to the devolatilization device from the polymerization solution, and the vacuum degree of devolatilization is controlled to 130 Torr. Unreacted monomers and organic solvents, etc. The volatile matter is separated, and the resin pellets are pelletized by an extruder. The continuous phase of the composition contains 36 parts by weight of a styrene structural monomer and 64 parts by weight of methyl methacrylate, and pentaerythritol of a transparent styrene resin composition. Tetrastearate content is 0.3 parts by weight (based on 100 parts by weight of transparent styrene resin), the weight average particle size of the dispersed phase rubber particles is 0.41, and the molecular weight in the dichloromethane soluble fraction is less than The content of low molecular weight polymer of 350% accounts for 0.43% by weight of the total solubles. Bundle Example 3 | Using a continuous polymerization device composed of four series-connected reaction tanks with a total mixing capacity of 40 liters to produce transparent styrene resin Composition, 8.4 parts by weight of a rubbery copolymer (styrene / butadiene content = 25/75% by weight, 1,2-vinyl content == 15.4%, Mooney viscosity 45 increasing block copolymer), With styrene 2 2.8 parts by weight, 37.0 parts by weight of methyl methacrylate, 1-8 parts by weight of acrylonitrile, 30 parts by weight of ethylbenzene, and dodecyl mercaptan 0φ1 by weight—r —___ page 20 Standard (CNS) Α4 specification (210x297 public camera) I " " (Please read the precautions on the back before filling this page)
、1T _線·— 經濟部中央標準局員工消費合作社印製 506973 Λ7 --一--— ___^ R7 五、發明説明(19 ) 知、季戊四醇四硬脂酸酯〇·32重量份,以及過氧化二苯甲 醯〇·ι重量份形成進料溶液,使用幫浦以35kg/hr之流量連續 地供給至反應槽中進行聚合,第一反應槽的溫度為1〇2它, 第二反應槽的溫度為l〇6°C,第三反應槽的溫度為117t, 第四反應槽的溫度為127t:,總聚合轉化率在6〇%。聚合後 由反應槽經聚合溶液連續供給至脫揮發裝置,控制其脫揮 發的真空度在80 T0rr,將未反應單體及有機溶劑等之揮發 性物質分離,而後經由擠壓機將樹脂丸粒化。 其組成之連續相中含有苯乙烯構造單體34重量份、甲 基丙烯酸甲®旨63重量份、丙烯腈3重量份,透明苯乙烯系樹 脂組成物之季戊四醇四硬脂酸酯含量為〇 7重量份(基於1〇〇 重I份之透明苯乙烯系樹脂),分散相橡膠粒子之重量平均 粒徑為0.35μιη,二氣曱烷可溶份中分子量低於35〇之低分 子量聚合物含量佔全部可溶份的〇·22重量%。 例4丨 使用容量為40公升之完全混合型反應槽四個串聯所構 成之連續聚合裝置來製造透明苯乙烯系樹脂組成物,將橡 膠狀共聚物8.4重量份(苯乙烯/丁二烯含量=25/75重量%, 1,2-乙烯基含量=15·4% , M〇〇ney黏度“之漸增嵌段共聚 物),與苯乙烯22.8重量份、甲基丙烯酸曱酯37 〇重量份、 丙稀腈1.8重量份、乙苯30重量份、十二院基硫醇〇ι重量 份、季戊四醇四硬脂酸酯〇·91重量份,以及過氧化二苯曱 酿〇.1重量份形成進料溶液,使用幫浦以35kg/hr之流量連續 地供給至反應槽中進行聚合,第一反應槽的溫度為ι〇2 ^ -7------ ^21 頁 本紙張尺度適财麵家料·( CNS ) Α4規格(2Λ〇7297^Υ~ (請先閱讀背面之注意事項再填寫本頁)、 1T _line · —Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs 506973 Λ7 ----- ___ ^ R7 V. Description of the invention (19) Known, pentaerythritol tetrastearate 0.32 parts by weight, and Dibenzyl oxide was formed into a feed solution by weight, and was continuously supplied to the reaction tank at a flow rate of 35 kg / hr using a pump for polymerization. The temperature of the first reaction tank was 102, and the second reaction tank The temperature was 10 ° C, the temperature in the third reaction tank was 117t, and the temperature in the fourth reaction tank was 127t :, the total polymerization conversion rate was 60%. After the polymerization, the reaction tank was continuously supplied to the devolatilization device through the polymerization solution, and the vacuum degree of devolatilization was controlled to 80 T0rr. The volatile substances such as unreacted monomers and organic solvents were separated, and then the resin pellets were extruded through an extruder. Into. The continuous phase of the composition contains 34 parts by weight of styrene structural monomer, 63 parts by weight of methyl methacrylate, 3 parts by weight of acrylonitrile, and the pentaerythritol tetrastearate content of the transparent styrene resin composition is 〇7. Parts by weight (based on 100 parts by weight of transparent styrene resin), the weight average particle size of the dispersed phase rubber particles is 0.35 μm, and the content of the low molecular weight polymer in the dioxane-soluble fraction is less than 35. It is 0.22% by weight of the total solubles. Example 4 丨 A continuous styrenic resin composition was manufactured using four continuous polymerization devices composed of four fully-mixed reaction tanks with a capacity of 40 liters in series, and 8.4 parts by weight of a rubbery copolymer (styrene / butadiene content = 25/75% by weight, 1,2-vinyl content = 15.4%, MOONY viscosity "increasing block copolymer", with 22.8 parts by weight of styrene and 37% by weight of methacrylate , 1.8 parts by weight of acrylonitrile, 30 parts by weight of ethylbenzene, 0 parts by weight of dodecanyl mercaptan, 0.91 parts by weight of pentaerythritol tetrastearate, and 0.1 parts by weight of diphenyl peroxide. The feed solution was continuously supplied to the reaction tank at a flow rate of 35 kg / hr using a pump for polymerization. The temperature of the first reaction tank was ι〇2 ^ -7 ------ ^ 21 pages Noodles (CNS) Α4 specifications (2Λ〇7297 ^ Υ ~ (Please read the precautions on the back before filling in this page)
、1T 線·! 經濟部中央標準局員工消費合作社印製 Λ7 、^、___ B7 A、發明説明(20 ) —— 第二反應槽的溫度為l〇6°C,第三反應槽的溫度為U7t:, 第四反應槽的溫度為127°C,總聚合轉化率在60%。聚合後 由反應槽經聚合溶液連續供給至脫揮發裝置,控制其脫揮 發的真空度在80 Torr,將未反應單體及有機溶劑等之揮發 性物質分離’而後經由擠壓機將樹脂膠粒化。 其組成之連續相中含有苯乙烯構造單體34重量份、甲 基丙烯酸甲酯63重量份、丙烯腈3重量份,透明苯乙烯系樹 脂組成物之季戊四醇四硬脂酸酯含量為2 〇重量份(基於1〇〇 重里伤之透明苯乙烯系樹脂),分散相橡膠粒子之重量平均 粒徑為0·35μιη,二氯甲烷可溶份中分子量低於35〇之低分 子量聚合物含量佔全部可溶份的〇·21重量%。 f施例5丨 使用容量為40公升之完全混合型反應槽四個串聯所構 成之連續聚合裝置來製造透明苯乙烯系樹脂組成物,將橡 膠狀共聚物8.4重量份(苯乙烯/丁二烯含量=25/75重量%, 1,2-乙烯基含量=15.4%, Mooney黏度45之漸增嵌段共聚 物),與本乙嫦22.8重量份、甲基丙稀酸甲酯" ο重量份、 丙烯腈1_8重量份、乙苯30重量份、十二烷基硫醇〇1重量 伤,以及過氧化二苯甲醯〇· 1重量份形成進料溶液,使用幫 浦以35kg/hr之流量連續地供給至反應槽中進行聚合,第一 反應槽的溫度為102°C,第二反應槽的溫度為1〇6。〇,第三 反應槽的溫度為117°C,第四反應槽的溫度為127。〇,總聚 合轉化率在60%。聚合後由反應槽經聚合溶液連續供給至 脫揮發裝置,控制其脫揮發的真空度在8〇 T〇rr,將未反應 ________第 22 頁 本紙張尺度適用中國國家標準(CNS ) A4規格(21〇x]97公嫠)~ -------- (請先閱讀背面之注意事項再填寫本頁) 、^τ 506973 Λ7 η________B? 五、發明説明(21 ) 單體及有機溶劑等之揮發性物質分離,而後經由擠壓機將 樹脂膠粒化。之後將上述笨乙烯系樹脂1〇〇重量份與〇.3重 1份之季戊四醇四硬脂酸酯混合均勾後,經押出機混練押 出造粒。 其組成之連續相中含有苯乙烯構造單體34重量份、甲 基丙烯酸甲酯63重量份、丙烯腈3重量份,透明苯乙烯系樹 脂組成物之季戊四醇四硬脂酸酯含量為0.3重量份(基於1〇〇 重量份之透明苯乙烯系樹脂),分散相橡膠粒子之重量平均 粒徑為0.33μπι,二氯甲烷可溶份中分子量低於35〇之低分 子量聚合物含量佔全部可溶份的〇 24重量%。 啐較例1丨 經濟部中央標準局員工消費合作社印製 (請先閱讀背面之注意事項再填寫本頁} 使用容量為40公升之完全混合型反應槽四個串聯所構 成之連續聚合裝置來製造透明苯乙烯系樹脂組成物,將橡 膠狀共聚物8.4重量份(苯乙烯/丁二烯含量=25/75重量% , 1,2-乙烯基含量=ΐ5·4%, Mooney黏度45之漸增嵌段共聚 物)’與苯乙稀22.8重量份、甲基丙稀酸甲酯37.0重量份、 丙烯腈1.8重量份、乙苯30重量份、十二烷基硫醇〇 〇6重量 份、季戊四醇四硬脂酸酯〇·48重量份,以及過氧化二苯甲 醯0_05重量份形成進料溶液,使用幫浦以35kg/hr:^流量連 續地供給至反應槽中進行聚合,第一反應槽的溫度為U4C>c ,苐一反應槽的溫度為120°C,第三反應槽的溫度為135 °C ,第四反應槽的溫度為155°C,總聚合轉化率在64%。聚合 後由反應槽經聚合溶液連續供給至脫揮發裝置,控制其脫 揮發的真空度在250T〇rr,將未反應單體及有機溶劑等之揮 __第烈頁 本紙張尺度適用中國國家標準(CNS ) A4規格(210X 297公釐) 一---- 經濟部中央標準局員工消費合作社印製 506973 hi —-__________B7 五、發明説明(22 ) 發性物質分離,而後經由擠壓機將樹脂膠粒化。 其組成之連續相中含有苯乙烯構造單體34重量份、甲 基丙烯酸甲酯63重量份、丙烯腈3重量份,透明苯乙烯系樹 脂組成物之季戊四醇四硬脂酸酯含量為1 〇重量份(基於1〇〇 重量份之透明苯乙烯系樹脂),分散相橡膠粒子之重量平均 粒徑為0·45μιη,二氯甲烷可溶份中分子量低於35〇之低子 量聚合物含量佔全部可溶份的2·2重量%。 f較例2丨 使用谷里為40公升之完全混合型反應槽四個串聯所構 成之連續聚合裝置來製造透明苯乙烯系樹脂組成物,將橡 膠狀共聚物8.4重量份(苯乙烯/ 丁二烯含量=25/75重量%, 1,2-乙烯基含量=ΐ5·4%, Mooney黏度45之漸增嵌段共聚 物),與苯乙烯22.8重量份、甲基丙烯酸甲酯37 〇重量份、 丙烯腈1.8重量份、乙苯30重量份、十二烷基硫醇〇1重量 份,以及過氧化二苯甲醯01重量份形成進料溶液,使用幫 浦以35kg/hr之流量連續地供給至反應槽中進行聚合,第一 反應槽的‘溫度為1〇2。〇,第二反應槽的溫度為1〇6。〇,第三 反應槽的溫度為117°C,第四反應槽的溫度為127t:,總聚 合轉化率在60%。聚合後由反應槽經聚合溶液連續供給至 脫揮發裝置,控制其脫揮發的真空度在8〇 T〇rr,將未反應 單體及有機溶劑等之揮發性物質分離,而後經由擠壓機將 樹脂膠粒化。 其組成之連續相中含有苯乙烯構造單體34重量份、甲 基丙烯酸甲酯63重量份、丙烯腈3重量份,基於1〇〇重量份 _____________ 第 24 頁 本紙張尺度適用中國國家標準(CNS ) Α槻格(21〇^了97公着f (請先閱讀背面之注意事項再填寫本頁) 、1Τ · I - I - 五、 Λ7 B? 經濟部中央標準局員工消費合作社印製 發明説明(23 ) 之透明苯乙烯系樹脂,該分散相橡膠粒子之重量平均粒徑 為〇·37μιη,二氯甲烷可溶份中分子量低於35〇之低分子量 聚合物的含量佔全部可溶份的0.25重量%,所得之樹脂組 成物射出成型時離型性差。 Ρ較例3| 使用容量為40公升之完全混合型反應槽四個串聯所構 成之連續聚合裝置來製造透明苯乙烯系樹脂組成物,將橡 膠狀共聚物8.4重量份(苯乙稀/丁二稀含量=25/75重量%, 1,2-乙稀基含量=15.4%, Mooney黏度45之漸增嵌段共聚 物),與苯乙烯22.8重量份、甲基丙烯酸甲酯37〇重量份、 丙烯腈1.8重量份、乙苯30重量份、十二烷基硫醇〇〇9重 份,以及過氧化二苯甲醯0.丨重量份形成進料溶液,使用 浦以35kg/hr之流量連續地供給至反應槽中進行聚合,第 反應槽的溫度為102°C,第二反應槽的溫度為1〇6。〇,第 反應槽的溫度為117°C,第四反應槽的溫度為127它,總 合轉化率在60%。聚合後由反應槽經聚合溶液連續供給 脫揮發裝置,控制其脫揮發的真空度在8〇 T〇rr,將未反 單體及有機溶劑等之揮發性物質分離,而後經由擠壓機 樹脂膠粒化。之後將上述苯乙烯系樹脂1〇〇重量份與6重 份之季戊四醇四硬旨混合均勾後,經押出機混練押 造粒。 其組成之連續相中含有苯乙烯構造單體34重量份、 ㈣酸甲,63重量份、丙婦腈3重量份,透明苯乙稀系樹 脂組成物之季戊四醇四硬脂酸酯含量為6 〇重量份(基於1 〇〇 量 至 應 將 量 甲 (請先閲讀背面之注意事項再填寫本頁}Line 1T ·! Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs Λ7, ^, ___ B7 A, Description of Invention (20) —— The temperature of the second reaction tank is 106 ° C, and the temperature of the third reaction tank is U7t: The temperature of the fourth reaction tank is 127 ° C, and the total polymerization conversion rate is 60%. After the polymerization, the reaction tank was continuously supplied to the devolatilization device through the polymerization solution, and the vacuum degree of devolatilization was controlled at 80 Torr. The volatile substances such as unreacted monomers and organic solvents were separated, and then the resin pellets were extruded through an extruder. Into. The continuous phase of the composition contains 34 parts by weight of a styrene structural monomer, 63 parts by weight of methyl methacrylate, and 3 parts by weight of acrylonitrile. The pentaerythritol tetrastearate content of the transparent styrene resin composition is 200% by weight. Parts (based on 100% transparent styrene resin), the weight average particle size of the dispersed phase rubber particles is 0.35 μm, and the content of low-molecular-weight polymers with a molecular weight of less than 35 in the dichloromethane solubles accounts for all Soluble content was 0.21% by weight. fExample 5 丨 A continuous styrenic resin composition was produced by using a continuous polymerization device composed of four series-connected full-mixing reaction tanks with a capacity of 40 liters, and 8.4 parts by weight of a rubbery copolymer (styrene / butadiene Content = 25/75% by weight, 1,2-vinyl content = 15.4%, Mooney viscosity 45 increasing block copolymer), with 22.8 parts by weight of ethyl acetate, methyl methacrylate " ο weight Parts, 1-8 parts by weight of acrylonitrile, 30 parts by weight of ethylbenzene, 1 part by weight of dodecyl mercaptan, and 0.1 parts by weight of dibenzoyl peroxide, forming a feed solution, using a pump at 35 kg / hr. The flow rate was continuously supplied to the reaction tank for polymerization. The temperature in the first reaction tank was 102 ° C, and the temperature in the second reaction tank was 106. ○, the temperature of the third reaction tank was 117 ° C, and the temperature of the fourth reaction tank was 127. 〇, the total polymerization conversion rate is 60%. After the polymerization, the reaction tank is continuously supplied to the devolatilization device through the polymerization solution, and the vacuum degree of devolatilization is controlled to 80 Torr. The unreacted ________ page 22 This paper applies the Chinese National Standard (CNS) A4 specification (21〇x] 97 公 嫠) ~ -------- (Please read the notes on the back before filling this page), ^ τ 506973 Λ7 η ________ B? V. Description of the invention (21) Monomer and organic solvent The volatile materials are separated, and then the resin is pelletized by an extruder. Thereafter, 100 parts by weight of the above stupid vinyl resin was mixed with 0.3 part by weight of 1 part of pentaerythritol tetrastearate, and then the mixture was mixed and extruded through an extruder to pelletize. The continuous phase of the composition contains 34 parts by weight of a styrene structural monomer, 63 parts by weight of methyl methacrylate, and 3 parts by weight of acrylonitrile. The pentaerythritol tetrastearate content of the transparent styrene resin composition is 0.3 parts by weight. (Based on 100 parts by weight of transparent styrene resin), the weight average particle diameter of the dispersed phase rubber particles is 0.33 μm, and the content of the low molecular weight polymer with a molecular weight of less than 35 in the dichloromethane soluble fraction accounts for all the soluble Parts of 0. 24% by weight.啐 Comparative example 1 丨 Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs (please read the precautions on the back before filling this page) Manufactured using a continuous polymerization device composed of four serially connected reaction tanks with a capacity of 40 liters Transparent styrene resin composition, 8.4 parts by weight of rubber-like copolymer (styrene / butadiene content = 25/75% by weight, 1,2-vinyl content = ΐ5.4%, Mooney viscosity 45 gradually increasing Block copolymer) 'with 22.8 parts by weight of styrene, 37.0 parts by weight of methyl methacrylate, 1.8 parts by weight of acrylonitrile, 30 parts by weight of ethylbenzene, 006 parts by weight of dodecyl mercaptan, and pentaerythritol 0.48 parts by weight of tetrastearate and 0_05 parts by weight of dibenzoylperoxide were fed into a reaction tank at a flow rate of 35 kg / hr: ^ using a pump to perform polymerization. The first reaction tank The temperature is U4C> c, the temperature in the first reaction tank is 120 ° C, the temperature in the third reaction tank is 135 ° C, the temperature in the fourth reaction tank is 155 ° C, and the total polymerization conversion rate is 64%. After polymerization, Continuously supplied from the reaction tank through the polymerization solution to the devolatilizing device to control The vacuum degree of devolatilization is 250T0rr, and the volatility of unreacted monomers and organic solvents will be reduced._ 第 烈 页 The paper size applies the Chinese National Standard (CNS) A4 specification (210X 297 mm). Printed by the Consumers' Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 506973 hi —-__________ B7 V. Description of the invention (22) The hair substance is separated, and then the resin gel is pelletized by an extruder. The continuous phase of the composition contains a styrene structural monomer 34 parts by weight, 63 parts by weight of methyl methacrylate, 3 parts by weight of acrylonitrile, and the pentaerythritol tetrastearate content of the transparent styrene resin composition is 10 parts by weight (based on 100 parts by weight of transparent styrene Series resin), the dispersed phase rubber particles have a weight-average particle diameter of 0.45 μm, and the content of the low-molecular-weight polymer in the dichloromethane-soluble fraction of less than 350,000 accounts for 2.2% by weight of the total soluble fraction. Comparative Example 2 丨 A transparent styrenic resin composition was manufactured by using a continuous polymerization device composed of four serially-equipped 40-liter fully-mixed reaction tanks in series, and 8.4 parts by weight of a rubbery copolymer (styrene / butadiene With = 25/75% by weight, 1,2-vinyl content = ΐ5.4%, Mooney viscosity 45 increasing block copolymer), with 22.8 parts by weight of styrene, 37.0 parts by weight of methyl methacrylate, propylene 1.8 parts by weight of nitrile, 30 parts by weight of ethylbenzene, 0.01 parts by weight of dodecyl mercaptan, and 01 parts by weight of dibenzoylperoxide were fed into a feed solution, which was continuously supplied to the pump at a flow rate of 35 kg / hr. Polymerization was performed in the reaction tank. The temperature of the first reaction tank was 102.0, the temperature of the second reaction tank was 106.0, the temperature of the third reaction tank was 117 ° C, and the temperature of the fourth reaction tank. 127t: The total polymerization conversion rate is 60%. After the polymerization, the reaction tank was continuously supplied to the devolatilization device through the polymerization solution, and the vacuum degree of devolatilization was controlled to 80 Torr, and the volatile substances such as unreacted monomers and organic solvents were separated, and then extruded through the extruder. Resin gum is granulated. The continuous phase of the composition contains 34 parts by weight of styrene structural monomer, 63 parts by weight of methyl methacrylate, and 3 parts by weight of acrylonitrile. Based on 100 parts by weight _____________ page 24 This paper applies Chinese national standards ( CNS) Α 槻 格 (21〇 ^ 97 public f (please read the notes on the back before filling out this page), 1T · I-I-5, Λ7 B? Printed by the Consumers Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs It is stated that the weight average particle diameter of the dispersed styrene resin of the transparent styrene resin of (23) is 0.37 μm, and the content of the low-molecular-weight polymer having a molecular weight of less than 35 in the dichloromethane solubles accounts for the total solubles. 0.25% by weight, the obtained resin composition had poor mold release properties during injection molding. Comparative Example 3 | A continuous styrenic resin composition was produced by using a continuous polymerization device composed of four series-connected complete mixing reaction tanks with a capacity of 40 liters. 8.4 parts by weight of a rubbery copolymer (styrene / butadiene content = 25/75% by weight, 1,2-ethylene content = 15.4%, Mooney viscosity 45 increasing block copolymer), With styrene 22.8 weight , 37 parts by weight of methyl methacrylate, 1.8 parts by weight of acrylonitrile, 30 parts by weight of ethylbenzene, 009 parts by weight of dodecyl mercaptan, and 0.1 part by weight of dibenzoyl peroxide forming feed The solution was continuously supplied to the reaction tank at a flow rate of 35 kg / hr using Pu to polymerize. The temperature in the first reaction tank was 102 ° C, the temperature in the second reaction tank was 106. 0, and the temperature in the second reaction tank was 117. ° C, the temperature of the fourth reaction tank is 127, and the total conversion rate is 60%. After the polymerization, the reaction tank is continuously supplied to the devolatilization device through the polymerization solution, and the vacuum degree of the devolatilization is controlled to 80 Torr. The volatile substances such as the anti-monomer and the organic solvent are separated, and then granulated by the resin of the extruder. After mixing 100 parts by weight of the above styrene resin with 6 parts by weight of the pentaerythritol four hard purpose, The extruder is mixed and extruded and granulated. The continuous phase of the composition contains 34 parts by weight of styrene structural monomer, 63 parts by weight of formic acid, 63 parts by weight, and 3 parts by weight of acetonitrile, and pentaerythritol tetra, a transparent styrene resin composition. The stearic acid content is 60 parts by weight (based on 100 parts) To the amount of A (Please read the precautions on the back before filling this page}
私纸張尺度適用中國國家標準(CNS ) A4規格 3 25頁 (210x297公釐) A7 ' —------- B7 五、發明説明(24) 一 — — 重量份之透明苯乙烯系樹脂),分散相橡膠粒子之重量平均 粒徑為,二氯甲烧可溶份中分子量低於350之低分子 I聚合物含量佔全部可溶份的0·24重量%。 (請先閱讀背面之注意事項再填寫本頁) [^例4丨 經濟部中央標準局員工消費合作社印製 使用谷里為40 Α升之元全混合型反應槽四個串聯所構 成之連續聚合裝置來製造透明笨乙婦系樹脂組成物,將橡 膠狀共聚物8·4重量份(苯乙婦/丁二烯含量=25/75重量%, 1,2-乙烯基含量=15.4%,M_ey黏度衫之漸增嵌段共聚 物)’與苯乙婦22.8重量份、甲基丙烯酸甲酯37〇重量份、 丙烯腈1.8重量份、乙苯3〇重量份、十二烧基硫醇〇〇9重量 份,以及過氧化二苯甲酿〇.〇9重量份形成進料溶液,使用 幫浦以35kg/hr之流量連續地供給至反應槽中進行聚合,第 一反應槽的溫度為103。〇,第二反應槽的溫度為107t:,第 二反應槽的溫度為123°C,第四反應槽的溫度為131它,總 聚合轉化率在60%。聚合後由反應槽經聚合溶液連續供給 至脫揮發裝置,控制其脫揮發的真空度在13〇 T〇rr,將未 反應單體及有機溶劑等之揮發性物質分離,而後經由擠壓 機將樹脂膠粒化。將上述苯乙烯系樹脂1〇〇重量份與2重量 份之硬脂酸甲酯混合均勻後經由押出機混練押出造粒。 其組成之連續相中含有苯乙烯構造單體34重量份、甲 基丙烯酸甲酯63重量份、丙烯腈3重量份,透明苯乙烯系樹 脂組成物之硬脂酸甲酯的含量為2_〇重量份(基於1〇〇重量份 之透明苯乙烯系樹脂),分散相橡膠粒子之重量平均粒徑為 0·4μιη ’ 一氣甲烧可溶份中分子量低於350之低分子量聚合 — 第 26頁 ^紙張尺度適用中國國家標準(CNS ) Α4規格(2ι〇χ297公釐) 經濟部中央標準局員工消費合作社印製 A7 -------一~~_____B? 五、發明説明(25) —…— ^―'— —~~一 物含量佔全部可溶份的〇·43重量%。 ^WWs\ 使用容量為40公升之完全混合型反應槽四個串聯所構 成之連續聚合裝置來製造透明笨乙烯系樹脂組成物,將橡 膠狀共聚物8.4重量份(苯乙烯/ 丁二烯含量=25/75重量%, 1,2-乙烯基含量=15·4%, M〇〇ney黏度衫之漸增嵌段共聚 物),與苯乙烯22.8重量份、甲基丙烯酸甲酯37 〇重量份、 丙烯如1.8重1份、乙苯3〇重量份、十二烷基硫醇〇 〇8重量 份,以及過氧化二苯甲醯0·08重量份形成進料溶液,使用 幫浦以35kg/hr之流量連續地供給至反應槽中進行聚合,第 一反應槽的溫度為1〇4。(:,第二反應槽的溫度為1〇9。〇,第 二反應槽的溫度為125X:,第四反應槽的溫度為135°c,總 聚合轉化率在60%。聚合後由反應槽經聚合溶液連續供給 至脫揮發裝置,控制其脫揮發的真空度在2〇〇T〇rr ,將未反 應單體及有機溶劑等之揮發性物質分離,而後經由擠壓機 將樹脂膠粒化。上述苯乙烯系樹脂1〇〇重量份與2重量份之 硬月曰酸丁醋混合均勻後經由押出機混練押出造粒。 其組成之連續相中含有苯乙烯構造單體34重量份、曱 基丙烯酸甲酯63重量份 '丙烯腈3重量份,透明苯乙烯系樹 脂組成物之硬脂酸丁酯含量為2·〇重量份(基於1〇〇重量份之 透明苯乙烯系樹脂),分散相橡膠粒子之重量平均粒徑為 〇·41μπι’二氯甲烧可溶份中分子量低於350之低分子量聚 合物含量佔全部可溶份的0.62重量%。 較例6| ___第 27 頁 本紙張尺度適用中國國家標準(CNS ) A4規格(210X 297公釐) (請先閱讀背面之注意事項再填寫本頁) 訂 _線·· 經濟部中央標準局員工消費合作社印製 506973 A7 ------------______ 五、發明説明(26 ) 一 使用容量為40公升之完全混合型反應槽四個串聯所構 成之連續聚合裝置來製造透明苯乙烯系樹脂組成物,將橡 膠狀共聚物8.4重量份(苯乙烯/丁二烯含量=25/75重量%, 1,2-乙烯基含量=15.4%, Mooney黏度45之漸增嵌段共聚 物),與本乙稀22.8重量份、甲基丙婦酸甲酯37·〇重量份、 丙烯腈1.8重量份、乙苯30重量份、十二烧基硫醇重量 伤,以及過氧化二苯甲酿〇 · 1重量份形成進料溶液,使用幫 浦以35kg/hr之流1連績地供給至反應槽中進行聚合,第一 反應槽的溫度為102°C,第二反應槽的溫度為1〇6°c,第三 反應槽的溫度為117T:,第四反應槽的溫度為127°c,總聚 合轉化率在60%。聚合後由反應槽經聚合溶液連續供給至 脫揮發裝置,控制其脫揮發的真空度在8〇 T〇rr,將未反應 單體及有機溶劑等之揮發性物質分離,而後經由擠壓機將 樹脂膠粒化。上述苯乙烯系樹脂1〇〇重量份與2重量份之乙 烯雙硬脂醯胺混合均句後經由押出機混練押出造粒。 其組成之連續相中含有苯乙烯構造單體34重量份、甲 基丙烯酸甲酯63重量份、丙烯腈3重量份,透明苯乙烯系樹 脂組成物之乙烯雙硬脂醯胺含量為2.〇重量份(基於1〇〇重量 份之透明苯乙烯系樹脂),分散相橡膠粒子之重量平均粒徑 為〇·35μπι,二氣甲烷可溶份中分子量低於35〇之低分子量 聚合物含量佔全部可溶份的〇.2ΐ重量%。 使用容量為40公升之完全混合型反應槽四個串聯所構 成之連續聚合裝置來製造透明苯乙烯系樹脂組成物,將橡 __ _ 第 28 頁 本紙張尺度適用中國國家標準(CNS ) 公f )-----*- (請先閱讀背面之注意事項再填寫本頁}Private paper size applies to Chinese National Standard (CNS) A4 size 3 25 pages (210x297 mm) A7 '—------- B7 V. Description of the invention (24) 1--parts by weight of transparent styrene resin ), The weight average particle diameter of the dispersed phase rubber particles is that the content of the low molecular I polymer having a molecular weight of less than 350 in the dichloromethane-soluble fraction accounts for 0.24% by weight of the total soluble fraction. (Please read the precautions on the back before filling out this page) [^ Example 4 丨 Printed by the Consumers' Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs using a 40-liter full-mixed reaction tank in the valley. The device was used to make a transparent resin composition, and 8.4 parts by weight of a rubbery copolymer (styrene / butadiene content = 25/75% by weight, 1,2-vinyl content = 15.4%, M_ey Viscosity shirt's increasing block copolymer) 'with 22.8 parts by weight of acetophenone, 37 parts by weight of methyl methacrylate, 1.8 parts by weight of acrylonitrile, 30 parts by weight of ethylbenzene, and dodecyl mercaptan. 9 parts by weight and 0.09 parts by weight of dibenzoyl peroxide were used to form a feed solution, which was continuously supplied to the reaction tank at a flow rate of 35 kg / hr using a pump for polymerization. The temperature of the first reaction tank was 103. 〇, the temperature of the second reaction tank is 107t :, the temperature of the second reaction tank is 123 ° C, the temperature of the fourth reaction tank is 131, and the total polymerization conversion rate is 60%. After the polymerization, the reaction tank was continuously supplied to the devolatilization device through the polymerization solution, and the vacuum degree of devolatilization was controlled to be 130 Torr. The volatile substances such as unreacted monomers and organic solvents were separated, and then extruded through the extruder. Resin gum is granulated. 100 parts by weight of the above styrene-based resin and 2 parts by weight of methyl stearate were mixed uniformly, and then granulated through an extruder. The continuous phase of the composition contains 34 parts by weight of a styrene structural monomer, 63 parts by weight of methyl methacrylate, and 3 parts by weight of acrylonitrile. The content of methyl stearate in the transparent styrenic resin composition is 2 mm. Parts by weight (based on 100 parts by weight of transparent styrenic resin), the weight average particle size of the dispersed phase rubber particles is 0.4 μm η ′ Low molecular weight polymerization with a molecular weight of less than 350 in the gas-soluble sintering — page 26 ^ The paper size applies the Chinese National Standard (CNS) A4 specification (2 × 297 mm) Printed by the Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs A7 ------- 一 ~~ _____ B? V. Description of Invention (25) — … — ^ ―'— — ~~ The content of one substance accounts for 0.43% by weight of the total solubles. ^ WWs \ A continuous polymerization device composed of four series-connected complete mixing reaction tanks with a capacity of 40 liters was used to manufacture a transparent stupid vinyl resin composition. 8.4 parts by weight of a rubbery copolymer (styrene / butadiene content = 25/75% by weight, 1,2-vinyl content = 15.4%, an incremental block copolymer of Money viscosity shirt), with 22.8 parts by weight of styrene and 37.0 parts by weight of methyl methacrylate 1, such as 1.8 parts by weight of propylene, 30 parts by weight of ethylbenzene, 008 parts by weight of dodecyl mercaptan, and 0.08 parts by weight of dibenzoylperoxide to form a feed solution, using a pump at 35 kg / The flow rate of hr was continuously supplied to the reaction tank for polymerization, and the temperature of the first reaction tank was 104. (: The temperature of the second reaction tank is 109.0. The temperature of the second reaction tank is 125X :, the temperature of the fourth reaction tank is 135 ° C, and the total polymerization conversion rate is 60%. After the polymerization, the reaction tank The polymerization solution is continuously supplied to the devolatilization device, and the vacuum degree of devolatilization is controlled to 2000 Torr. The volatile substances such as unreacted monomers and organic solvents are separated, and then the resin is pelletized through an extruder. 100 parts by weight of the styrene resin and 2 parts by weight of hard butyl vinegar are mixed and extruded and granulated by an extruder. The continuous phase of the composition contains 34 parts by weight of styrene structural monomer, 63 parts by weight of methyl acrylate, 3 parts by weight of acrylonitrile, and butyl stearate content of the transparent styrene resin composition was 2.0 parts by weight (based on 100 parts by weight of the transparent styrene resin), dispersed The weight average particle size of the phase rubber particles is 0.41 μm, and the content of the low-molecular-weight polymer having a molecular weight of less than 350 in the dichloromethane-soluble fraction accounts for 0.62% by weight of the total soluble fraction. Comparative Example 6 | ___ page 27 This paper size applies to Chinese National Standards (CNS ) A4 size (210X 297 mm) (Please read the notes on the back before filling out this page) Order_line ·· Printed by the Staff Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 506973 A7 ----------- -______ V. Description of the invention (26) A continuous polymerization device composed of four serially connected complete reaction tanks with a capacity of 40 liters is used to manufacture a transparent styrene resin composition. 8.4 parts by weight of a rubbery copolymer (benzene Ethylene / butadiene content = 25/75% by weight, 1,2-vinyl content = 15.4%, Mooney viscosity 45 increasing block copolymer), and 22.8 parts by weight of ethylene, methyl methacrylate 37.0 parts by weight of ester, 1.8 parts by weight of acrylonitrile, 30 parts by weight of ethylbenzene, weight of dodecyl mercaptan, and 0.1 parts by weight of dibenzoyl peroxide were used to form a feed solution, using a pump at 35 kg The flow rate of 1 / hr was continuously supplied to the reaction tank for polymerization. The temperature of the first reaction tank was 102 ° C, the temperature of the second reaction tank was 106 ° C, and the temperature of the third reaction tank was 117T: The temperature of the fourth reaction tank is 127 ° C, and the total polymerization conversion rate is 60%. After the polymerization, the reaction tank passes the polymerization solution. Continue to supply to the devolatilization device, control the vacuum degree of devolatilization to 80 Torr, separate the volatile materials such as unreacted monomers and organic solvents, and then granulate the resin through an extruder. The styrene above 100 parts by weight of resin is mixed with 2 parts by weight of ethylene distearylamine, and the granules are kneaded and extruded through an extruder to form granules. The continuous phase of the composition contains 34 parts by weight of styrene structural monomer and methyl methacrylate. 63 parts by weight of ester, 3 parts by weight of acrylonitrile, ethylene bisstearylamine content of the transparent styrenic resin composition is 2.0 parts by weight (based on 100 parts by weight of the transparent styrenic resin), and dispersed phase rubber The weight-average particle size of the particles is 0.35 μm, and the content of the low-molecular-weight polymer having a molecular weight of less than 35 in the digas methane soluble fraction accounts for 0.2% by weight of the total soluble fraction. A continuous styrenic resin composition is manufactured by using a continuous polymerization device composed of four series of fully mixed reaction tanks with a capacity of 40 liters. The size of this paper applies to Chinese National Standards (CNS). ) ----- *-(Please read the notes on the back before filling this page}
、1T 線‘ 經濟部中央標準局員工消費合作社印製 ^06973 A7 一_______B7 五、發明説明(27) ~ — 膠狀共聚物8.4重量份(苯乙烯/丁二烯含量=25/75重量%, 1,2-乙烯基含量=15.4%, Mooney黏度45之漸增嵌段共聚 物),與笨乙烯22·8重量份、甲基丙烯酸甲酯37 〇重量份、 丙烯腈1.8重f份、乙苯3〇重量份,與十二烷基硫醇重 量份、白蠟油0.91重量份、過氧化二苯甲醯〇1重量份形成 進料溶液,使用幫浦以35kg/hr之流量連續地供給至反應槽 中進行聚合’第一反應槽的溫度為1 〇2°c,第二反應槽的溫 度為106°C,第三反應槽的溫度為ii7cC,第四反應槽的溫 度為127 C,總聚合轉化率在60%。聚合後由反應槽經聚合 溶液連續供給至脫揮發裝置,控制其脫揮發的真空度在8〇 Torr,將未反應單體及有機溶劑等之揮發性物質分離,而 後經由擠壓機將樹脂膠粒化。 其組成之連續相中含有苯乙烯構造單體34重量份、甲 基丙烯酸甲酯63重量份、丙烯腈3重量份,透明苯乙稀系樹 脂組成物之白蠛油含量為2.0重量份(基於1〇〇重量份之透明 苯乙烯系樹脂),分散相橡膠粒子之重量平均粒徑為〇.37μιη ,二氯甲烷可溶份中分子量低於350低分子量聚合物含量 佔全部可溶份的0.21重量%。 啐較例8丨 使用容量為40公升之完全混合型反應槽四個串聯所構 成之連續聚合裝置來製造透明苯乙烯系樹脂組成物,將橡 膠狀共聚物8.4重量份(苯乙烯/丁二烯含量=25/75重量%, 1,2-乙烯基含量=15.4%, Mooney黏度45之漸增嵌段共聚 物),與苯乙烯22.8重量份、甲基丙烯酸甲酯37.0重量份、 __ 第 29 頁_____ 本紙張尺度適用中國國家標準(CNS ) A4規格(210X 297公釐) (請先閱讀背面之注意事項再填寫本頁)Line 1T printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs ^ 06973 A7 _______B7 V. Description of the Invention (27) ~ — 8.4 parts by weight of colloidal copolymer (styrene / butadiene content = 25/75% by weight 1,2-vinyl content = 15.4%, Mooney viscosity 45 increasing block copolymer), with 22.8 parts by weight of stupid ethylene, 37.0 parts by weight of methyl methacrylate, 1.8 parts by weight of acrylonitrile, 30 parts by weight of ethylbenzene, 0.91 parts by weight of dodecyl mercaptan, 0.91 parts by weight of white wax oil, and 01 parts by weight of dibenzoyl peroxide were fed into the feed solution continuously using a pump at a flow rate of 35 kg / hr. Polymerization in the reaction tank 'The temperature of the first reaction tank is 10 ° C, the temperature of the second reaction tank is 106 ° C, the temperature of the third reaction tank is ii7cC, and the temperature of the fourth reaction tank is 127 C, The total polymerization conversion was 60%. After the polymerization, the reaction tank was continuously supplied to the devolatilization device through the polymerization solution, and the vacuum degree of devolatilization was controlled to 80 Torr. The volatile substances such as unreacted monomers and organic solvents were separated, and then the resin gum was extruded through an extruder. Granulated. The continuous phase of the composition contains 34 parts by weight of a styrene structural monomer, 63 parts by weight of methyl methacrylate, and 3 parts by weight of acrylonitrile. The content of the white oil of the transparent styrene resin composition is 2.0 parts by weight (based on 100 parts by weight of transparent styrene resin), the weight average particle size of the dispersed phase rubber particles is 0.37 μιη, and the content of the low molecular weight polymer in the dichloromethane soluble fraction is less than 350, accounting for 0.21 of the total soluble fraction. weight%.啐 Comparative Example 8 丨 A continuous styrenic resin composition was manufactured by using a continuous polymerization device composed of four series-connected fully-mixed reaction tanks with a capacity of 40 liters, and 8.4 parts by weight of a rubbery copolymer (styrene / butadiene Content = 25/75% by weight, 1,2-vinyl content = 15.4%, Mooney viscosity 45 increasing block copolymer), with 22.8 parts by weight of styrene, 37.0 parts by weight of methyl methacrylate, Page _____ This paper size applies Chinese National Standard (CNS) A4 (210X 297 mm) (Please read the precautions on the back before filling this page)
506973 A7 B7 五 經濟部中央標準局員工消費合作社印製 發明説明(28 ) 〜 丙烯腈1.8重量份、乙苯3〇 旦^ 、 里里切 與十二烷基硫醇0.1重 里伤、過氧化二苯甲醯〇· J重量份 里切开7成進料溶液,使用幫浦 以35kg/hr之流量連續地#仏 化K也仏、、、口至反應槽中進行聚合,第一反 應槽的溫度為1 〇2,筮-只_姚^ 弟一反應槽的溫度為106°C,第三反 應槽的溫度為urc ’第四反應槽的溫度為飢,總聚合 轉化率在6G%。*合後由反應槽經聚合溶液連續供給至脫 揮發裝置’控制其脫揮發的真空度在⑽W,將未反應單 體及有機溶劑等之揮發性物f分離,而後經由擠壓機將樹 脂膠粒化。之後將上述苯乙烯系樹脂100重量份與2重量份 之聚乙烯堰(PE Wax)混合均勻後,經押出機混練押出造粒 〇 其組成之連續相中含有苯乙烯構造單體34重量份、甲 基丙婦酸甲酉旨63重量份、丙婦腈3重量份,透明苯乙婦系樹 脂組成物之聚乙烯蠟含量為2. 〇重量份(基於i 〇 〇重量份之透 明苯乙烯系樹脂),分散相橡膠粒子之重量平均粒徑為 〇.37μπι 一氣甲烧可溶份中分子量低於350之低分子量聚 合物含量佔全部可溶份的0.22重量%。 以上實施例1〜5及比較例1〜8的物性測試比較見表一。味施例6丨 使用聚苯乙烯1〇〇重量份(奇美公司POLYREX PG383) 與〇·6重量份之季戊四醇四硬脂酸酯混合均句後由押出機混 練押出造粒,測其二氣甲烷可溶份中分子量低於35〇之低 分子量聚合物的含量為0.65重量%,加工性(ΜΙ)為3.6,透 明性(Haze)為1_0%,穿透率為90.5%,射出成型之離型性良 (請先閱讀背面之注意事項再填寫本頁) -—^ϋ ϋ·^^— af^—ϋ ml·. 訂 第30頁 本紙張尺度適用中國國家標準(CNS ) A4規格(210X 297公髮) 經濟部中央標準局員工消費合作社印製 Λ 7 s—---------B7 五、發明説明(29 ) … 好。 例9丨 使用聚苯乙烯100重量份(奇美公司p〇LYRE pG383)測 其二氣甲烧可溶份中分子量低於350之低分子量聚合物含 里為0.65重量%,加工性(]^1)為3〇,透明性(11^幻為〇8% ’穿透率為90·8%,但樹脂之射出成型的離型性差。 使用苯乙烯-丙烯腈共聚物1〇〇重量份(奇美公司 KIBISAN PN-117)與〇.5重量份之季戊四醇四硬脂酸酯混合 物均勻後,由押出機混練押出造粒,測其二氯甲烷可溶份 中分子量低於350之低分子量聚合物含量為185重量%,加 工性(MI)為3·4 ’透明性(Haze)為1.5%,穿透率為90.6%, 射出成型之離型性良好。 ¥較例10丨 使用苯乙烯-丙烯腈共聚物1〇〇重量份(奇美公司 KIBISAN PN-117),測其二氣甲烧可溶份中分子量低於35〇 之低分子量聚合物含量為185重量%,加卫性⑽)為3 〇, 透明性(Haze)為1.4%,穿透率為9〇 8%,但樹脂之射出成型 之離型性差。 由比較例1之實驗結果得知,當樹脂組成物中二氯甲烷 可溶份中分子量小於350之低分子量聚合物含量高於2 〇重 量份時,樹脂在射出成型時產生模具污染,而由比較例2 之實驗結果得知,當樹脂中未添加季戊四醇之酯類時,樹 脂的加工性不理想且樹脂之離型性差,而當樹脂中添加過 _________ 第 31 頁 本紙張尺度適用中國國家標準(CNS ) A4規格(21 〇χ 297公髮) (請先閲讀背面之注意事項再填寫本頁)506973 A7 B7 Printed invention description printed by the Consumers' Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs (28) ~ 1.8 parts by weight of acrylonitrile, 30 denier of ethylbenzene ^, richet and dodecyl mercaptan 0.1 grave injury, peroxide 70% by weight of benzamidine was cut into a feed solution, and the pump was continuously polymerized at a flow rate of 35 kg / hr using a pump to polymerize the reaction solution in the reaction tank. The temperature was 10%, the temperature of the first reaction tank was 106 ° C, the temperature of the third reaction tank was urc ', the temperature of the fourth reaction tank was hungry, and the total polymerization conversion rate was 6G%. * After the synthesis, the reaction tank is continuously supplied to the devolatilization device through the polymerization solution. The vacuum degree of devolatilization is controlled at ⑽W to separate unreacted monomers and organic solvents such as volatile matter f, and then the resin glue is extruded through an extruder. Granulated. Then, 100 parts by weight of the above styrene-based resin and 2 parts by weight of a polyethylene weir (PE Wax) were mixed uniformly, and then extruded and granulated by an extruder. The continuous phase of the composition contained 34 parts by weight of a styrene structural monomer, 63 parts by weight of methopropionate, 3 parts by weight of fenpropyronitrile, and a polyethylene wax content of the transparent styrenic resin composition is 2.0 parts by weight (based on i 〇〇parts of transparent styrene Resin), the dispersed phase rubber particles have a weight-average particle size of 0.37 μm, and the content of the low-molecular-weight polymer with a molecular weight of less than 350 in the gas-fired soluble fraction accounts for 0.22% by weight of the total soluble fraction. Table 1 shows the comparison of the physical properties of the above Examples 1 to 5 and Comparative Examples 1 to 8. Example 6 丨 Using 100 parts by weight of polystyrene (CHIMEI Corporation POLYREX PG383) and 0.6 parts by weight of pentaerythritol tetrastearate are mixed and extruded and granulated by an extruder, and the methane gas is measured. The content of the low-molecular-weight polymer with a molecular weight of less than 35 in the soluble fraction is 0.65% by weight, the processability (MI) is 3.6, the transparency (Haze) is 1_0%, the transmittance is 90.5%, and the release molding is released. Liang Liang (Please read the precautions on the back before filling this page) -—— ^ ϋ ϋ · ^^ — af ^ —ϋ ml ·. Order page 30 This paper size is applicable to China National Standard (CNS) A4 specifications (210X 297 Published) Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs Λ 7 s —--------- B7 V. Invention Description (29)… Good. Example 9 丨 Using 100 parts by weight of polystyrene (Chimei p0LYRE pG383) to measure the low molecular weight polymer with a molecular weight of less than 350 in the digassing solution, the content is 0.65% by weight, and the processability (] ^ 1 ) Is 30, transparency (11% is 8%, 'penetration is 90 · 8%, but the release properties of resin injection molding are poor. 100 parts by weight of styrene-acrylonitrile copolymer (Chimei Company KIBISAN PN-117) and 0.5 parts by weight of pentaerythritol tetrastearate were homogenized, and then extruded and granulated by an extruder, and measured the content of low molecular weight polymers with a molecular weight of less than 350 in the dichloromethane solubles. It is 185% by weight, the processability (MI) is 3.4%, the transparency (Haze) is 1.5%, the transmittance is 90.6%, and the release property of injection molding is good. Comparative Example 10 丨 Use of styrene-acrylonitrile 100 parts by weight of the copolymer (KIBISAN PN-117) from Chimei, the content of the low molecular weight polymer having a molecular weight of less than 3500 in the digassine-soluble product was 185% by weight, and the protective property was 3). The transparency (Haze) is 1.4% and the transmittance is 908%, but the release properties of resin injection molding are poor. From the experimental results of Comparative Example 1, it is known that when the content of the low molecular weight polymer with a molecular weight of less than 350 in the dichloromethane-soluble portion of the resin composition is higher than 20 parts by weight, mold contamination occurs during injection molding of the resin. The experimental results of Comparative Example 2 show that when pentaerythritol esters are not added to the resin, the processability of the resin is not satisfactory and the release properties of the resin are poor, and when the resin has been added _________ page 31 This paper applies to China Standard (CNS) A4 specification (21 〇χ 297) (Please read the precautions on the back before filling this page)
經濟部中央標準局員工消費合作社印製 五、發明説明(30 ) "一~— —, 一 星之季戊四醇之酯類時,易產生模具污染且透明度亦降低 ’此由比較例3之實驗結果可證實;再由比較例4、5、7等 實驗結果得知,在透明苯乙烯樹脂中分別添加硬脂酸甲酯 、硬醋酸丁 S旨、白蠟油時,會產生模具污染及透明性差的 現象。另由比較例6、8實驗結果得知,在樹脂中加入乙烯 一硬脂酿胺、聚乙烯蠟,則樹脂的透明性差。 參閱本發明各實施例,本發明在透明苯乙烯系樹脂中 加入特定含量之季戊四醇的酯類化合物,並控制樹脂中二 氣甲烧可溶份中特定低分子量含量,確實可使樹脂組成物 具有良好的透明性及加工性,同時在樹脂成型時亦不會產 生模具污染之現象,因此,本發明確為一新穎、進步,並 具有產業上利用價值之樹脂組成物。 惟以上所述僅為本發明數較佳可行實施例,舉凡熟習 此項技藝人仕,其依本發明精神範疇所作之修飾或變更', 均理應包含在本案申請專利範圍内。 表1 :本發明各實施例與比較例間之物性測試比較表。 (請先閱讀背面之注意事項再填寫本頁〕Printed by the Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs. 5. Description of the invention (30) " One ~ ——, Pentaerythritol esters of one star, mold pollution is easy to occur and transparency is reduced. This can be obtained from the experimental results of Comparative Example 3. Confirmation: According to the experimental results of Comparative Examples 4, 5, and 7, it is known that when methyl stearate, butyl acetate and white wax oil are added to the transparent styrene resin, mold contamination and poor transparency will occur. . It is also known from the experimental results of Comparative Examples 6 and 8 that when ethylene-stearylamine and polyethylene wax are added to the resin, the transparency of the resin is poor. Referring to the embodiments of the present invention, the present invention adds a specific content of pentaerythritol ester compounds to the transparent styrene resin, and controls the specific low molecular weight content of the digasmethane solubles in the resin, which can indeed make the resin composition have Good transparency and processability, and at the same time, mold pollution will not occur during resin molding. Therefore, the present invention is indeed a novel, progressive, and industrially useful resin composition. However, the above description is only a few of the preferred and feasible embodiments of the present invention. For those skilled in the art, modifications or changes made according to the spirit of the present invention should all be included in the scope of patent application in this case. Table 1: Comparison table of physical property test between each example and comparative example of the present invention. (Please read the notes on the back before filling this page)
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TWI481651B (en) * | 2013-05-23 | 2015-04-21 | Chi Mei Corp | (meth) acrylate-styrene based copolymer composition and the molding product thereof |
TWI503362B (en) * | 2013-10-28 | 2015-10-11 | Chi Mei Corp | Rubber-modified polystyrene-based resin composition and molding product |
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US6806313B2 (en) * | 2003-03-05 | 2004-10-19 | W. R. Grace & Co.-Conn. | Erucamide-free closure and liner compositions |
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TWI481651B (en) * | 2013-05-23 | 2015-04-21 | Chi Mei Corp | (meth) acrylate-styrene based copolymer composition and the molding product thereof |
TWI503362B (en) * | 2013-10-28 | 2015-10-11 | Chi Mei Corp | Rubber-modified polystyrene-based resin composition and molding product |
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