TW200724571A - A process for preparing homoblock co-polysulfones and polysulfones prepared therefrom - Google Patents

A process for preparing homoblock co-polysulfones and polysulfones prepared therefrom Download PDF

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TW200724571A
TW200724571A TW95135397A TW95135397A TW200724571A TW 200724571 A TW200724571 A TW 200724571A TW 95135397 A TW95135397 A TW 95135397A TW 95135397 A TW95135397 A TW 95135397A TW 200724571 A TW200724571 A TW 200724571A
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block copolymer
homoblocks
molecular weight
homoblock
block
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TW95135397A
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Chinese (zh)
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Prakash Druman Trivedi
Atul Ramaniklai Raja
Mukesh Shambhubhai Jesani
Modi Haresh Sevantilal
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Solvay Specialities India Priv
Prakash Druman Trivedi
Atul Ramaniklai Raja
Mukesh Shambhubhai Jesani
Modi Haresh Sevantilal
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G75/00Macromolecular compounds obtained by reactions forming a linkage containing sulfur with or without nitrogen, oxygen, or carbon in the main chain of the macromolecule
    • C08G75/20Polysulfones
    • C08G75/23Polyethersulfones
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G65/00Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
    • C08G65/34Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from hydroxy compounds or their metallic derivatives
    • C08G65/38Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from hydroxy compounds or their metallic derivatives derived from phenols
    • C08G65/40Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from hydroxy compounds or their metallic derivatives derived from phenols from phenols (I) and other compounds (II), e.g. OH-Ar-OH + X-Ar-X, where X is halogen atom, i.e. leaving group
    • C08G65/4012Other compound (II) containing a ketone group, e.g. X-Ar-C(=O)-Ar-X for polyetherketones
    • C08G65/4056(I) or (II) containing sulfur

Description

200724571 (1) 九、發明說明 【發明所屬之技術領域】 、 本發明有關一種製備嵌段共聚物之方法及 ^ 之嵌段共聚物。 尤其,本發明有關製備包含至少兩種均嵌 聚物的方法,該均嵌段係屬於聚颯族,尤其f 、PSU、PSS、PPSU、PSSB、PES、TPES φ TMPSS且有關自彼所製備之嵌段共聚物。 此外,本發明有關二-及三-嵌段及無規 聚物及其製備方法。此等均嵌段與其存在於嵌 之分子量比較時可具有不同之分子量或可具有 量。此等嵌段共聚物顯示單一玻璃轉化溫度( 透明性且可使用傳統塑料加工技術而輕易地加 接使用於模塑、擠塑且亦可作爲其高分子量同 容劑。 【先前技術】 聚楓聚合物家族係技術界所熟知,有三種 即聚颯(PSU )、聚醚礪(PES )及聚伸苯基j 〇 市售聚礪(PSU、PPSU、PES)具有良好 ,通常在3 5 0 °C至4 〇 〇 °C之加工溫度下不降解 外,其係透明、淺琥珀色非晶形塑料,具有優 電性質及良好之耐化學性及耐火性。此等聚楓 由彼所製備 段之嵌段共 :選自 PSSD 、PESK 及 多-嵌段共 段共聚物中 相同之分子 Tg)、良好 工。其可直 系物的促相 市售聚碾, 風(PPSU ) 之耐高溫性 或變色。此 異之機械及 可使用一般 -5- 200724571 (2) 塑料加工技術輕易地加工,諸如注射模塑、壓塑、吹塑及 擠塑。此點使其成爲極多用途且易使用之塑料,在電子、 電工業、醫藥、一般工程、食品加工及其他工業具有無數 之應用。 聚礪PSU係於1 960年代早期於Union Carbide (美國 專利第4,1 08,8 3 7號,1 97 8 )發現。自此,即維持積極地 改善PSU品質,多年來,仍持續尋求改善顏色、熱安定 性、分子量及降低殘留單體及溶劑。 雖然PSU、PES及PPSU在顏色、電性質、耐化學性 、耐火性等方面具有許多相似點,但亦存在重要差異。其 中最主要之差異係爲玻璃轉化溫度(Tg) 。PSU具有189 。(:之Tg,PES具有225 t:之Tg,而PPSU則具有222。(:之 Tg。因此’ PSU與PPSU比較,尤其是與具有最高之耐熱 性的PES比較,具有就其形穩性而言整體上較低之耐熱 性。此外,PES亦具有較PSU及PPSU (兩者皆70至75 MPa)爲高之抗張強度(>90 MPa)。另一方面,PPSU 具有如同聚碳酸酯(PC )之優異耐衝擊性,其懸臂樑式 缺口耐衝擊強度係爲670至700 J/m。PES及PSU兩者皆 具有僅5 0至5 5 J/m之較低懸臂樑式缺口耐衝擊強度。相 同地,技術界已知由PPSU製得之物件可承受> 1 000個滅 菌循環而不裂開,但以PSU爲主之物件承受約80個循環 且以PES爲主之物件僅承受約100個循環。另一方面, PSU具有最淺之顏色且可較輕易地加工,而ppsu較暗且 較PSU或PES難以加工。 200724571 (3) 因此,期望PSU性質(諸如易加工性及淺色性質) 與PPSU性質(諸如耐高溫性及耐衝擊性)之組合。將一 、個比例之PSU摻入PPSU內亦可降低整體成本。雖然 , PPSU與PSU之物理性摻合爲達成此目的之一種方式,但 其破壞兩均聚物之一種最重要性質,即其透明性。相同地 ,PES與PSU之物理性摻合物不僅不透明,亦無法加工 產生具有所需性質之摻合物,因其係極不相容之聚合物。 B 在任一情況下,此等組合物皆僅顯示Tg< 225 °c。 較高Tg聚芳基醚礪(TMPES)係使用3,3’,5,5’ —四 甲基一 4,4’ 一二羥基二苯基颯及4,4’ 一二氯二苯基礪作爲 單體來製備。美國專利第5,008,3 64號提及其他具有聯苯 單元如4,4’—二一(4 一氯苯基一磺醯基)一聯苯及4,4’ 一二一(4 一羥基苯基一磺醯基)一聯苯之聚芳基颯,其 於高溫下具安定性。 亦期望以下其他組合物,因其具有高於2 2 0 °C ( P E S B 之Tg)的Tg,藉由摻入此等組合物以進一步提高之耐高 溫性,且藉著於其鏈結構中摻入PES、PSU或PPSU以使 得該耐高溫性聚合物更容易加工。 聚礪家族之某些單元鏈結構係顯示如下: PPSU : --c6h4- so2- c6h4- o- c6h4- C6H4- ο--PSU : --c6h4- so2- c6h4- o- c6h4- C(CH3)2- 〇-- PES : - - C 6 H 4 一 S O 2 一 C 6 H 4 — O 一 C 6 H 4 — S 0 2 — C 6 H 4 — 0-- PSSD : --c6h4- so2- c6h4- c6h4- S〇2- c6h4~ o- 200724571 (4) C6H4 — S〇2 — C6H4 — PSSB : --C6H4- S〇2- C6H4- C6H4- S02- a b 4 〜〇 C6H4 — C6H4 — TPES : --C6H4 — S〇2~ C6H4 — 〇 — C s a s ~~ S〇2 — p ^sH8 PSS : —c6H4— so2- c6h4— c6H4— so2— c6h4〜0- PESK : __c6h4- co2— c.h4- o- c6h4- so2〜p u Z ^ 6 H 4 —200724571 (1) Description of the Invention [Technical Field of the Invention] The present invention relates to a method for preparing a block copolymer and a block copolymer of the same. In particular, the invention relates to a process for the preparation of at least two homopolymers belonging to the group of polyterpenes, in particular f, PSU, PSS, PPSU, PSSB, PES, TPES φ TMPSS and related to their preparation. Block copolymer. Further, the present invention relates to di- and tri-blocks and random polymers and processes for their preparation. These homoblocks may have different molecular weights or may have amounts when compared to their molecular weight present in the embedding. These block copolymers exhibit a single glass transition temperature (transparency and can be easily added for molding, extrusion, and also as a high molecular weight compatibilizer using conventional plastic processing techniques. [Prior Art] Poly Maple The polymer family is well known in the art, and there are three types of polyfluorene (PSU), polyether oxime (PES) and polyphenylene phenyl ruthenium (PSU, PPSU, PES) which are good, usually at 3 50. It is a transparent, light amber amorphous plastic with a non-degradable processing temperature from °C to 4 〇〇 °C. It has excellent electrical properties and good chemical and fire resistance. The block is: selected from the same molecular Tg in PSSD, PESK and multi-block copolymers, and works well. It can promote the phase of the direct product, the high temperature resistance or discoloration of the wind (PPSU). This machine can be easily processed using general processing techniques such as injection molding, compression molding, blow molding and extrusion. This makes it a highly versatile and easy-to-use plastic with numerous applications in the electronics, electrical, medical, general engineering, food processing and other industries. The Poly PSU was discovered in Union Carbide (US Patent No. 4,1 08,8 3 7 ,1 97 8 ) in the early 1960s. Since then, it has been actively improving the quality of PSU, and for many years, it has continued to seek to improve color, thermal stability, molecular weight and reduce residual monomers and solvents. Although PSU, PES and PPSU have many similarities in color, electrical properties, chemical resistance, fire resistance, etc., there are also important differences. The most important difference is the glass transition temperature (Tg). The PSU has 189. (: Tg, PES has 225 t: Tg, and PPSU has 222. (: Tg. Therefore 'PSU compared with PPSU, especially compared with PES with the highest heat resistance, has its shape stability The overall lower heat resistance. In addition, PES also has a higher tensile strength (> 90 MPa) than PSU and PPSU (both 70 to 75 MPa). On the other hand, PPSU has the same polycarbonate. (PC) Excellent impact resistance, its Izod notched impact strength is 670 to 700 J/m. Both PES and PSU have a lower Izod notch resistance of only 50 to 5 5 J/m. Impact strength. Similarly, it is known in the art that articles made from PPSU can withstand > 1 000 sterilization cycles without cracking, but objects with PSU-based objects are subjected to about 80 cycles and PES-based objects are only It takes about 100 cycles. On the other hand, PSU has the lightest color and can be processed relatively easily, while ppsu is darker and more difficult to process than PSU or PES. 200724571 (3) Therefore, PSU properties (such as ease of processing and Light color properties) Combination with PPSU properties such as high temperature resistance and impact resistance. The incorporation of U into the PPSU also reduces the overall cost. Although the physical blending of PPSU and PSU is one way to achieve this, it destroys one of the most important properties of the two homopolymers, namely their transparency. The physical blend of PES and PSU is not only opaque, nor can it be processed to produce a blend of desirable properties because it is a highly incompatible polymer. B In either case, these compositions only show Tg<lt; 225 °c. Higher Tg polyaryl ether oxime (TMPES) uses 3,3',5,5'-tetramethyl-4,4'-dihydroxydiphenyl fluorene and 4,4' one-two Chlorodiphenylphosphonium is prepared as a monomer. U.S. Patent No. 5,008,3,64, the disclosure of other biphenyl units such as 4,4'-di(4-chlorophenylmonosulfonyl)-biphenyl and 4 , 4'-1-2 (4-hydroxyphenyl-sulfonyl)-biphenyl polyaryl fluorene, which has stability at high temperatures. Other compositions are also expected because they have a higher than 2 2 0 ° The Tg of C (Tg of PESB) is further improved by the incorporation of such compositions, and by incorporating PES, PSU or PPSU into its chain structure This high temperature resistant polymer is made easier to process. Some of the unit chain structure of the polyfluorene family is shown as follows: PPSU : --c6h4- so2- c6h4- o- c6h4- C6H4- ο--PSU : --c6h4- so2 - c6h4- o- c6h4- C(CH3)2- 〇-- PES : - - C 6 H 4 -SO 2 -C 6 H 4 - O -C 6 H 4 - S 0 2 - C 6 H 4 - 0 -- PSSD : --c6h4- so2- c6h4- c6h4- S〇2- c6h4~ o- 200724571 (4) C6H4 — S〇2 — C6H4 — PSSB : --C6H4- S〇2- C6H4- C6H4- S02- Ab 4 ~〇C6H4 — C6H4 — TPES : --C6H4 — S〇2~ C6H4 — 〇 — C sas ~~ S〇2 — p ^sH8 PSS : —c6H4 — so2- c6h4 — c6H4 — so2— c6h4~0- PESK : __c6h4- co2 — c.h4- o- c6h4- so2 ~ pu Z ^ 6 H 4 —

O — TMPSS : ,,c6h4— so2- C6H4— c6h4— so2n o —C^H^— S〇2--CgH8~ 〇-聚颯係使用一或多種芳族二鹵基化合物如二氯二¥ _ 颯(DCDPS)、二氯二苯基甲酮(DCB)或二氯二苯基— 磺醯基聯苯(CSB )及其個別單、二、三或四甲基或院其 衍生物及一或多種芳族二羥基單體如雙酚A、二_基二# • 基颯(DHDPS )、聯苯酚、二羥基二苯基二磺醯基聯苯( HSB )、二羥基二苯基醚、二羥基二苯基甲烷、{雙〜( 3,5 —二甲基一 4 一羥苯基)礪}、其個別經單、二、〜 〜 —Μ 四取代之甲基衍生物等製備。 就PPSU而言,所使用之二羥基化合物係爲聯苯酌( HO-C6H4-C6H4-OH ) ,PES 爲 DHDPS,PSU 爲雙酣 A ( HO-C6H4_C(CH3)2-C6H4-OH ),且 TPES 係爲 TMDHDPS (HO-C6H2(CH3)2-S02-C6H2(CH3)2-OH ),而使用 DCDPS 作爲所有此等聚颯之第二種單體。 -8- 200724571O — TMPSS : ,, c6h4— so2- C6H4— c6h4— so2n o —C^H^— S〇2--CgH8~ 〇-Polyfluorene uses one or more aromatic dihalogen compounds such as dichloro 2 _飒 (DCDPS), dichlorodiphenyl ketone (DCB) or dichlorodiphenyl-sulfonylbiphenyl (CSB) and its individual mono-, di-, tri- or tetra-methyl or its derivatives and one or A variety of aromatic dihydroxy monomers such as bisphenol A, bis-base II • guanidine (DHDPS), biphenol, dihydroxydiphenyldisulfonylbiphenyl (HSB), dihydroxydiphenyl ether, two Hydroxydiphenylmethane, {bis~(3,5-dimethyl-4-hydroxyphenyl)anthracene}, which are prepared by a single, two, ~~~~ tetrasubstituted methyl derivative. In the case of PPSU, the dihydroxy compound used is biphenyl (HO-C6H4-C6H4-OH), PES is DHDPS, and PSU is bis-A (HO-C6H4_C(CH3)2-C6H4-OH), and TPES is TMDHDPS (HO-C6H2(CH3)2-S02-C6H2(CH3)2-OH), and DCDPS is used as the second monomer of all such polyfluorenes. -8- 200724571

就PSSD而言,所使用之二羥基化合物係爲DHDPS (h〇-c6h4-so2-c6h4-〇h ),且 PSSB 爲聯苯酚 • ( HO-C6H4-C6H4-OH ) ,TMPSS 係爲 TMDHDPS (H0-C6H2(CH3)2_S02-C6H2(CH3)2-0H ) ,PSS 爲 HSB ( oh-c6h4-so2-c6h4-c6h4-so2-c6h4-oh );而使用 CSB ( Cl-C6H4-S〇2-C6H4-C6H4_S02-C6H4-Cl)作爲第二種單體。 PESK可使用 DCB (二氯二苯基甲酮)及DHDPS製 φ 得。相同地,其他均聚物可藉著DCB與其他二羥基化合 物如DHDPS、聯苯酚、TMDHDPS及HSB反應而製得。 前文製備之均嵌段可與其他均嵌段如PSS、PSSD、 PPSU、PES、PSU、TPES、PSSB 及 TMPSS 等反應。 多於一種二羥基單體之使用亦爲已知。例如,Amoco 所製造稱爲「PAS」之聚合物係在DCDPS及DHDPS之外 包括少量氫醌。第三種單體係於製程開始時添加,故以無 規序列聚合於聚合物鏈中。 φ 先前技術中之其他無規共聚物顯示亦可添加更大量之In the case of PSSD, the dihydroxy compound used is DHDPS (h〇-c6h4-so2-c6h4-〇h), and PSSB is biphenol (HO-C6H4-C6H4-OH), and TMSPS is TMDHDPS (H0). -C6H2(CH3)2_S02-C6H2(CH3)2-0H), PSS is HSB (oh-c6h4-so2-c6h4-c6h4-so2-c6h4-oh); and CSB (Cl-C6H4-S〇2-C6H4) is used. -C6H4_S02-C6H4-Cl) as the second monomer. PESK can be obtained by using DCB (dichlorodiphenyl ketone) and DHDPS φ. Similarly, other homopolymers can be prepared by reacting DCB with other dihydroxy compounds such as DHDPS, biphenol, TMDHDPS and HSB. The homoblocks prepared above can be reacted with other homoblocks such as PSS, PSSD, PPSU, PES, PSU, TPES, PSSB and TMPSS. The use of more than one dihydroxy monomer is also known. For example, a polymer called "PAS" manufactured by Amoco includes a small amount of hydroquinone outside of DCDPS and DHDPS. The third single system is added at the beginning of the process and is therefore polymerized in the polymer chain in a random sequence. φ Other random copolymers in the prior art display can also add a larger amount

第三種單體。因此,GB專利4,331,79 8 ( 1 982 )及US 專利5,326,834 ( 1994)教示三聚物之製備,其係使用80 至40莫耳%之DHDPS及對應之20至60莫耳%的聯苯酚 與接近等莫耳%之DCDPS。因爲兩專利皆教示聚合係以 單體本身開始,故可知DHDPS及聯苯酚於最終共聚物中 之分佈係無規性。因此,取一無規序列諸如… ABAABBBAABAAABBABABBAAABB--,其中 A 及 B 係以 無規序列出現且出現之變化量係視A及B或DHDPS及聯 200724571 (6) 苯酚(DCDPS部分會出現於A-B、A-B & B-B基團之間, 唯此處未顯示)之起始濃度而定。相同地,歐洲專利第 0,331,492號教示DCDPS及DHDPS /聯苯酚或雙酚A /聯 苯酚之無規三聚物的合成。同理,自三種單體開始藉累積 分子量產生無規三聚物(而非嵌段共聚物),其中鏈中A & B之序列係無規,無法預測。 先前技術顯示已製備其中僅一嵌段爲聚礪之嵌段共聚 物。Hedtmann — Rein 及 Heinz (US 專利 5,036,146-1991 )教示PSU與聚醯亞胺(PI )之嵌段共聚物的製備。此 情況下,首先製備胺終端之聚颯的均嵌段。此係使用 DCDPS、雙酣A及對一胺基酚製備,產生分子量介於 1 5 00至20000範圍內之均嵌段。所製得之均嵌段隨後與 四羧酸(諸如二苯基甲酮四甲酸二酐)及另一種二胺(諸 如4,4’一二胺基二苯基甲烷)反應,製得PSu— PI之嵌段 共聚物。該共聚物係於3 5 0 °C於熔融相下製備。The third monomer. Thus, GB Patent 4,331,79 8 (1 982) and US Patent 5,326,834 (1994) teach the preparation of terpolymers using 80 to 40 mole % DHDPS and corresponding 20 to 60 mole % biphenol. Close to the DCD of the Mox%. Since both patents teach that the polymerization begins with the monomer itself, it is known that the distribution of DHDPS and biphenol in the final copolymer is random. Therefore, take a random sequence such as... ABAABBBAABAAABBABABBAAABB--, where A and B appear in a random sequence and the amount of change occurs as A and B or DHDPS and 200724571 (6) phenol (DCDPS part will appear in AB, The initial concentration of AB & BB groups, not shown here). Similarly, European Patent No. 0,331,492 teaches the synthesis of random terpolymers of DCDPS and DHDPS/biphenol or bisphenol A/biphenol. Similarly, a random trimer (rather than a block copolymer) is produced from the three monomers starting from the cumulative molecular weight, wherein the sequence of A & B in the chain is random and unpredictable. The prior art has shown that block copolymers in which only one block is polyfluorene have been prepared. Hedtmann - Rein and Heinz (US Patent 5,036, 146-1991) teach the preparation of block copolymers of PSU and polyimine (PI). In this case, the homoblock of the polyfluorene of the amine terminal is first prepared. This is prepared using DCDPS, biguanide A and p-aminophenol to produce a homoblock having a molecular weight in the range of from 1 500 to 20,000. The resulting homoblock is then reacted with a tetracarboxylic acid (such as diphenyl ketone tetracarboxylic dianhydride) and another diamine (such as 4,4'-diaminodiphenylmethane) to produce PSu- Block copolymer of PI. The copolymer was prepared at 350 ° C in the molten phase.

McGrath 及同事(Polymer preprints, 25,14,1 984 ) 已製備PSU —聚對苯二甲酸酯共聚物。此係使用DCDPS (〇· 141莫耳)及氫醌與聯苯酚(各〇·〇75莫耳)混合物 完成,於溶液中產生均嵌段,之後使用溶液或界面技術使 該均嵌段與對苯二甲醯氯及聯苯酚反應,產生嵌段共聚物 〇McGrath and colleagues (Polymer preprints, 25, 14, 1 984) have prepared PSU-poly terephthalate copolymers. This is done using a mixture of DCDPS (〇· 141 mol) and hydroquinone with biphenol (each 〇·〇 75 mol) to produce a homoblock in solution, after which the homoblock is paired using solution or interfacial techniques. Reaction of phthalocyanine chloride with biphenol to produce a block copolymer

McGrath φ \ ( Polymer Preprints, 26,275,1 98 5 )進 一步描述使用乙醯基末端封蓋PSU與對-乙醯氧基苯甲 酸或聯苯酚二乙酸酯/對苯二甲酸以製得PSU /聚醚之嵌 -10- 200724571 (7) 段共聚物的製備,後者係高度結晶或甚至液晶聚合物。嵌 段共聚物之合成係以熔體或於二苯基颯存在下於200至 3 00 °C進行。嵌段共聚物製備係由產物不可溶於一般有機 溶劑的事實顯示。McGrath φ \ (Polymer Preprints, 26, 275, 1 98 5 ) further describes the use of an ethyl thiol end capping PSU with p-acetoxybenzoic acid or biphenol diacetate / terephthalic acid to produce a PSU / Polyether Embedding - 200724571 (7) Preparation of a segment copolymer, the latter being highly crystalline or even a liquid crystal polymer. The synthesis of the block copolymer is carried out in the presence of a melt or in the presence of diphenylphosphonium at 200 to 300 °C. The preparation of block copolymers is shown by the fact that the product is insoluble in common organic solvents.

Maresca等人已製備具有改良之玻璃轉化溫度的聚芳 基醚,其含有至少20重量%雙一(3,5 —二甲基—4 —羥 苯基)颯。 _ Wang 及同事(Polymer International,5 0(2),249 200 1已合成由苯甲內醯胺及全氟亞異丙基-聚芳基醚颯 所組成之新穎無規及嵌段共聚物。Maresca et al. have prepared polyaryl ethers having an improved glass transition temperature containing at least 20% by weight of bis(3,5-dimethyl-4-hydroxyphenyl)anthracene. _ Wang and colleagues (Polymer International, 50(2), 249 200 1 have synthesized novel random and block copolymers composed of benzalamine and perfluoroisopropylidene-polyarylether.

Gerhard及同事(US專利3,647,751)已使用二鹵基 一二苯基-二礪芳基及鹼金屬雙酚鹽製備聚芳基醚颯。Gerhard and coworkers (U.S. Patent 3,647,751) have used the dihalo-diphenyl-diindenyl and alkali metal bisphenolates to prepare polyaryl ether oximes.

McGrath 及同事(Polymer Preprints, 26,277,1 9 8 5 ) 亦發展PSU與PEEK之嵌段共聚物,其係使用羥基終端之 寡聚P SU均嵌段及二氟二苯基甲酮本身或視情況添加氫 • 醌及/或聯苯酚。第一種方法非產生嵌段共聚物,而是產 生藉二氟二苯基甲酮連接之PSU嵌段。然而,第二種方 法具有在PSU及PEEK共聚物中同時產生無規及嵌段兩結 構之可能。 雖然前述硏究已製備PSU嵌段共聚物,但可發現大 部分係選擇羥基終端PSU與其他單體之組合物,在聚合 時產生嵌段共聚物。此種方法中,聚合之單體極易產生變 化極大之嵌段尺寸,使得某些PSU嵌段僅藉分子量僅有 300或更小(當然<1〇〇〇)之單一單體單元連接。因此, -11 - 200724571 (8) 第二嵌段之分子量不是PSU寡聚物者,理想是>1000方 稱爲嵌段。因此,視濃度而定,第二均嵌段易不多於單一 或兩個單體單元。此情況可藉著個別製備兩均嵌段且使其 反應產生嵌段共聚物來避免。McGrath and colleagues (Polymer Preprints, 26, 277, 1 9 8 5) also developed block copolymers of PSU and PEEK, which use hydroxyl terminated oligo P SU homoblocks and difluorodiphenyl ketone itself or Add hydrogen, hydrazine and/or biphenol, as appropriate. The first method does not produce a block copolymer, but instead produces a PSU block linked by difluorodiphenyl ketone. However, the second method has the potential to simultaneously produce both random and block structures in the PSU and PEEK copolymers. Although the foregoing studies have prepared PSU block copolymers, it has been found that most of the combinations of hydroxyl terminated PSUs with other monomers produce block copolymers upon polymerization. In such a process, the polymerized monomer is highly susceptible to a greatly variable block size such that certain PSU blocks are only joined by a single monomer unit having a molecular weight of only 300 or less (of course <1〇〇〇). Therefore, -11 - 200724571 (8) The molecular weight of the second block is not a PSU oligomer, and is ideally > 1000 square. Therefore, depending on the concentration, the second homoblock is preferably no more than a single or two monomer units. This can be avoided by separately preparing the two homoblocks and reacting them to produce a block copolymer.

Noshay 及同事(J. Polymer Sci. A-1,3147,1971)已 製備胺終端二甲基矽氧烷及羥基終端psu之嵌段共聚物 。該羥基終端PSU係使用稍微較DCDPS ( 0.45〇莫耳)過 量之雙酚A(0.495莫耳)製備。該- ON a基團隨之使用草 酸轉化成-OH基團,產物沉澱。經乾燥之PSU粉末與個 別製備之胺終端聚矽氧烷於乙醚中在6 0 °C反應。可注意 因P S U爲塑性,聚矽氧烷爲彈性,因此組合物產生具有 類似熱塑性彈料性質之嵌段共聚物。 然而,意外的是所述之方法及所進行之合成皆無法使 用兩種礪均嵌段形成具有熱塑性之嵌段共聚物。 製備此等聚颯之一般方法係由以下製程組成: 將選自環丁楓、N —甲基吡咯啶酮(NMP )或二甲基 亞礪(DMS0 )之非質子有機溶劑(通常於鹼上蒸餾)置 入反應器中。DCDPS或任一種類似之二鹵基單體(如二 氯二苯基二磺醯基聯苯(CSB )、二氯二苯基甲酮等)及 一種第二種二羥基單體(聯苯酚、DHDPS、TMDHDS或 HSB等)通常在接近莫耳比1.00 : 1.00下與碳酸鈉或碳 酸鉀一起添加於此反應器中。添加甲苯或單氯苯(MCB) 以促進脫水。混合物溫度隨後緩緩增至14〇C至230C ( 視所採用之溶劑而定)’此時驗性碳酸鹽與酚反應產生鹽 -12- 200724571 Ο) 並釋出水。將水餾除,此係藉甲苯或MCB (若存在)增 進。 ' 移除水之後的反應混合物接著加熱至170°c至250°c . 範圍內之溫度(視所使用之溶劑、鹼及二羥基單體而定) ’直至達到所需之黏度或分子量。之後,增長之鏈視情況 於末端封蓋上MeCl,過濾反應物質以移除鹽,之後沉澱 物鏈於水或MeOH中沉澱,進一步處理以移除殘留之溶劑 φ 並乾燥。或可閃蒸去除溶劑,反應物質可直接通經脫揮發 物擠塑機,以去除殘留溶劑並將聚合物造粒。 於前述者中添加一種以上之羥基單體產生鏈中無規摻 入三種(而非兩種)單體單元之三元共聚物。 期望發展一種嵌段共聚物形成方法,以將兩塑料(兩 者皆爲以颯爲主之均嵌段)連接形成嵌段共聚物形式之單 一鏈。如前所述,不同聚楓之嵌段共聚物係技術界所未知 〇 # 通常,如技術界已知,自均嵌段成功地形成嵌段共聚 物須符合三項要求: i)該兩均嵌段應具有彼此反應之末端基團,即-OH & -CNO。 ii )每個均嵌段應具有兩個相同末端基團,即-OH或-CNO。 i i i )該兩均嵌段應於正確化學計量比例下混合以產生 局分子量嵌段共聚物。 本發明揭示一種使用二或更多種不同聚楓均嵌段製備 -13- 200724571 (10) 嵌段共聚物之方法,而避開每個均嵌段具有實際相同之末 端基團的嚴格要求。相同地,可在形成高分子量嵌段聚合 物時免除二或更多種均嵌段之正確化學計量的需要。 【發明內容】 發明槪述 本發明有關一種製備嵌段共聚物之方法,該嵌段共聚 物包含至少兩種均嵌段,該均嵌段係選自P S S D、P S S B、 TPES、PSS、TMPSS 或 PESK 或選自至少一種 PSSD、 PSSB、TPES、PSS、TMPSS 或 PESK 及至少一種 PPSU、 PES或PSU,其中該均嵌段各具有至少1 000之相同或相 異分子量且具有總重量之至少5 %,其中該嵌段共聚物係 具有至少2000之分子量,該方法步驟係包含: (a )藉著於至少一種鹼存在下,視情況於至少一種 溶劑中,且另外視情況於共沸劑存在下,加熱至少一種芳 族二醇/二羥基化合物與至少一種芳族二鹵基化合物(其 中一種含有至少一個楓基),製備前述各種均嵌段, (b )使前述均嵌段一起於介於! 3 〇 至2 5 0。(:間之溫 度下視情況於至少一種溶劑中反應,另外視情況接著將該 嵌段共聚物之末端封蓋, (c )回收該嵌段共聚物。 本發明亦有關使用前述方法製備之嵌段共聚物及包含 至少兩種均嵌段之嵌段共聚物,該均嵌段係選自p S S D、 PSSB、TPES、PSS、TMPSS 或 pESK 或選自至少一種 -14- 200724571 (11) PSSD、PSSB、TPES、PSS、TMPSS 或 PESK 及至少一種 PPSU、PES或PSU,直接鍵合或藉鍵合基團鍵合以形成 ~ 嵌段共聚物鏈,其中該均嵌段各具有至少1 000之相同或 、 相異分子量且具有總重量之至少5 %且其中該嵌段共聚物 係具有至少2000之分子量。 此等新穎之嵌段共聚物係使用先個別製備較低分子量 之均嵌段,隨之以不同比例混合並進一步反應產生高分子 p 量嵌段共聚物的技術製備。使用此種技術,可確定嵌段結 構之形成及其序列及嵌段分子量。除了分段之多嵌段化合 物外,甚至可使用此方法製得具有已知嵌段分子量之高分 子量二嵌段或三嵌段及多嵌段。發現所製備之嵌段共聚物 可作爲新穎之聚颯塑料,亦可作爲促相容劑。 發明描述 通常,聚礪之均嵌段的聚合物鏈上存有兩個可能之鏈 ϋ 末端結構。此等末端基團係爲來自二鹵基(DCDPS、CSB 、DCB等)部分之-C1及來自酚單體之-ΟΗ。特定均嵌段 聚合物鏈亦可兼具兩末端基團之混合物。 就嵌段共聚物而言,基於先前技術預測其中一均嵌段 應僅具有兩個-C1末端基團/鏈且第二個均嵌段應僅具有 兩個-ΟΗ末端基團/鏈。於正確之化學計量比例下混合且 使其反應則會產生高分子量嵌段共聚物。然而,因爲兩均 嵌段皆可能具有-C1或-oh混合末端基團,故本發明顯示 可不遵守前文所述每個均嵌段皆應同樣具有兩個相同末端 -15- 200724571 (12) 基團且兩均嵌段須以正確化學計量比例混合的嚴苛要求。 聚颯通常具有一'些-C1及一些-OH末端基團。每一種 之濃度皆由兩個重要因素決定:首先爲二鹵基化合物如 DCDPS、DCB或 CSB等相對於所使用之二羥基酚單體的 起始莫耳比,其次若莫耳比並非確實1 : 1則爲可建構之 聚合物的分子量。兩單體之比例爲極重要因素,因爲欲建 構極高分子量,比例以莫耳計須保持接近1 : 1。通常, 一種單體之濃度不應較另一種單體高出約1至2莫耳%。 因此,莫耳比通常保持在1.02: 1.00至1.00: 1.02範圍 內,以得到高分子量。任一種單體之濃度增加至超過此範 圍通常皆導致化學計量紊亂至無法建構足夠之共聚物分子 量的程度,大部分聚合物性質皆受損,因其未達到最佳値 。然而,製備寡聚均嵌段時,該種嚴苛之化學計量出乎意 料地並非必要,因爲不需建構高分子量。因此,就均嵌段 製備而言,本發明已成功地採用高達1.15: 1.00之單體 比例。均嵌段中之單體比例範圍因此係自1.02 : 1.00增 至1.15 : 1.00,而未犧牲嵌段共聚物之最終分子量。 本發明有關新穎之聚楓嵌段共聚物結構及進行其製備 之新穎方法。本發明尤其有關新穎類型之嵌段共聚物的製 備,該嵌段共聚物係使用 PES、PPSU、PSSD、PSSB、 PSS、TPES、PSU、TMPSS及P E S K及類似之聚颯均嵌段 製得,且有關其製備方法。該嵌段共聚物可使用至少兩種 不同之聚颯製得且可使用多於兩種之聚颯製得。 本發明方法包括使用溶液聚合技術製備新穎之聚颯家 -16- 200724571 (13) 族嵌段共聚物。此等嵌段共聚物係使用較 嵌段(例如聚伸苯基楓(PPSU ) 、PES、 - TPES、PSS、TMPSS、PSU 及 PESK )製備 _ 本發明之一重要態樣係本發明有關一 度及高玻璃轉化溫度的嵌段共聚物。該嵌 (> 22 0 °C )及嚴苛之化學環境下保持可 理性質。先前技術所揭示之嵌段共聚物具 § 溫度,因此僅能使用於需要連續使用溫度 用,而無法使用於高溫應用,諸如燈具外 料及其他暴露於熱及機械應力之物件。 本發明方法主要的新穎且意料外態樣 給予之均嵌段應僅具有兩末端基團中之一 間之化學計量須爲1 : 1的嚴苛要求。因 可製備高分子量嵌段共聚物,而每個均嵌 同末端基團且並非嚴格控制化學計量。因 ϋ 化嵌段共聚物之形成。而且,與較早期之 製備方法比較,本發明可更輕易地使用相 大組成範圍之嵌段共聚物組合物。當然, 端基團之均嵌段且使之具有正確化學計量 方法,但此等條件不再是建構高分子量嵌 〇 此種方法亦使其可適當地控制末端基 聚物,其中該兩均嵌段具有各種分子量且 具有大範圍之組成,而此點在稍早討論之 低分子量寡聚均 PSSB 、 PSSD 、 ί ° 種具有高撓曲溫 段共聚物於高溫 使用之機械及物 有較低之熱撓曲 低於180°C之應 殼、太空複合材 係其可不遵守所 且所使用均嵌段 此,本發明方法 段上並不具有相 此本發明大幅簡 分段嵌段共聚物 同均嵌段製得較 使用具有相同末 比例絕不傷及該 段共聚物的前提 團以製備嵌段共 嵌段共聚物亦可 其他類型嵌段共 -17- 200724571 (14) 聚物中不易或甚至不可能達成。 新穎嵌段共聚物係藉著先使用原來個別製備之具有實 -施例性鏈末端基團的較低分子量均嵌段製得。術語「均嵌 。段」係表示每個嵌段具有PES或PSSB或TPES或PSSD 或PPSU或TMPSS或PSS、PSU或PESK或某些該種聚楓 結構,不同之均嵌段具有彼此相異之結構。該兩均嵌段係 個別製備且排列成具有兩個依序相或相異之末端基團。重 P 點是實現本發明所教示的-兩相異末端基團(此情況下 爲-C1及-OH )當然應接近化學計量平衡。重要的是可兩 末端基團皆存在於兩均嵌段上。 製備均嵌段之不同方式如下: 第一組均嵌段係製備成主要具有鹵素末端基團,諸 如-F、-Cl、-Br及-I。第二組均嵌段係製備成主要具有第 二種末端基團,其可與鹵素末端基團反應,諸如-OH (其 可以鹽形式存在- OK、-ONa或- OLi )。此在第一種情況下 § 係藉著採用較之二羥基單體爲大量莫耳過量的二鹵基單體 完成,在第二種情況則掉換該比例。通常,當主要具有第 一種末端基團之較低分子量均嵌段與另一種主要具有第二 種末端基團之均嵌段反應時,得到具有高分子量之嵌段共 聚物。因此,例如,主要具有-OH末端基團之低分子量 PSSB均嵌段與主要具有-C1末端基團之低分子量PSSD均 嵌段反應產生在嵌段共聚物序列中具有[PSSD-PSSB]z或 {[PSSB…PSSD]z}之新穎嵌段共聚物。當一均嵌段主要具 有完全相同末端基團(例如-C1 )且與主要皆具有第二種 -18- 200724571 (15) 末端基團(例如-OH )之第二種均嵌段反應時,所得之嵌 段共聚物具有分子量如同起始均嵌段的PSSD & PSSB嵌 •段。本發明因此可使均嵌段之分子量幾乎與其成爲鏈中一 .部分的嵌段相同。 亦可根據本發明製備其中PSSD之均嵌段具有鹵素末 端基團且PSSB均嵌段具有酚-oh末端基團之嵌段共聚物 ,及相反地其中PSSD具有羥基末端基團且PSSB具有鹵 • 素末端基團之嵌段共聚物。如本發明所示,特定均嵌段之 末端基團可相互交換。當各均嵌段具有不相同之末端基團 (例如-C1及-OH )時,重要的是使其在兩均嵌段中具有 相對上相同之化學計量。當製造一或兩高分子量均嵌段時 ’重要的是如同二-嵌段及三-嵌段製備般地使兩末端基 團儘可能保持相異。 然而,本發明可使兩均嵌段皆具有兩末端基團且仍使 用於製造高分子量嵌段共聚物。此點可藉著採用接近相同 • 莫耳比之兩單體而達成。此情況下,末端基團係爲鹵素及 羥基,而與均嵌段之分子量無關。因此,使用前述實例, 可製得皆具有-C1及-OH末端基團之PSSD及PSSB均嵌段 ,使其一起反應以形成具有所需分子量之嵌段共聚物。此 情況下,所形成之嵌段共聚物可含有具類似或高於均嵌段 分子量之鏈中分子量的嵌段。 前述製備均嵌段之方法可同樣使用於所有均嵌段,即 PSSD、PSU、PPSU、PSSB、P E S、T P E S、P S S、P E S K 或 TMPSS 等 〇 -19- 200724571 (16) 本發明亦教示除了所製備整嵌段共聚物中之無規均嵌 段序列外,亦可藉著調整均嵌段之分子量及進行反應以形 成該嵌段共聚物之兩均嵌段的化學計量來製得二-及-嵌 段共聚物。 本發明因此教示二-嵌段、三-嵌段及分段嵌段共聚 物之製備,其中該均嵌段可交替或存在爲無規序列。 若均嵌段分子量保持得夠低且謹慎地控制末端基團’ | 則本發明可建構在鏈中具有基本上交替之均嵌段結構的高 分子量共聚物。該等嵌段共聚物中,所有嵌段皆具有如同 兩起始均嵌段之分子量。若均嵌段分子量保持高値,則可 建構具有相對高分子量之二一及三一嵌段共聚物。 前述本發明另一重要部分係爲嵌段共聚程度z可自低 達1(二-嵌段)改變至交替或無規多嵌段共聚物的高達 1〇〇或更高。 本發明之另一重要部分係爲亦可藉著正確地控制均嵌 • 段之分子量、化學計量及末端基團而製備特定三-嵌段共 聚物。 本發明之新穎態樣係爲認知藉由改變用以製備均嵌段 之基本單體的化學計量,尤其是該均嵌段具有較低分子量 時,可使此等均嵌段主要具有已知之末端基團。因此使用 單一單體,即較DHDPS過量約3莫耳%之CSB,即莫耳 化學計量> 1.0 3 : 1 · 0 0,得到基本上僅具有-C 1末端基團 之PSSD。此因較高濃度之CSB導致存在於DHDPS上之 所有-OH基團基本上完全反應,因而限制分子量增加,而 -20 - 200724571 (17) 於均嵌段p s s D基本上僅提供-c 1末端基團。相同地,當 使用C S B製備均嵌段時使用高濃度聯苯酚,得到基本上 皆爲-OH之末端基團(其Na或K鹽形式)。基本上具有 此等酚基之PSSB不會與自身反應產生較高分子量PSSB 。相同地,具有-C1末端基團之PSSD亦無法與自身反應 產生較高分子量PSSD。此等情況下,分子量不會進一步 增加,顯示具有其他末端基團之鏈用盡。 然而,當基本上完全具有-C1末端基團之PSSD均嵌 段與基本上完全具有-OK末端基團之PSSB均嵌段混合時 ,發生進一步聚合,生成PSSB-PSSD嵌段。此反應進一 步進行導致形成具有[PSSB-PSSD]z類型結構之無規嵌段 共聚物,其中z係大於或等於i,視均嵌段之分子量及建 構之化學計量與分子量而定。 前述製備均嵌段之方法可同樣適用於所有均嵌段,即 PSSD、PSU、PPSU、PSSB、PES、T P E S、P S S、P E S K 或 TMPSS。 本發明之一重要態樣係有計劃地使用較高之兩單體比 例以製備均嵌段,產生基本上一類末端基團。該比例可爲 1.03 - 1.15: 1.00,即一種單體較第二種單體高3至15莫 耳%之量。 本發明另一重要態樣係該均嵌段亦可藉由混合、製備 具有所需組成之高分子量嵌段共聚物,在保持所需之均嵌 段分子量下,使用接近相等化學計量之兩種基本單體適當 地製備。 -21 - 200724571 (18) 本發明之重要態樣因此係製備具有已知末端基團之較 低分子量均嵌段,及其於正確比例下混合,以產生具有較 高分子量之無規嵌段共聚物。 本發明另一新穎重要態樣係製備二-及三-嵌段共聚 物。此等二-及三-嵌段賦形劑亦爲具有新穎組成之材料 。就此製劑而言,再次確認可製備具有不同分子量而具有 基本上已知之末端基團的均嵌段。通常,確知控制均嵌段 及嵌段共聚物之分子量可充分控制存在於嵌段共聚物中之 均嵌段數目,可於二或三嵌段階段停止反應。需要具有充 分高分子量或特定黏度(Inhv.)之聚颯來產生最佳機械 及其他聚合物性質,吾人可建構均嵌段分子量範圍。因此 ,具有約50000數量平均分子量(Μη)而具有-C1末端基 團之PSSD及具有約相同分子量而具有-ΟΚ末端基團之 PS SB於1 : 1莫耳比例下混合並反應時,分子量幾乎倍增 ,產生二一嵌段。分子量可使用凝膠滲透層析(GPC )連 線控制。 若使二-嵌段進一步反應產生更高分子量,則得到三 —及四一嵌段等等。因此,具有結構…[PSSB-PSSD]之二 —嵌段進一步反應產生具有結構-[--]-[-PSSB-PSSD-PSSB] 及--[-PSSD-PSSB-PSSD]之三—嵌段,其進一步反應產生 四-嵌段及更高階之多-嵌段。因此,藉著控制分子量、 化學計量及末端基團,本發明可製備PSSB及PSSD之二 -嵌段及三-嵌段及多-嵌段共聚物。 前述製備均嵌段之方法可同樣適用於所有均嵌段,即 -22- 200724571 (19) PSSD、PSU、PPSU、PSSB、PES、TPES、PSS、PESK 或 TMPSS。 本發明另可使用以下三種不同類型之均嵌段製備三嵌 段。首先使用兩種均嵌段製備二嵌段,其中存在於單一均 嵌段上之兩個末端基團係相同,相同地’第二種均嵌段之 鏈上具有兩個相同但異於第一種之末端基團。此二-嵌段 與具有兩個與第一種或第二種均嵌段相同之末端基團的弟 三種均嵌段反應,產生三-嵌段。 可檢測所製之嵌段聚合物的GPC分子量、特定黏度 、D S C、T g、M FI等,以進行品質控制。該嵌段共聚物可 於粉末形式下用於調配,之後用於造粒’或可作爲促相容 劑添加於已個別製得之高分子量同系聚楓° 本發明尋求達成以下各項: •提供具有受控之二-嵌段、三-嵌段及多-嵌段結 構之二或多種不同聚芳基楓均嵌段內容物的新穎嵌段共聚 物。 •使用此等具有低分子量及受控鏈末端基團之聚芳基 颯均嵌段製備高分子量嵌段共聚物。 •使用具有較低分子量及反應性鏈末端之均嵌段製備 高分子量二-嵌段及三一嵌段共聚物。 •製備兩種均嵌段,其各基本上僅具有鹵素或羥基末 端基團,因此在兩者間反應時產生多-嵌段共聚物,嵌段 分子量與起始均嵌段分子量相同。 •製備兩聚芳基》之嵌段共聚物,其中該兩均嵌段之 -23- 200724571 (20) 比例係爲95 : 5至5 : 95範圍內。 •製備二或更多種聚芳基颯均嵌段之嵌段共聚物,其 係透明且顯示單一中間Tg。 •使用習用注射模塑法、擠塑法或其他可接受之塑料 加工方法,製備熱安定性且可於3 5 0 °C至4 0 0 °C溫度範圍 內加工之嵌段共聚物。 •提供用以製備具有已知分子量及受控之末端基團的 聚芳基楓均嵌段的方法。 •提供一種製備低分子量受控鏈末端均嵌段之方法及 另一種製備具有二/三/多-嵌段鏈中結構之高分子量嵌 段共聚物的方法。 根據本發明,提供一種可製備低分子量、受控鏈末端 均嵌段之方法,且採用此等均嵌段製備具有高分子量之二 一、三一及多一嵌段共聚物。 本發明較佳係使用環丁颯、NMP、DMAc、DMSO、 DMS 02、二苯基颯或任何其他非質子有機溶液,以製備低 分子量均嵌段及其高分子量嵌段共聚物。較佳係使用 MCB或甲苯或任何其他非反應性溶劑作爲使用於鹽形成 、脫水及聚合步驟之稀釋劑及脫水劑。 該方法較佳係於120°C至25(TC溫度範圍內使用前述 溶劑’使用鹼諸如 NaOH、KOH、NaHC03、KHC03、Noshay and colleagues (J. Polymer Sci. A-1, 3147, 1971) have prepared block copolymers of amine terminal dimethyl methoxy oxane and hydroxyl terminal psu. The hydroxyl terminated PSU was prepared using slightly more bromine A (0.495 moles) than DCDPS (0.45 moles). This -ON a group is subsequently converted to an -OH group using oxalic acid and the product precipitates. The dried PSU powder was reacted with separately prepared amine terminal polyoxane in diethyl ether at 60 °C. It can be noted that since P S U is plastic and polyoxyalkylene is elastic, the composition produces a block copolymer having properties similar to thermoplastic elastomers. However, it is surprising that neither the described method nor the synthesis performed can form a thermoplastic block copolymer using two ruthenium blocks. The general method for preparing such polyfluorenes consists of the following processes: an aprotic organic solvent selected from cyclobutyl, N-methylpyrrolidone (NMP) or dimethyl hydrazine (DMS0) (usually on a base) Distillation) was placed in the reactor. DCDPS or any similar dihalo-based monomer (such as dichlorodiphenyldisulfonylbiphenyl (CSB), dichlorodiphenyl ketone, etc.) and a second dihydroxy monomer (biphenol, DHDPS, TMDHDS or HSB, etc.) are typically added to the reactor together with sodium carbonate or potassium carbonate at a molar ratio of 1.00: 1.00. Add toluene or monochlorobenzene (MCB) to promote dehydration. The temperature of the mixture is then gradually increased to 14 ° C to 230 ° C (depending on the solvent used). At this time, the test carbonate reacts with the phenol to produce a salt -12- 200724571 Ο) and releases water. The water is distilled off, which is increased by toluene or MCB (if present). The reaction mixture after removal of water is then heated to a temperature in the range of 170 ° C to 250 ° C (depending on the solvent, base and dihydroxy monomer used) until the desired viscosity or molecular weight is achieved. Thereafter, the chain of growth is optionally capped with MeCl, and the reaction mass is filtered to remove the salt, after which the precipitate chain is precipitated in water or MeOH, further treated to remove residual solvent φ and dried. Alternatively, the solvent may be flashed off and the reaction mass may be passed directly through a devolatilizer extruder to remove residual solvent and granulate the polymer. Addition of more than one hydroxy monomer to the foregoing produces a terpolymer in which a chain of three (but not two) monomer units is randomly incorporated. It is desirable to develop a block copolymer formation process in which two plastics, both of which are homoblocks based on ruthenium, are joined to form a single chain in the form of a block copolymer. As mentioned above, the block copolymers of different poly-Maple are unknown in the technical field. Generally, as is known in the art, the successful formation of block copolymers from the homoblocks must meet three requirements: i) the two The blocks should have terminal groups that react with each other, namely -OH & -CNO. Ii) Each homoblock should have two identical terminal groups, namely -OH or -CNO. i i i ) The two homoblocks should be mixed at the correct stoichiometric ratio to produce a local molecular weight block copolymer. The present invention discloses a process for preparing a block copolymer using two or more different poly-sand blocks, while avoiding the stringent requirements of each homoblock having substantially the same terminal group. Similarly, the need for proper stoichiometry of two or more homoblocks can be eliminated when forming high molecular weight block polymers. SUMMARY OF THE INVENTION The present invention is directed to a method of preparing a block copolymer comprising at least two homoblocks selected from the group consisting of PSSD, PSSB, TPES, PSS, TMPSS or PESK Or selected from at least one of PSSD, PSSB, TPES, PSS, TMPSS or PESK and at least one PPSU, PES or PSU, wherein the homoblocks each have at least 1 000 of the same or different molecular weight and have a total weight of at least 5%, Wherein the block copolymer has a molecular weight of at least 2000, the method step comprising: (a) by the presence of at least one base, optionally in at least one solvent, and optionally in the presence of an entraining agent, Heating at least one aromatic diol/dihydroxy compound and at least one aromatic dihalogen compound (one of which contains at least one maple group) to prepare the aforementioned various homoblocks, (b) the aforementioned homoblocks together! 3 〇 to 2 5 0. (wherein the temperature is optionally reacted in at least one solvent, and optionally the end of the block copolymer is subsequently capped, (c) the block copolymer is recovered. The invention also relates to the inlay prepared using the aforementioned method. a segment copolymer and a block copolymer comprising at least two homoblocks selected from the group consisting of p SSD, PSSB, TPES, PSS, TMPSS or pESK or selected from at least one of -14-200724571 (11) PSSD, PSSB, TPES, PSS, TMPSS or PESK and at least one PPSU, PES or PSU, directly bonded or bonded by a bonding group to form a ~block copolymer chain, wherein the homoblocks each have at least 1 000 identical Or, differing molecular weight and having a total weight of at least 5% and wherein the block copolymer has a molecular weight of at least 2000. These novel block copolymers are prepared by separately preparing a lower molecular weight homoblock. The technique of mixing and further reacting in different proportions to produce a polymer p-block copolymer. Using this technique, the formation of the block structure and its sequence and block molecular weight can be determined. In addition to the segmented multi-block compound, very High molecular weight diblock or triblock and multiblock having a known block molecular weight can be obtained by this method. The prepared block copolymer can be used as a novel polyfluorene plastic or as a compatibilizer. DESCRIPTION OF THE INVENTION In general, there are two possible chain end structures on the polymer chain of the homoblock of polyfluorene. These terminal groups are -C1 from the dihalo group (DCDPS, CSB, DCB, etc.) And a phenol monomer - a specific homoblock polymer chain may also have a mixture of both terminal groups. In the case of block copolymers, based on prior art predictions, one of the homoblocks should have only two - The C1 terminal group/chain and the second homoblock should have only two -ΟΗ terminal groups/chains. Mixing at the correct stoichiometric ratio and allowing it to react will result in a high molecular weight block copolymer. Since both homoblocks may have a -C1 or -oh mixed end group, the present invention shows that each of the homoblocks as described above may also have two identical end-15-200724571 (12) groups and Two uniform blocks must be mixed in the correct stoichiometric ratio The polyfluorene usually has a certain -C1 and some -OH end groups. The concentration of each is determined by two important factors: firstly a dihalogen compound such as DCDPS, DCB or CSB, etc. The initial molar ratio of the hydroxyphenol monomer, and secondly if the molar ratio is not exactly 1:1, the molecular weight of the polymer that can be constructed. The ratio of the two monomers is a very important factor, because the extremely high molecular weight is to be constructed, the ratio is The ohmmeter must be kept close to 1:1. Typically, the concentration of one monomer should not be about 1 to 2 moles higher than the other. Therefore, the molar ratio is usually maintained at 1.02: 1.00 to 1.00: 1.02. Inside to get a high molecular weight. Increasing the concentration of any of the monomers above this range generally results in stoichiometric disturbances to the extent that sufficient molecular weight of the copolymer cannot be constructed, and most of the polymer properties are impaired because they do not achieve optimum enthalpy. However, this harsh stoichiometry is unexpectedly not necessary when preparing oligomeric homoblocks because there is no need to construct high molecular weights. Thus, in terms of homoblock production, the present invention has successfully employed monomer ratios of up to 1.15: 1.00. The range of monomer ratios in the homoblock is thus increased from 1.02: 1.00 to 1.15: 1.00 without sacrificing the final molecular weight of the block copolymer. The present invention relates to novel poly-Maple block copolymer structures and novel methods of making the same. The invention relates in particular to the preparation of novel types of block copolymers which are prepared using PES, PPSU, PSSD, PSSB, PSS, TPES, PSU, TMPSS and PESK and similar polybenzazole blocks, and About its preparation method. The block copolymers can be made using at least two different polyfluorenes and can be made using more than two polyfluorenes. The process of the present invention comprises the use of solution polymerization techniques for the preparation of the novel polyblock-16-200724571 (13) family block copolymer. These block copolymers are prepared using relatively block (e.g., polyphenylene sulfide (PPSU), PES, - TPES, PSS, TPSSS, PSU, and PESK) - an important aspect of the present invention is related to the present invention. High glass transition temperature block copolymer. The embedded (> 22 0 °C) and rigorous chemical environments maintain pharmaceutically acceptable properties. The block copolymers disclosed in the prior art have a temperature of § and therefore can only be used for applications requiring continuous use, and cannot be used in high temperature applications such as luminaire materials and other articles exposed to thermal and mechanical stress. The main novel and unexpected aspect of the process of the invention is to give a homoblock having only a stoichiometric requirement of a 1:1 stoichiometry between one of the two terminal groups. High molecular weight block copolymers can be prepared, each embedding end groups and not strictly controlled stoichiometry. Due to the formation of oxime block copolymers. Moreover, the present invention makes it easier to use a block copolymer composition having a relatively large composition range as compared with the earlier preparation method. Of course, the homoblocks of the terminal groups are made and have the correct stoichiometry, but these conditions are no longer the construction of high molecular weight inlays. This method also allows for proper control of the terminal polymers, wherein the two are embedded. The segments have various molecular weights and have a wide range of compositions, and this point is discussed earlier in the low molecular weight oligomerization PSSB, PSSD, ί ° species with high flexural temperature copolymers at lower temperatures. The shell and space composites having a heat deflection of less than 180 ° C are not obeying the uniform block used, and the method of the present invention does not have the substantially simple segmented block copolymer of the present invention. The block is prepared by using a premise group having the same final ratio and never injuring the copolymer to prepare a block copolymer copolymer. Other types of blocks may be difficult or even in the -17-200724571 (14) polymer. It is impossible to achieve. Novel block copolymers are prepared by first using lower molecular weight homoblocks of the original individually prepared functional end chain groups. The term "all-in-segment." means that each block has PES or PSSB or TPES or PSSD or PPSU or TMPSS or PSS, PSU or PESK or some of such poly-Maple structures, and different homoblocks have structures different from each other. . The two homoblocks are individually prepared and arranged to have two sequential or distinct terminal groups. The heavy P point is the two-phase hetero-end group (in this case -C1 and -OH) to achieve the teachings of the present invention, and of course should be close to the stoichiometric equilibrium. It is important that both end groups are present on both homoblocks. The different ways of preparing the homoblocks are as follows: The first group of homoblocks is prepared to have predominantly halogen terminal groups such as -F, -Cl, -Br and -I. The second group of homoblocks is prepared to have predominantly a second terminal group which is reactive with a halogen terminal group such as -OH (which may be present in the form of a salt - OK, -ONa or -OLi). This is done in the first case by using a dihalogen monomer that is a large molar excess compared to the dihydroxy monomer, and in the second case it is swapped. Generally, when a lower molecular weight homoblock having mainly the first terminal group is reacted with another homoblock having mainly the second terminal group, a block copolymer having a high molecular weight is obtained. Thus, for example, a low molecular weight PSSB homoblock having predominantly an -OH end group reacts with a low molecular weight PSSD homoblock having predominantly a -C1 terminal group to produce [PSSD-PSSB]z in the block copolymer sequence or A novel block copolymer of {[PSSB...PSSD]z}. When a homoblock has predominantly identical terminal groups (eg, -C1) and reacts with a second homoblock having predominantly a second -18-200724571 (15) terminal group (eg, -OH), The resulting block copolymer has a PSSD & PSSB embedded segment with a molecular weight like the starting homoblock. The present invention thus makes it possible to make the molecular weight of the homoblock almost the same as the block which becomes a part of the chain. It is also possible according to the invention to prepare a block copolymer in which the homoblock of the PSSD has a halogen end group and the PSSB homoblock has a phenol-oh end group, and conversely wherein the PSSD has a hydroxyl end group and the PSSB has a halogen. a block copolymer of a terminal group. As shown in the present invention, the terminal groups of a particular homoblock can be exchanged with each other. When each homoblock has a different terminal group (e.g., -C1 and -OH), it is important to have a relatively identical stoichiometry in both homoblocks. When one or two high molecular weight homoblocks are produced, it is important that the two terminal groups remain as dissimilar as possible as in the two-block and three-block preparation. However, the present invention allows both homoblocks to have both terminal groups and still be used to make high molecular weight block copolymers. This can be achieved by using two monomers that are close to the same • Moerby. In this case, the terminal groups are halogen and hydroxyl groups, regardless of the molecular weight of the homoblock. Thus, using the foregoing examples, PSSD and PSSB homoblocks having both -C1 and -OH end groups can be prepared which are reacted together to form a block copolymer having the desired molecular weight. In this case, the block copolymer formed may contain a block having a chain molecular weight similar to or higher than the homoblock molecular weight. The foregoing method for preparing the homoblocks can be equally applied to all homoblocks, ie, PSSD, PSU, PPSU, PSSB, PES, TPES, PSS, PESK or TMPSS, etc. -19-200724571 (16) The present invention also teaches that in addition to the preparation In addition to the random average block sequence in the monoblock copolymer, it is also possible to produce a di- and - by adjusting the molecular weight of the homoblock and reacting to form the stoichiometry of the two homoblocks of the block copolymer. Block copolymer. The present invention thus teaches the preparation of di-block, tri-block and segmented block copolymers wherein the homoblocks are alternating or present in a random sequence. If the homoblock molecular weight is kept low enough and the terminal groups are carefully controlled, then the present invention can construct a high molecular weight copolymer having substantially alternating homoblock structures in the chain. In the block copolymers, all of the blocks have the same molecular weight as the two starting homoblocks. If the homoblock molecular weight is kept high, a di- and tri-block copolymer having a relatively high molecular weight can be constructed. Another important aspect of the foregoing invention is that the degree of block copolymerization z can vary from as low as 1 (di-block) to as much as 1 Torr or higher of alternating or random multi-block copolymers. Another important aspect of the present invention is the ability to prepare specific tri-block copolymers by properly controlling the molecular weight, stoichiometry, and terminal groups of the intercalated segments. The novel aspect of the present invention is to recognize the stoichiometry of the basic monomer used to prepare the homoblock, especially when the homoblock has a lower molecular weight, such that the homoblocks have predominantly known ends Group. Thus, a single monomer, i.e., about 3 moles of CSB in excess of DHDPS, i.e., molar stoichiometry > 1.0 3 : 1 · 0 0 , was used to obtain a PSSD having substantially only a -C 1 terminal group. This results in a substantially complete reaction of all -OH groups present on the DHDPS due to the higher concentration of CSB, thus limiting the molecular weight increase, while -20 - 200724571 (17) provides only the -c 1 terminus in the homoblock pss D Group. Similarly, when a homoblock is prepared using C S B , a high concentration of biphenol is used to obtain terminal groups (which are in the form of Na or K salts) which are substantially all -OH. A PSSB having substantially these phenolic groups does not react with itself to produce a higher molecular weight PSSB. Similarly, a PSSD having a -C1 terminal group is also unable to react with itself to produce a higher molecular weight PSSD. In these cases, the molecular weight does not increase further, indicating that the chain with other terminal groups is used up. However, when a PSSD homoblock having substantially a -C1 terminal group is substantially block-mixed with a PSSB substantially completely having an -OK end group, further polymerization occurs to form a PSSB-PSSD block. This reaction is further carried out to form a random block copolymer having a structure of the [PSSB-PSSD]z type, wherein the z system is greater than or equal to i, depending on the molecular weight of the homoblock and the stoichiometry and molecular weight of the structure. The foregoing method of preparing the homoblocks is equally applicable to all homoblocks, i.e., PSSD, PSU, PPSU, PSSB, PES, T P E S, P S S, P E S K or TMPSS. An important aspect of the present invention is the systematic use of a higher ratio of two monomers to produce a homoblock, resulting in a substantially class of terminal groups. The ratio may be from 1.03 to 1.15: 1.00, i.e., one monomer is from 3 to 15 mol% higher than the second monomer. Another important aspect of the present invention is that the homoblock can also be prepared by mixing and preparing a high molecular weight block copolymer having a desired composition, while maintaining a desired uniform block molecular weight, using nearly equal stoichiometry. The basic monomers are suitably prepared. -21 - 200724571 (18) An important aspect of the present invention is therefore to prepare lower molecular weight homoblocks having known terminal groups and to mix them at the correct ratio to produce random block copolymers having higher molecular weights. Things. Another novel and important aspect of the invention is the preparation of di- and tri-block copolymers. These di- and tri-block excipients are also materials of novel composition. For this formulation, it has again been confirmed that homoblocks having different molecular weights and having substantially known terminal groups can be prepared. In general, it is known that controlling the molecular weight of the homoblock and the block copolymer can sufficiently control the number of homoblocks present in the block copolymer, and the reaction can be stopped in the di- or triblock stage. Polymers with sufficient high molecular weight or specific viscosity (Inhv.) are required to produce optimum mechanical and other polymer properties, and we can construct a homoblock molecular weight range. Therefore, when the PSSD having a number average molecular weight (Μη) of about 50,000 and having a -C1 terminal group and PS SB having about the same molecular weight and having a -ΟΚ terminal group are mixed and reacted at a molar ratio of 1:1, the molecular weight is almost Multiply, producing a two-block. The molecular weight can be controlled using gel permeation chromatography (GPC). If the di-block is further reacted to produce a higher molecular weight, a tri- and tetra-block is obtained. Therefore, having the structure...[PSSB-PSSD] bis-block further reacts to produce a tri-block having the structure -[--]-[-PSSB-PSSD-PSSB] and --[-PSSD-PSSB-PSSD] Further reaction produces a tetra-block and a higher order poly-block. Thus, by controlling molecular weight, stoichiometry, and terminal groups, the present invention can prepare diblock- and tri-block and multi-block copolymers of PSSB and PSSD. The foregoing method for preparing the homoblocks is equally applicable to all homoblocks, i.e., -22-200724571 (19) PSSD, PSU, PPSU, PSSB, PES, TPES, PSS, PESK or TMPSS. The present invention can also be used to prepare three blocks using the following three different types of homoblocks. The diblock is first prepared using two homoblocks, wherein the two terminal groups present on a single homoblock are identical, and the same as the 'second homoblock' has two identical but different from the first End group. This di-block reacts with three homoblocks having two terminal groups identical to the first or second homoblock to produce a tri-block. The GPC molecular weight, specific viscosity, D S C, T g, M FI, etc. of the block polymer produced can be detected for quality control. The block copolymers can be formulated in powder form for subsequent granulation or can be added as a compatibilizing agent to the individually prepared high molecular weight homologues. The present invention seeks to achieve the following: Novel block copolymers having two or more different polyaryl maple block contents of controlled di-block, tri-block and multi-block structures. • Preparation of high molecular weight block copolymers using such polyaryl ruthenium blocks having low molecular weight and controlled chain end groups. • Preparation of high molecular weight di-block and tri-block copolymers using homoblocks with lower molecular weight and reactive chain ends. • Preparation of two homoblocks, each of which essentially has only a halogen or hydroxyl end group, thus producing a multi-block copolymer when reacted between the two, the block molecular weight being the same as the initial homoblock molecular weight. • Preparation of a block copolymer of a dimeric aryl group wherein the ratio of -23-200724571 (20) of the two homoblocks is in the range of 95:5 to 5:95. • A block copolymer of two or more polyarylfluorene homoblocks is prepared which is transparent and exhibits a single intermediate Tg. • Prepare block copolymers that are thermally stable and processable at temperatures ranging from 350 ° C to 400 ° C using conventional injection molding, extrusion or other acceptable plastic processing methods. • A method for preparing a polyaryl maple homoblock having a known molecular weight and a controlled end group. • A method of preparing a low molecular weight controlled chain terminal homoblock and another method of preparing a high molecular weight block copolymer having a structure in a di/tri/multi-block chain are provided. According to the present invention, there is provided a process for preparing a low molecular weight, controlled chain terminal homoblock, and the use of such homoblocks to prepare a di-, tri-, and poly-block copolymer having a high molecular weight. Preferably, the invention utilizes cyclobutyl hydrazine, NMP, DMAc, DMSO, DMS 02, diphenyl hydrazine or any other aprotic organic solution to produce low molecular weight homoblocks and high molecular weight block copolymers thereof. Preferably, MCB or toluene or any other non-reactive solvent is used as the diluent and dehydrating agent for the salt formation, dehydration and polymerization steps. The method is preferably carried out at a temperature of from 120 ° C to 25 (using the aforementioned solvent in the temperature range of TC) using a base such as NaOH, KOH, NaHC03, KHC03,

Na2C03或K2C03本身或此等之組合物或任何其他該種適 當之鹼物質。 根據本發明,提供一種製造新穎均嵌段及多-嵌段共 -24- 200724571 (21) 聚物之方法,其係於120 °C至25 0 °C溫度範圍內使用非質 子有機溶劑或溶劑且之後使用MeCl或任何適當之末端封 - 蓋劑進行末端封蓋。該方法係包括以下較佳步驟:過濾該 、 鹽並於非溶劑(如H20或MeOH或兩者之混合物)中自 反應混合物沉澱析出嵌段共聚物,之後進一步水/或 MeOH處理以降低粉末之殘留溶劑含量,之後乾燥該聚合 物粉末。 φ 現在參考以下實施例描述本發明。說明本發明之具體 實施例不應視爲限制其範圍。 【實施方式】 實施例: 實施例1: TPSS: 50: 50PSSD: PSSB之嵌段共聚物 使用以下三部分方法製備此種TPSS ( PSSD-PSSB ) 嵌段共聚物。 第1部分:PSSD均嵌段之製備 PSSD係使用DHDPS及CSB作爲單體而製得。 4頸3公升玻璃燒瓶裝置頂部攪拌器,連接貫穿其中 心頸部之不銹鋼攪拌槳。經由一側頸連接CloisonnS接頭 。Cloisonn6接頭之另一頸連接於Dean-Stark汽水閥及水 -冷卻冷凝器。經另一側頸插入熱偶溫度計。另一個側頸 則插入氮氣入口。該燒瓶置入油浴中,其係連接於溫度控 制器。 -25- 200724571 (22) 將環丁颯(4410克,3500毫升/莫耳)及甲苯(1000 毫升/莫耳)置入燒瓶中’連繪通以氮氣泡,加熱至45 °C 。將4,4’雙[(4 一氯苯基)磺醯基]聯苯(CSB) (523克 )及4,4’二羥基二苯基颯(DHDPS) ( 250克)添加於燒 瓶中,CSB : DHDPS係爲1·〇4 : 1.00莫耳比,反應混合 物攪拌3 0分鐘。添加無水碳酸鈉(12 3克)。藉氣洗於 燒瓶中保持氮氛圍。甲苯係作爲共沸溶劑。反應物之溫度 | 係以5小時緩緩增加至220°C,攪拌速度設定於400 rpm 。因爲Na2C03與DHDPS反應所形成之水係以與甲苯之共 沸物形式餾除且收集於Dean-Stark汽水閥中。甲苯一旦 與水分離即送回反應混合物。一旦完全移除水,則停止將 甲苯添加回反應器。之後隨著反應物溫度增加自該反應混 合物完全移除甲苯。在5小時後達到所需溫度。之後將反 應溫度保持於220°C,當黏度開始增加時,攪拌速度提高 至 500 rpm。在所需之 Μη 17,000,Mw 約 20,000 且 MWD I 1.19下,藉著將溫度降低至< 130°c而停止反應。CSB對 DHDPS之相對高莫耳比產生具有相對低分子量且主要具 有-Ph-Cl末端基團之PSSD。 第2部分:PSSB均嵌段之製備 PS SB係使用聯苯酚及CSB作爲單體製得。 將環丁颯(4410克,3500毫升/莫耳)及甲苯(1〇〇〇 毫升/莫耳)置入燒瓶中,連續通以氮氣泡,加熱至45°C 。將4,4’雙[(4 一氯苯基)磺醯基]聯苯(CSB) (503克 -26- 200724571 (23) )及聯苯酚(1 8 8克)添加於燒瓶中,聯苯酚:C S B係爲 1.01 : 1_00莫耳比,反應混合物攪拌30分鐘。添加無水 碳酸鈉(1 23克)。甲苯係作爲共沸溶劑。反應物之溫度 係以5小時緩緩增加至220°C,攪拌速度設定於400 rpm 。因爲反應所形成之水係以與甲苯之共沸物形式餾除且收 集於Dean-Stark汽水閥中。甲苯一旦與水分離即送回反 應混合物。一旦完全移除水,則停止將甲苯添加回反應器 P 。之後隨著反應物溫度增加自該反應混合物完全移除甲苯 。在4小時後達到所需溫度。之後將反應溫度保持於220 °C,當黏度開始增加塒,攪拌速度提高至5 00 rpm。在所 需之 Mn 29,000,Mw 約 3 8,000 且 MWD 1.31 下,迅速冷 卻反應物質以停止進一步聚合。聯苯酚對CSB之相對高 莫耳比產生具有相對低分子量且主要具有-Ph-OH末端基 團之PSSB 。 第3部分:嵌段共聚物之製備 第1部分及第2部分之反應混合物於等重量比例下混 合,於220°C進行嵌段聚合。達到所需之MW (如GPC所 示)後,反應混合物以環丁礪(504克,400毫升/莫耳) 中止反應,溫度降至2 1 0 °C。之後使甲基氯氣體冒泡通經 反應混合物歷經3小時,以確定完成末端封蓋。反應混合 物隨之以環丁颯(400毫升/莫耳)稀釋第二次。聚合物溶 液於壓濾器漏斗中使用2公斤/厘米2氮壓力經1 5微米濾 器過濾以移除鹽類。最後藉著於高速攪拌下緩緩添加不含 -27- 200724571 (24) 鹽之聚合物溶液於去離子水(1 3毫升/克聚合物)中而 回收嵌段共聚物。之後藉過濾回收沉澱之聚合物。沉澱之 聚合物經硏磨且於90 °C使用去離子水回流三次,以完全 移除所有鹽類及環丁楓。之後過濾沉澱之聚合物並於1 40 °C爐中乾燥,直至藉Karl Fischer滴定決定之水含量< 0.5%。 嵌段共聚物基於聚苯乙烯標準物之GPC分析顯示Μη 爲 88,000,Mw 爲 121,000 且 MWD 爲 1.37。因此,所製 之共聚物具有遠高於作爲單體單元之兩均嵌段的分子量, 表示製備嵌段共聚物。嵌段共聚物粉末隨後與0.25%熱安 定劑混合且使用雙螺桿擠塑機造粒。PSSD之Tg及比重個 別係爲25 9°C及1.29,而高分子量PSSB本身係爲27(TC 及1.3 20。嵌段共聚物(TPSS )之透明顆粒顯示DSC Tg 爲266 °C且比重爲1.31。產物之顆粒透明性、單一 GPC 波峰、中間Tg及比重明確顯示確實已形成PSSD及PSSB 之嵌段共聚物且產物不僅是兩均聚物PSSD及PP SB之摻 合物。詳細性質列於表1。詳細化學反應表示於(圖I ) 實施例2: TPSS : 90: 10 PSSD : PSSB嵌段共聚物 使用以下三部分方法製備TPSS(PSSD: PSSB)嵌段 共聚物。 第1部分:PSSD均嵌段之製備 -28- 200724571 (25) PSSD係使用DHDPS及CSB作爲單體而製得。 使用如同實施例1所述之實驗配置。 將環丁颯(1687克,1500毫升/莫耳)及甲苯(700 毫升/莫耳)置入燒瓶中,連續通以氮氣泡,加熱至45 °C 。將4,4’雙[(4 一氯苯基)磺醯基]聯苯(CSB) (461克 )及4,4’二羥基二苯基颯(DHDPS) ( 225克)添加於燒 瓶中,CSB : DHDPS係爲 1.02 : 1.00莫耳比,反應混合 物攪拌3 0分鐘。添加無水碳酸鈉(1 1 2 · 5克)。藉氣洗於 燒瓶中保持氮氛圍。甲苯係作爲共沸溶劑。 其餘方法係與實施例1第1部分所述者相同。所得之 均嵌段具有GPC分子量Μη 17,000,Mw 23,000且MWD 1 ·36。 第2部分:PS SB均嵌段之製備 PSSB係使用聯苯酚及CSB作爲單體製得。 • 將環丁楓(437克,3500毫升/莫耳)及甲苯(1000 毫升/莫耳)置入燒瓶中,連續通以氮氣泡,加熱至45 °C 。將4,4,雙[(4 一氯苯基)磺醯基]聯苯(CSB) (50.8克 )及聯苯酚(18.6克)添加於燒瓶中,聯苯酚:CSB係爲 1· 〇1 : 1.00莫耳比,反應混合物攪拌30分鐘。添加無水 碳酸鈉(1 2 · 5克)。 其餘方法係與實施例1第2部分所述者相同。所得之 均嵌段具有GPC分子量Μη 10,000,Mw 12,000且MWD 1.20。 29 - 200724571 (26) 第3部分:嵌段共聚物之製備 混合第1部分(9份)及第2部分(1份)之反應混 合物,於22(TC進行嵌段聚合。達到所需之MW (如GPC 所示)後,反應混合物以環丁楓(504克,400毫升/莫耳 )中止反應,溫度降至210 °C。之後使甲基氯氣體冒泡通 經反應混合物歷經3小時,以確定完成末端封蓋。反應混 合物隨之以環丁礪(400毫升/莫耳)稀釋第二次。聚合物 溶液於壓濾器漏斗中使用2公斤/厘米2氮壓力經1 5微米 濾器過濾以移除鹽類。最後藉著於高速攪拌下緩緩添加不 含鹽之聚合物溶液於去離子水(1 3毫升/克聚合物)中 而回收嵌段共聚物。之後藉過濾回收沉澱之聚合物。沉澱 之聚合物經硏磨且於90 °C使用去離子水回流三次,以完 全移除所有鹽類及環丁楓。之後過濾沉澱之聚合物並於 140°C爐中乾燥,直至藉Karl Fischer滴定決定之水含量 < 0.5%。 嵌段共聚物基於聚苯乙烯標準物之GPC分析顯示Μη 爲 90,000,Mw 爲 131,000 且 M WD 爲 1.37。因此,所製 之共聚物具有遠高於作爲單體單元之兩均嵌段的分子量, 表示製備嵌段共聚物。嵌段共聚物粉末隨後與0.25%熱安 定劑混合且使用雙螺桿擠塑機造粒。PSSD之Tg及比重個 別係爲260 °C及1.29,而PSSB者係爲270 °C及1.330。嵌 段共聚物之透明顆粒顯示DSC Tg爲266 °C且比重爲1.34 。產物之顆粒透明性、單一 G P C波峰、中間T g及比重明 -30- 200724571 (27) TPSS ) 詳細性 確顯示確實已形成PSSD及PSSB之嵌段共聚物( 且產物不僅是兩均聚物PSSD及PPSB之摻合物。 質列於表1。 實施例3: DPSS: 50: 50 PSSD: PSS之嵌段共聚: 嵌段共 使用以下三部分方法製備DPSS(PSSD-PSS) 聚物。Na2C03 or K2C03 itself or a combination of these or any other such suitable base material. According to the present invention, there is provided a process for the manufacture of a novel homoblock and multi-block co--24-200724571 (21) polymer which is used in an aprotic organic solvent or solvent at a temperature ranging from 120 ° C to 25 ° C. The end capping is then carried out using MeCl or any suitable end capping-capping agent. The method comprises the following preferred steps: filtering the salt, and precipitating the block copolymer from the reaction mixture in a non-solvent such as H20 or MeOH or a mixture of the two, followed by further water/MeOH treatment to reduce the powder. The solvent content is residual, after which the polymer powder is dried. φ The invention will now be described with reference to the following examples. It is to be understood that the specific embodiments of the invention are not to be construed as limiting. EXAMPLES Example: Example 1: TPSS: 50: 50PSSD: Block copolymer of PSSB This TPSS (PSSD-PSSB) block copolymer was prepared using the following three-part method. Part 1: Preparation of PSSD homoblocks PSSD was prepared using DHDPS and CSB as monomers. A 4-neck 3 liter glass flask with an overhead stirrer connected to a stainless steel paddle that runs through the center of the heart. Connect the CloisonnS connector via one side neck. The other neck of the Cloisonn6 connector is connected to the Dean-Stark soda valve and the water-cooling condenser. Insert the thermocouple thermometer through the other side of the neck. The other side neck is inserted into the nitrogen inlet. The flask was placed in an oil bath which was attached to a temperature controller. -25- 200724571 (22) Put cyclopentanthene (4410 g, 3500 ml/mole) and toluene (1000 ml/mole) into the flask' and draw with nitrogen bubbles and heat to 45 °C. 4,4' bis[(4-chlorophenyl)sulfonyl]biphenyl (CSB) (523 g) and 4,4' dihydroxydiphenyl hydrazine (DHDPS) (250 g) were added to the flask. CSB: DHDPS is 1·〇4: 1.00 mol ratio, and the reaction mixture is stirred for 30 minutes. Anhydrous sodium carbonate (123 g) was added. Wash in a flask to maintain a nitrogen atmosphere. Toluene is used as an azeotropic solvent. The temperature of the reactants was gradually increased to 220 ° C in 5 hours, and the stirring speed was set at 400 rpm. The water system formed by the reaction of Na2C03 with DHDPS was distilled off in the form of azeotrope with toluene and collected in a Dean-Stark soda valve. The toluene is returned to the reaction mixture once it is separated from the water. Once the water is completely removed, the addition of toluene to the reactor is stopped. Toluene was then completely removed from the reaction mixture as the temperature of the reactants increased. The desired temperature was reached after 5 hours. The reaction temperature was then maintained at 220 ° C and the agitation speed was increased to 500 rpm as the viscosity began to increase. At the desired Μ 17,000, Mw of about 20,000 and MWD I 1.19, the reaction was stopped by lowering the temperature to < 130 °c. The relatively high molar ratio of CSB to DHDPS produces a PSSD having a relatively low molecular weight and predominantly having a -Ph-Cl end group. Part 2: Preparation of PSSB homoblocks PS SB is prepared using biphenol and CSB as monomers. Cyclopentane (4410 g, 3500 ml/mole) and toluene (1 ml/mol) were placed in a flask, and nitrogen bubbles were continuously passed through and heated to 45 °C. Add 4,4' bis[(4-chlorophenyl)sulfonyl]biphenyl (CSB) (503 g-26-200724571 (23)) and biphenol (1 8 8 g) to the flask, biphenol : CSB was 1.01 : 1_00 molar ratio, and the reaction mixture was stirred for 30 minutes. Anhydrous sodium carbonate (1 23 g) was added. Toluene is used as an azeotropic solvent. The temperature of the reactant was gradually increased to 220 ° C in 5 hours, and the stirring speed was set at 400 rpm. The water formed by the reaction was distilled off in the form of an azeotrope with toluene and collected in a Dean-Stark soda valve. The toluene is returned to the reaction mixture once it is separated from the water. Once the water is completely removed, the addition of toluene to the reactor P is stopped. Toluene was then completely removed from the reaction mixture as the temperature of the reactants increased. The desired temperature was reached after 4 hours. After that, the reaction temperature was maintained at 220 ° C. When the viscosity began to increase, the stirring speed was increased to 500 rpm. At the desired Mn 29,000, Mw of about 38,000 and MWD 1.31, the reaction mass was rapidly cooled to stop further polymerization. The relatively high molar ratio of biphenol to CSB produces a PSSB having a relatively low molecular weight and predominantly having a -Ph-OH end group. Part 3: Preparation of block copolymer The reaction mixture of the first part and the second part was mixed at an equal weight ratio, and block polymerization was carried out at 220 °C. After the desired MW (as indicated by GPC) was reached, the reaction mixture was quenched with cyclohexane (504 g, 400 mL/m) and the temperature was reduced to 210 °C. Methyl chloride gas was then bubbled through the reaction mixture over a period of 3 hours to determine completion of the end cap. The reaction mixture was then diluted a second time with cyclobutyl hydrazine (400 ml/mole). The polymer solution was filtered through a 15 micron filter using a 2 kg/cm 2 nitrogen pressure in a filter press funnel to remove salts. Finally, the block copolymer was recovered by slowly adding a polymer solution containing no salt of -27-200724571 (24) in deionized water (13 ml/g polymer) under high-speed stirring. The precipitated polymer is then recovered by filtration. The precipitated polymer was honed and refluxed three times with deionized water at 90 °C to completely remove all salts and butyl sulphate. The precipitated polymer was then filtered and dried in an oven at 1400 °C until the water content determined by Karl Fischer titration < 0.5%. GPC analysis of the block copolymer based on polystyrene standards showed a Μη of 88,000, a Mw of 121,000 and an MWD of 1.37. Therefore, the copolymer produced has a molecular weight far higher than the two homoblocks as monomer units, indicating the preparation of the block copolymer. The block copolymer powder was then mixed with 0.25% thermal stabilizer and granulated using a twin screw extruder. The Tg and specific gravity of PSSD are 25 9 ° C and 1.29, while the high molecular weight PSSB itself is 27 (TC and 1.3 20 . The transparent particles of block copolymer (TPSS ) show DSC Tg of 266 ° C and specific gravity of 1.31. The particle transparency of the product, the single GPC peak, the intermediate Tg and the specific gravity clearly indicate that the block copolymer of PSSD and PSSB has indeed been formed and the product is not only a blend of the two homopolymers PSSD and PP SB. The detailed properties are listed in the table. 1. Detailed chemical reaction is shown in (Figure I) Example 2: TPSS: 90: 10 PSSD: PSSB block copolymer The TPSS (PSSD: PSSB) block copolymer was prepared using the following three methods: Part 1: PSSD Preparation of Blocks -28- 200724571 (25) PSSD was prepared using DHDPS and CSB as monomers. The experimental configuration as described in Example 1 was used. Ring oxime (1687 g, 1500 ml/mole) and Toluene (700 ml/mole) was placed in a flask, continuously bubbled with nitrogen, and heated to 45 ° C. 4,4' bis[(4-chlorophenyl)sulfonyl]biphenyl (CSB) (461克) and 4,4' dihydroxydiphenyl hydrazine (DHDPS) (225 g) were added to the flask, CSB: DHDPS was 1.02 : 1.0 0 molar ratio, the reaction mixture was stirred for 30 minutes. Anhydrous sodium carbonate (1 1 2 · 5 g) was added, and the mixture was purged with air to maintain a nitrogen atmosphere. Toluene was used as an azeotropic solvent. The remaining method was the same as in Example 1. The homoblock obtained has the same GPC molecular weight 1η 17,000, Mw 23,000 and MWD 1 · 36. Part 2: Preparation of PS SB homoblocks PSSB is prepared using biphenol and CSB as monomers. • Place Cyclosporin (437 g, 3500 ml/mole) and toluene (1000 ml/mole) in a flask with continuous nitrogen bubbles and heat to 45 ° C. 4, 4, double [(4) Monochlorophenyl)sulfonyl]biphenyl (CSB) (50.8 g) and biphenol (18.6 g) were added to the flask, biphenol: CSB was 1·〇1: 1.00 mol ratio, and the reaction mixture was stirred 30 Anhydrous sodium carbonate (1 2 · 5 g) was added. The remaining methods were the same as those described in Example 2, Part 2. The resulting homoblock had a GPC molecular weight of 10,000 10,000, Mw 12,000 and MWD 1.20. 29 - 200724571 ( 26) Part 3: Preparation of block copolymers Mix the first part (9 parts) and the second part (1 part) The mixture should be subjected to block polymerization at 22 (TC). After reaching the desired MW (as indicated by GPC), the reaction mixture was quenched with cyclohexane (504 g, 400 ml/mol) and the temperature was lowered to 210 °C. . Methyl chloride gas was then bubbled through the reaction mixture over a period of 3 hours to determine completion of the end cap. The reaction mixture was then diluted a second time with cyclobutyl hydrazine (400 ml/mole). The polymer solution was filtered through a 15 micron filter using a 2 kg/cm 2 nitrogen pressure in a filter press funnel to remove salts. Finally, the block copolymer was recovered by slowly adding a salt-free polymer solution to deionized water (13 ml/g polymer) under high-speed stirring. The precipitated polymer is then recovered by filtration. The precipitated polymer was honed and refluxed three times with deionized water at 90 °C to completely remove all salts and Cyclopentane. The precipitated polymer was then filtered and dried in a 140 ° C oven until the water content determined by Karl Fischer titration < 0.5%. GPC analysis of the block copolymer based on polystyrene standards showed a Μη of 90,000, a Mw of 131,000 and a M WD of 1.37. Therefore, the copolymer produced has a molecular weight far higher than the two homoblocks as monomer units, indicating the preparation of the block copolymer. The block copolymer powder was then mixed with 0.25% thermal stabilizer and granulated using a twin screw extruder. The Tg and specific gravity of PSSD are 260 °C and 1.29, while those of PSSB are 270 °C and 1.330. The transparent particles of the block copolymer showed a DSC Tg of 266 ° C and a specific gravity of 1.34. Particle transparency of the product, single GPC peak, intermediate T g and specific gravity -30- 200724571 (27) TPSS ) The detail shows that the block copolymer of PSSD and PSSB has indeed been formed (and the product is not only the two homopolymer PSSD) And the blend of PPSB. The mass is listed in Table 1. Example 3: DPSS: 50: 50 PSSD: Block copolymerization of PSS: The block was prepared using the following three-part method to prepare DPSS (PSSD-PSS) polymer.

第1部分:PSSD均嵌段之製備 PSSD係使用DHDPS及CSB作爲單體而製得' 使用如同實施例1所述之實驗配置。 將環丁颯(4410克,3 500毫升/莫耳)及甲薄 晕:升/莫耳)置入燒瓶中,連續通以氮氣泡,加熱 。將4,4’雙[(4 一氯苯基)磺醯基]聯苯(CSB)( )及4,4’二羥基二苯基礪(DHDPS ) ( 25 0克)簿 瓶中,CSB: DHDPS係爲1·04: 1·〇〇莫耳比,反 物攪拌3 0分鐘。添加無水碳酸鈉(1 23克)。藉 燒瓶中保持氮氛圍。甲苯係作爲共沸溶劑。 其餘方法係與實施例1第1部分所述者相同。 均嵌段具有GPC分子量Μη 20,000,Mw 22,000 1.10。 第2部分:PSS均嵌段之製備 PSS係使用HSB及CSB作爲單體製得。Part 1: Preparation of PSSD homoblocks PSSD was prepared using DHDPS and CSB as monomers. The experimental setup as described in Example 1 was used. Ring guanidine (4410 g, 3 500 ml/mole) and a halo: liter/mole were placed in a flask, and nitrogen bubbles were continuously passed through and heated. 4,4' bis[(4-chlorophenyl)sulfonyl]biphenyl (CSB) ( ) and 4,4' dihydroxydiphenyl hydrazine (DHDPS) (250 g) in a bottle, CSB: The DHDPS system was 1·04: 1·〇〇 molar ratio, and the anti-object was stirred for 30 minutes. Anhydrous sodium carbonate (1 23 g) was added. The nitrogen atmosphere was maintained in the flask. Toluene is used as an azeotropic solvent. The remaining methods are the same as those described in the first part of Example 1. The homoblock has a GPC molecular weight Μ 20,000, Mw 22,000 1.10. Part 2: Preparation of PSS homoblocks PSS is prepared using HSB and CSB as monomers.

(1000 ? 4 5°c 523克 加於燒 應混合 氣洗於 所得之 MWD -31 - 200724571 (28) 將環丁颯(44 10克,3500毫升/莫耳)及甲苯(⑺⑽ 毫升/莫耳)置入燒瓶中,連續通以氮氣泡’加熱至45 °C 。將4,4,雙[(4 —氯苯基)磺醯基]聯苯(CSB ) ( 503克 )及4,4’雙[(4 一羥基苯基)磺醯基]聯苯酚(HSB)( 471克)添加於燒瓶中,HSB: CSB係爲1·〇1: 1.00莫耳 比,反應混合物攪捽3 0分鐘。添加無水碳酸鈉(1 2 3克 )。甲苯作爲共沸溶劑。 其餘方法係與實施例1第2部分所述者相同。所得之 均嵌段具有GPC分子量Μη 29,000,Mw 38,000且MWD 1.31。 第3部分:嵌段共聚物之製備 於等重量比例下混合第1部分及第2部分之反應混 合物,於23 0°C進行嵌段聚合。達到所需之MW (如GPC 所示)後,反應混合物以環丁颯(504克,400毫升/莫耳 )中止反應,溫度降至2 1 0 °C。之後使甲基氯氣體冒泡通 經反應混合物歷經3小時,以確定完成末端封盡。反應混 合物隨之以環丁颯(400毫升/莫耳)稀釋第二次。聚合物 溶液於壓濾器漏斗中使用2公斤/厘米2氮壓力經1 5微米 濾器過濾以移除鹽類。最後藉著於高速攪拌下緩緩添加不 含鹽之聚合物溶液於去離子水(1 3毫升/克聚合物)中 而回收嵌段共聚物。之後藉過濾回收沉澱之聚合物。沉澱 之聚合物經硏磨且於90 °C使用去離子水回流三次,以完 全移除所有鹽類及環丁颯。之後過濾沉澱之聚合物並於 -32- 200724571 (29) 140°C爐中乾燥,直至藉Karl Fischer滴定決定之水含量 < 0.5%。 • 嵌段共聚物基於聚苯乙烯標準物之GPC分析顯示Μη . 爲 89,000,Mw 爲 122,000 且 MWD 爲 1.37。因此,所製 之共聚物具有遠高於作爲單體單元之兩均嵌段的分子量, 表示製備嵌段共聚物。嵌段共聚物粉末隨後與0.25%熱安 定劑混合且使用雙螺桿擠塑機造粒。P S S D之T g及比重個 • 別係爲259 °C及1.29,而PSS者係爲270 °C及1.32。嵌段 共聚物(DPSS)之透明顆粒顯示DSC Tg爲267°C且比重 爲1 .3 1。產物之顆粒透明性、單一 GP C波峰、中間T g及 比重明確顯示確實已形成PSSD及PSS之嵌段共聚物且產 物不僅是兩均聚物P S S D及P P S之摻合物。詳細性質列於 表1。詳細化學反應顯示於(圖II )。 實施例4 : TMPES : 25 : 75 PES : TPES之嵌段共聚物 • 使用以下三步驟方法製備此TMPES ( PES-TPES )嵌 段共聚物。 第1部分·· PES均嵌段之製備 使用與實施例1所述者相同之實驗配置。(1000 ? 4 5 °c 523 g added to the burner should be mixed with the gas obtained in the obtained MWD -31 - 200724571 (28) ring butyl sulfonate (44 10 g, 3500 ml / mol) and toluene ((7) (10) ml / mol Put into the flask and continue to heat with nitrogen bubbles to 45 ° C. 4,4, bis[(4-chlorophenyl)sulfonyl]biphenyl (CSB) (503 g) and 4,4' Bis[(4-hydroxyphenyl)sulfonyl]biphenol (HSB) (471 g) was added to the flask, HSB: CSB was 1 〇1: 1.00 molar ratio, and the reaction mixture was stirred for 30 minutes. Anhydrous sodium carbonate (1 2 3 g) was added. Toluene was used as the azeotropic solvent. The rest of the procedure was the same as described in Part 2 of Example 1. The resulting homoblock had a GPC molecular weight of 29 29,000, Mw 38,000 and MWD 1.31. Part 3: Preparation of block copolymer The reaction mixture of Part 1 and Part 2 is mixed at an equal weight ratio, and block polymerization is carried out at 23 ° C. After reaching the desired MW (as indicated by GPC), the reaction is carried out. The mixture was quenched with cyclobutyl hydrazine (504 g, 400 ml/mol) and the temperature was lowered to 210 ° C. The methyl chloride gas was then bubbled through the reaction mixture over 3 hours. To complete the completion of the end-cap. The reaction mixture was then diluted a second time with cyclobutyl hydrazine (400 mL/mol). The polymer solution was filtered through a 15 μm filter using a 2 kg/cm 2 nitrogen pressure in a filter press funnel. The salt was removed. Finally, the block copolymer was recovered by slowly adding a salt-free polymer solution to deionized water (13 ml/g polymer) under high-speed stirring. The precipitated polymer was honed and refluxed three times with deionized water at 90 ° C to completely remove all salts and cyclohexane. The precipitated polymer was then filtered and applied at -32-200724571 (29) 140°. Drying in a C furnace until the water content determined by Karl Fischer titration < 0.5%. • The GPC analysis of the block copolymer based on polystyrene standards showed Μη. It was 89,000, Mw was 122,000 and the MWD was 1.37. The resulting copolymer has a molecular weight much higher than the two homoblocks as monomer units, indicating the preparation of the block copolymer. The block copolymer powder is then mixed with 0.25% heat stabilizer and granulated using a twin screw extruder. PS g T g The specific gravity is 259 ° C and 1.29, while the PSS is 270 ° C and 1.32. The transparent particles of the block copolymer (DPSS) show a DSC Tg of 267 ° C and a specific gravity of 1.31. Particle transparency, a single GP C peak, intermediate T g and specific gravity clearly indicate that block copolymers of PSSD and PSS have indeed been formed and the product is not only a blend of two homopolymers PSSD and PPS. The detailed properties are listed in Table 1. The detailed chemical reaction is shown in (Figure II). Example 4: TMPES: 25: 75 PES: Block copolymer of TPES • This TMPES (PES-TPES) block copolymer was prepared using the following three-step process. Part 1· Preparation of PES homoblock The same experimental configuration as that described in Example 1 was used.

將環丁颯(300克,1〇〇〇毫升/莫耳)及甲苯(looo 毫升/莫耳)置入燒瓶中,連續通以氮氣泡,加熱至40 。將二羥基二苯基颯(DHDPS) (62.8克)、4,4,一二氯 一本基颯(DCDPS) (71.75克)添加於燒瓶中,DCDPS -33- 200724571 (30) 及DHDPS係爲1.00: 1·〇〇5莫耳比,反應物攪拌30分鐘 。添加無水碳酸鈉(3 2 · 2克)。藉氣洗於燒瓶中保持氮氛 圍。甲苯係作爲共沸溶劑。反應物之溫度係以6小時緩緩 增加至23 6 °C,攪拌速度設定於4〇〇 rpm。因爲Na2C03與 DHDPS反應所形成之水係以與甲苯之共沸物形式餾除且 收集於Dean-Stark汽水閥中。甲苯一旦與水分離即送回 反應混合物。一旦完全移除水,則停止將甲苯添加回反應 器。之後隨著反應物溫度增加自該反應混合物完全移除甲 苯。在6小時後達到所需溫度。之後將反應溫度保持於 23 6 °C,當黏度開始增加時,攪拌速度提高至5 00 rpm。 在所需之 Μη 19,300、Mw 約 22,000 且 MWD 1.14 下,反 應混合物冷卻至接近200°C。DHDPS對DCDPS之相對相 等莫耳比產生具有相對低分子量且主要具有-Ph-OH末端 基團之PES。 第2部分:TPES均嵌段之製備 將環丁颯(900克,1000毫升/莫耳)及甲苯(64 5克 ,1 00 0毫升/莫耳)置入燒瓶中,連續通以氮氣泡,加熱 至 4CTC。將四甲基聯苯酚颯(TMDHDPS) (229.5克) 及4,4’—二氯二苯基颯(DCDPS ) (221.7克)添加於燒 瓶中,DCDPS及TMDHDPS係爲1.03 : 1·00莫耳比,反 應混合物攪拌30分鐘。添加無水碳酸鈉Na2C03 ( 96.7克 )。反應物之溫度係以6小時緩緩增加至23 6°C,攪拌速 度設定於400 rpm。因爲Na2C03與TMDHDPS反應所形成 -34- 200724571 (31) 之水係以與甲苯之共沸物形式餾除且收集於Dean_Stai*k 汽水閥中。甲苯一旦與水分離即送回反應混合物。一旦完 全移除水,則停止將甲苯添加回反應器。之後隨著反應物 溫度增加自該反應混合物完全移除甲苯。在6小時後達到 所需溫度。之後將反應溫度保持於2 3 6 °C,當黏度開始增 加時,攪拌速度提高至500 rpm。在所需之Μη 1 8,200、 Mw 約 20,〇〇〇 且 MWD 1.10 下,DCDPS 對 TMDHDPS 之相 對高莫耳比產生具有相對低分子量且主要具有-Ph-Cl末端 基團之TMPES。 第3部分:嵌段共聚物之製備 第1部分及第2部分之反應混合物於等重量比例下 混合,於23 6°C進行嵌段聚合。達到所需之MW (如GPC 所示)後,反應混合物以環丁颯(250克,200毫升/莫耳 )中止反應,溫度降至220 °C。之後使甲基氯氣體冒泡通 經反應混合物歷經3小時,以確定完成末端封蓋。反應混 合物隨之以環丁礪(200毫升/莫耳)稀釋第二次。聚合物 溶液於壓濾器漏斗中使用2公斤/厘米2氮壓力經1 5微米 濾器過濾以移除鹽類。最後藉著於高速攪拌下緩緩添加不 含鹽之聚合物溶液於去離子水(13毫升/克聚合物)中 而回收嵌段共聚物。之後藉過濾回收沉澱之聚合物。沉澱 之聚合物經硏磨且於90 °C使用去離子水回流三次,以完 全移除所有鹽類及環丁颯。之後過濾沉澱之聚合物並於 140°C爐中乾燥,直至藉Karl Fischer滴定決定之水含量 -35- 200724571 (32) < 0.5%。 嵌段共聚物基於聚苯乙烯標準物之GPC分析顯示Μη 爲 79,800,Mw 爲 115,000 且 MWD 爲 1.44。因此,所製 之共聚物具有遠高於作爲單體單元之兩均嵌段的分子量, 表示製備嵌段共聚物。嵌段共聚物粉末隨後與0.25%熱安 定劑混合且使用雙螺桿擠塑機造粒。PES之Tg及比重個 別係爲225 °C及1.37,而TPES者係爲271 °C及1.33。嵌 段共聚物之透明顆粒顯示DSC Tg爲267°C且比重爲1.32 。產物之顆粒透明性、單一 GP C波峰、中間Tg及比重明 確顯示確實已形成PES及TPES之嵌段共聚物(TMPES) 且產物不僅是兩均聚物PES及TPES之摻合物。詳細性質 列於表3。詳細化學反應表示於(圖111 )。 實施例5: TMPES : 40 : 60 PES : TPES之嵌段共聚物 使用以下三步驟方法製備TMPES ( PES-TPES )嵌段 共聚物。 第1部分:PES均嵌段之製備 使用與實施例1所述者相同之實驗配置。 將環丁礪(480克,1000毫升/莫耳)及甲苯(344克 ,:1000毫升/莫耳)置入燒瓶中,連續通以氮氣泡,加熱 至 40°C。將二羥基二苯基颯(DHDPS) (100.5克)、 4,4’ 一二氯二苯基楓(DCDPS) (114.8克)添加於燒瓶 中,DCDPS及DHDPS係爲1.00: 1.005莫耳比,反應物 -36- 200724571 (33) 攪拌3 0分鐘。添加無水碳酸鈉(5 〇克)。藉氣洗於燒瓶 中保持氮氛圍。甲苯係作爲共沸溶劑。 其餘方法係如同實施例4第1部分所述。所得之均嵌 段具有 GPC 分子量 Μη 23,000,Mw 26,〇〇〇 及 MWD 1.11 第2部分:TPES均嵌段之製備 Φ 將環丁颯(720克,1〇〇〇毫升/莫耳)及甲苯(516克 ,1 000毫升/莫耳)置入燒瓶中,連續通以氮氣泡,加熱 至40°c。將四甲基聯苯酚礪(TMDHDPS) (183.6克) 及4,4’ —二氯二苯基颯(DCDPS) (177.4克)添加於燒 瓶中,DCDPS及TMDHDPS係爲1.03: 1.00莫耳比,反 應混合物攪拌30分鐘。添加無水碳酸鈉Na2C03 ( 75克 )° 其餘方法係如同實施例4第2部分所述。所得之均嵌 • 段具有 GPC 分子量 Μη 20,000,Mw 22,000 及 MWD 1 _ 1 〇 第3部分:嵌段共聚物之製備 第1部分及第2部分之反應混合物於等重量比例下 混合,於23 6 °C進行嵌段聚合。達到所需之MW (如GPC 所示)後,反應混合物以環丁颯(250克,200毫升/莫耳 )中止反應,溫度降至22〇°C。之後使甲基氯氣體冒泡通 經反應混合物歷經3小時,以確定完成末端封蓋。反應混 -37- 200724571 (34) 合物隨之以環丁楓(200毫升/莫耳)稀釋第二次。聚合物 溶液於壓濾器漏斗中使用2公斤/厘米2氮壓力經1 5微米 濾器過濾以移除鹽類。最後藉著於高速攪拌下緩緩添加不 含鹽之聚合物溶液於去離子水(1 3毫升/克聚合物)中 而回收嵌段共聚物。之後藉過濾回收沉澱之聚合物。沉澱 之聚合物經硏磨且於9 0 °C使用去離子水回流三次,以完 全移除所有鹽類及環丁颯。之後過瀘沉澱之聚合物並於 140°C爐中乾燥,直至藉Karl Fischer滴定決定之水含量 < 0.5%。 嵌段共聚物基於聚苯乙烯標準物之GPC分析顯示Μη 爲 80,900,Mw 爲 119,000 且 MWD 爲 1.47。因此,所製 之共聚物具有遠高於作爲單體單元之兩均嵌段的分子量, 表示製備嵌段共聚物。嵌段共聚物粉末隨後與0.25%熱安 定劑混合且使用雙螺桿擠塑機造粒。PES之Tg及比重個 別係爲225 °C及1.37,而TPES者係爲271°C及1.33。嵌 段共聚物之透明顆粒顯示DSC Tg爲2 5 8 °C且比重爲1.32 。產物之顆粒(TMPES )透明性、單一 GPC波峰、中間 Tg及比重明確顯示確實已形成PES及TPES之嵌段共聚 物且產物不僅是兩均聚物PES及TPES之摻合物。詳細性 質列於表3。詳細化學反應表示於(圖III )。 實施例6 : TMPES : 60: 40 PES : TPES之嵌段共聚物 使用以下三步驟方法製備此PES-TMPES嵌段共聚物 -38- 200724571 (35) 第1部分:P E S均嵌段之製備 使用與實施例1所述者相问之貫fe配置。 將環丁颯(720克,1000毫升/莫耳)及甲苯(516克 ,1 0 0 0毫升/莫耳)置入燒瓶中,連續通以氮氣泡,加熱 至40。(:。將二羥基二苯基礪(DHDPS) (150.7克)、 4,4,一二氯二苯基颯(DCDPS) (172.2克)添加於燒瓶 中,DCDPS及DHDPS係爲1.00: 1.005莫耳比’反應物 攪拌3 0分鐘。添加無水碳酸鈉(7 5克)。藉氣洗於燒瓶 中保持氮氛圍。甲苯係作爲共沸溶劑。 其餘方法係如同實施例4第1部分所述。所得之均嵌 段具有 GPC 分子量 Μη 25,000,Mw 28,000 及 MWD 1.12 第2部分:TPES均嵌段之製備 • 將環丁礪(480克,1000毫升/莫耳)及甲苯(3 44克 ,1 000毫升/莫耳)置入燒瓶中,連續通以氮氣泡,加熱 至40°c。將四甲基聯苯酚颯(TMDHDPS) (122.4克) 及4,4’ —二氯二苯基颯(DCDPS) (118.24克)添加於燒 瓶中,DCDPS及TMDHDPS係爲1.03: 1·〇〇莫耳比,反 應混合物攪拌30分鐘。添加無水碳酸鈉Na2C03 ( 50克 )° 其餘方法係如同實施例4第2部分所述。所得之均嵌 段具有 GPC 分子量 Μη 1 8,000,Mw 20,〇〇〇 及 MWD 1.10 -39 - 200724571 (36) 第3部分:嵌段共聚物之製備 第1部分及第2部分之反應混合物於等重量比例下 混合,於2 3 6 °C進行嵌段聚合。達到所需之M W (如GP C 所示)後,反應混合物以環丁颯(25 0克,200毫升/莫耳 )中止反應,溫度降至22(TC。之後使甲基氯氣體冒泡通 經反應混合物歷經3小時,以確定完成末端封蓋。反應混 合物隨之以環丁颯(200毫升/莫耳)稀釋第二次。聚合物 溶液於壓濾器漏斗中使用2公斤/厘米2氮壓力經1 5微米 濾器過濾以移除鹽類。最後藉著於高速攪拌下緩緩添加不 含鹽之聚合物溶液於去離子水(1 3毫升/克聚合物)中 而回收嵌段共聚物。之後藉過濾回收沉澱之聚合物。沉澱 之聚合物經硏磨且於9 0 °C使用去離子水回流三次,以完 全移除所有鹽類及環丁礪。之後過濾沉澱之聚合物並於 140°C爐中乾燥,直至藉Karl Fischer滴定決定之水含量 < 0.5%。 嵌段共聚物基於聚苯乙烯標準物之GPC分析顯示Μη 爲 85,700,Mw 爲 126,000 且 MWD 爲 1.47。因此,所製 之共聚物具有遠高於作爲單體單元之兩均嵌段的分子量, 表示製備嵌段共聚物。嵌段共聚物粉末隨後與0.25%熱安 定劑混合且使用雙螺桿擠塑機造粒。P E S之T g及比重個 別係爲225 °C及1.37,而TPES者係爲27 1°C及1.33。嵌 段共聚物之透明顆粒顯示DSC Tg爲247°C且比重爲1·32 -40-Ring guanidine (300 g, 1 〇〇〇 ml/mole) and toluene (looo cc/mole) were placed in a flask, and nitrogen bubbles were continuously passed through and heated to 40 liters. Dihydroxydiphenyl hydrazine (DHDPS) (62.8 g), 4,4, dichloro-based guanidine (DCDPS) (71.75 g) was added to the flask, DCDPS-33-200724571 (30) and DHDPS were 1.00: 1·〇〇5 molar ratio, the reaction was stirred for 30 minutes. Anhydrous sodium carbonate (3 2 · 2 g) was added. Wash in a flask to maintain a nitrogen atmosphere. Toluene is used as an azeotropic solvent. The temperature of the reactant was gradually increased to 23 6 ° C over 6 hours, and the stirring speed was set at 4 rpm. The water system formed by the reaction of Na2C03 with DHDPS was distilled off as an azeotrope with toluene and collected in a Dean-Stark soda valve. The toluene is returned to the reaction mixture once it is separated from the water. Once the water is completely removed, the addition of toluene to the reactor is stopped. The toluene is then completely removed from the reaction mixture as the temperature of the reactants increases. The desired temperature was reached after 6 hours. The reaction temperature was then maintained at 23 6 ° C. When the viscosity began to increase, the stirring speed was increased to 500 rpm. The reaction mixture was cooled to approximately 200 ° C at the desired Μ 19,300, Mw of approximately 22,000 and MWD 1.14. The relative phase molar ratio of DHDPS to DCDPS produces a PES having a relatively low molecular weight and having predominantly a -Ph-OH end group. Part 2: Preparation of TPES homoblocks Cyclobutane (900 g, 1000 ml/mole) and toluene (64 5 g, 1000 ml/mole) were placed in a flask with continuous nitrogen bubbles. Heat to 4CTC. Tetramethyl phenol phenolphthalein (TMDHDPS) (229.5 g) and 4,4'-dichlorodiphenyl hydrazine (DCDPS) (221.7 g) were added to the flask, and the DCDPS and TMDHDPS systems were 1.03: 1.00 m The reaction mixture was stirred for 30 minutes. Anhydrous sodium carbonate Na2C03 (96.7 g) was added. The temperature of the reactant was gradually increased to 23 6 ° C over 6 hours, and the stirring speed was set at 400 rpm. The water system formed by the reaction of Na2C03 with TMDHDPS -34- 200724571 (31) was distilled off as an azeotrope with toluene and collected in a Dean_Stai*k steam trap. The toluene is returned to the reaction mixture once it is separated from the water. Once the water is completely removed, the addition of toluene to the reactor is stopped. Toluene was then completely removed from the reaction mixture as the temperature of the reactants increased. The desired temperature is reached after 6 hours. Thereafter, the reaction temperature was maintained at 2 3 6 ° C, and when the viscosity began to increase, the stirring speed was increased to 500 rpm. At the desired Μ1 8,200, Mw of about 20, and MWD 1.10, DCDPS produces a relatively low molecular weight TMPES with a relatively low molecular weight and predominantly a -Ph-Cl end group for TMDHDPS. Part 3: Preparation of block copolymer The reaction mixture of the first part and the second part was mixed at an equal weight ratio, and block polymerization was carried out at 23 6 °C. After reaching the desired MW (as indicated by GPC), the reaction mixture was quenched with cyclohexane (250 g, 200 mL / m) and the temperature was reduced to 220 °C. Methyl chloride gas was then bubbled through the reaction mixture over a period of 3 hours to determine completion of the end cap. The reaction mixture was then diluted a second time with cyclobutyl hydrazine (200 ml/mole). The polymer solution was filtered through a 15 micron filter using a 2 kg/cm 2 nitrogen pressure in a filter press funnel to remove salts. Finally, the block copolymer was recovered by slowly adding a salt-free polymer solution to deionized water (13 ml/g of polymer) under high-speed stirring. The precipitated polymer is then recovered by filtration. The precipitated polymer was honed and refluxed three times with deionized water at 90 °C to completely remove all salts and cyclopentane. The precipitated polymer was then filtered and dried in an oven at 140 ° C until the water content determined by Karl Fischer titration -35 - 200724571 (32) < 0.5%. GPC analysis of the block copolymer based on polystyrene standards showed a η of 79,800, a Mw of 115,000 and an MWD of 1.44. Therefore, the copolymer produced has a molecular weight far higher than the two homoblocks as monomer units, indicating the preparation of the block copolymer. The block copolymer powder was then mixed with 0.25% thermal stabilizer and granulated using a twin screw extruder. The Tg and specific gravity of PES are 225 °C and 1.37, while those of TPES are 271 °C and 1.33. The transparent particles of the block copolymer showed a DSC Tg of 267 ° C and a specific gravity of 1.32. The particle transparency of the product, the single GP C peak, the intermediate Tg and the specific gravity clearly indicate that the block copolymer (TMPES) of PES and TPES has indeed been formed and the product is not only a blend of the two homopolymers PES and TPES. The detailed properties are listed in Table 3. The detailed chemical reaction is shown in (Fig. 111). Example 5: TMPES: 40: 60 PES: Block copolymer of TPES The TMPES (PES-TPES) block copolymer was prepared using the following three-step process. Part 1: Preparation of PES homoblock The same experimental configuration as described in Example 1 was used. Cyclopentane (480 g, 1000 ml/mole) and toluene (344 g, 1000 ml/mole) were placed in a flask, and nitrogen bubbles were continuously passed through and heated to 40 °C. Dihydroxydiphenyl hydrazine (DHDPS) (100.5 g), 4,4'-dichlorodiphenyl maple (DCDPS) (114.8 g) was added to the flask, and the DCDPS and DHDPS systems were 1.00: 1.005 molar ratio. Reactant -36- 200724571 (33) Stir for 30 minutes. Add anhydrous sodium carbonate (5 g). Wash in a flask to maintain a nitrogen atmosphere. Toluene is used as an azeotropic solvent. The remaining methods are as described in Part 1 of Example 4. The resulting homoblock has a GPC molecular weight Μη 23,000, Mw 26, 〇〇〇 and MWD 1.11 Part 2: Preparation of TPES homoblock Φ Ring oxime (720 g, 1 〇〇〇 ml/mole) and toluene (516 g, 1 000 ml/mole) was placed in a flask, continuously bubbled with nitrogen, and heated to 40 ° C. Tetramethyl phenol phenolphthalein (TMDHDPS) (183.6 g) and 4,4'-dichlorodiphenyl hydrazine (DCDPS) (177.4 g) were added to the flask, and the DCDPS and TMDHDPS systems were 1.03: 1.00 mol ratio. The reaction mixture was stirred for 30 minutes. Anhydrous sodium carbonate Na2C03 (75 g) was added. The rest of the procedure was as described in Part 2 of Example 4. The resulting intercalated segments have GPC molecular weights 20,000 20,000, Mw 22,000 and MWD 1 _ 1 〇 Part 3: Preparation of block copolymers The reaction mixtures of Part 1 and Part 2 are mixed at equal weight ratios, at 23 6 Block polymerization was carried out at °C. After reaching the desired MW (as indicated by GPC), the reaction mixture was quenched with cyclobutyl hydrazine (250 g, 200 mL/m) and the temperature was reduced to 22 °C. Methyl chloride gas was then bubbled through the reaction mixture over a period of 3 hours to determine completion of the end cap. Reaction Mix -37- 200724571 (34) The compound was then diluted a second time with cyclohexane (200 ml/mole). The polymer solution was filtered through a 15 micron filter using a 2 kg/cm 2 nitrogen pressure in a filter press funnel to remove salts. Finally, the block copolymer was recovered by slowly adding a salt-free polymer solution to deionized water (13 ml/g polymer) under high-speed stirring. The precipitated polymer is then recovered by filtration. The precipitated polymer was honed and refluxed three times with deionized water at 90 °C to completely remove all salts and cyclopentane. The precipitated polymer was then dried and dried in a 140 ° C oven until the water content determined by Karl Fischer titration < 0.5%. GPC analysis of the block copolymer based on polystyrene standards showed a Μη of 80,900, a Mw of 119,000 and an MWD of 1.47. Therefore, the copolymer produced has a molecular weight far higher than the two homoblocks as monomer units, indicating the preparation of the block copolymer. The block copolymer powder was then mixed with 0.25% thermal stabilizer and granulated using a twin screw extruder. The Tg and specific gravity of PES are 225 °C and 1.37, while those of TPES are 271 °C and 1.33. The transparent particles of the block copolymer showed a DSC Tg of 2 5 8 ° C and a specific gravity of 1.32. The particle (TMPES) transparency of the product, the single GPC peak, the intermediate Tg and the specific gravity clearly indicate that the block copolymer of PES and TPES has indeed been formed and the product is not only a blend of the two homopolymers PES and TPES. The details are listed in Table 3. The detailed chemical reaction is shown in (Fig. III). Example 6: TMPES: 60: 40 PES: Block copolymer of TPES The PES-TMPES block copolymer was prepared using the following three-step process -38- 200724571 (35) Part 1: Preparation of PES homoblocks The embodiment of the first embodiment is consistent with the fe configuration. Cyclopentane (720 g, 1000 ml/mole) and toluene (516 g, 1000 ml/mole) were placed in a flask, and nitrogen bubbles were continuously passed through and heated to 40. (: Dihydroxydiphenyl hydrazine (DHDPS) (150.7 g), 4,4, dichlorodiphenyl hydrazine (DCDPS) (172.2 g) was added to the flask, and the DCDPS and DHDPS systems were 1.00: 1.005 The ear was stirred for 30 minutes than the 'reactant. Anhydrous sodium carbonate (75 g) was added and the mixture was purged with air to maintain a nitrogen atmosphere. Toluene was used as an azeotrope. The rest of the procedure was as described in Part 1 of Example 4. The resulting homoblock has GPC molecular weight Μη 25,000, Mw 28,000 and MWD 1.12 Part 2: Preparation of TPES homoblocks • Ring guanidine (480 g, 1000 ml/mole) and toluene (3 44 g, 1 000) Placed in a flask with nitrogen bubbles continuously, heated to 40 ° C. Tetramethyl phenol phenol (TMDHDPS) (122.4 g) and 4,4'-dichlorodiphenyl hydrazine (DCDPS) (118.24 g) was added to the flask, DCDPS and TMDHDPS were 1.03:1·〇〇 molar ratio, and the reaction mixture was stirred for 30 minutes. Anhydrous sodium carbonate Na2C03 (50 g) was added. The rest of the method was as in Example 4 Partially obtained. The resulting homoblock has GPC molecular weight Μη 1 8,000, Mw 20, 〇〇〇 and MWD 1.10 -39 - 200724571 (36) Part 3: Preparation of block copolymers The reaction mixtures of Part 1 and Part 2 are mixed at equal weight ratios and block polymerization is carried out at 2 3 ° C. to achieve the desired MW (As indicated by GP C), the reaction mixture was quenched with cyclobutyl hydrazine (250 g, 200 ml/mol) and the temperature was lowered to 22 (TC). The methyl chloride gas was then bubbled through the reaction mixture over 3 The hour was determined to complete the end capping. The reaction mixture was then diluted a second time with cyclobutyl hydrazine (200 ml/mol). The polymer solution was used in a filter press funnel using a 2 kg/cm2 nitrogen pressure through a 15 micron filter. Filtration to remove salts. Finally, the block copolymer was recovered by slowly adding a salt-free polymer solution to deionized water (13 ml/g polymer) under high-speed stirring. The polymer was precipitated and honed and refluxed three times with deionized water at 90 ° C to completely remove all salts and cyclobutyl hydrazine. The precipitated polymer was then filtered and dried in a 140 ° C oven. Until the water content determined by Karl Fischer titration < 0.5% The GPC analysis of the block copolymer based on polystyrene standards showed a Μη of 85,700, a Mw of 126,000 and an MWD of 1.47. Therefore, the copolymer produced had a molecular weight much higher than the two homoblocks as monomer units, A block copolymer was prepared. The block copolymer powder was then mixed with 0.25% thermal stabilizer and granulated using a twin screw extruder. The T g and specific gravity of P E S are 225 ° C and 1.37, while those of TPES are 27 1 ° C and 1.33. The transparent particles of the block copolymer showed a DSC Tg of 247 ° C and a specific gravity of 1.32 -40-

200724571 (37) 。產物之顆粒(TMPES )透明性、單一 GPC波 Tg及比重明確顯示確實已形成PES及TPES之 物且產物不僅是兩均聚物P E S及TP E S之摻合物 質列於表2。詳細化學反應表示於(圖ΠΙ )。 實施例 7: TMDPSS: 50: 50 PSSD : TMPSS 之 物200724571 (37). The particle of the product (TMPES) transparency, the single GPC wave Tg and the specific gravity clearly indicate that PES and TPES have indeed been formed and the product is not only a blend of the two homopolymers P E S and TP E S as shown in Table 2. The detailed chemical reaction is shown in (Fig. ΠΙ). Example 7: TMDPSS: 50: 50 PSSD: TMPSS

使用以下三部分方法製備此PSSD — TMPSS 物。 第1部分:PSSD均嵌段之製備 PSSD係使用DHDPS及CSB作爲單體而製得 使用如同實施例1所述之實驗配置。 將環丁楓(4410克,3500毫升/莫耳)及甲3 毫升/莫耳)置入燒瓶中,連續通以氮氣泡,加熱 。將4,4’雙[(4 —氯苯基)磺醯基]聯苯(CSB) )及4,4’二羥基二苯基颯(DHDPS ) ( 25 0克)% 瓶中,CSB: DHDPS係爲1.04: 1.00莫耳比,f 物攪拌30分鐘。添加無水碳酸鈉(123克)。_ 燒瓶中保持氮氛圍。甲苯係作爲共沸溶劑。 其餘方法係與實施例1第1部分所述者相同 均嵌段具有GPC分子量Μη 18,000,Mw 22,000 1.22。 、中間 段共聚 詳細性 段共聚 段共聚This PSSD - TMPSS was prepared using the following three methods. Part 1: Preparation of PSSD homoblocks PSSD was prepared using DHDPS and CSB as monomers using the experimental configuration as described in Example 1. Dingfeng (4410 g, 3500 ml/mole) and a 3 ml/mole were placed in a flask, and nitrogen bubbles were continuously passed through and heated. Will be 4,4' bis[(4-chlorophenyl)sulfonyl]biphenyl (CSB) and 4,4' dihydroxydiphenyl fluorene (DHDPS) (250 g)% bottle, CSB: DHDPS The ratio was 1.04: 1.00 molar ratio, and the material was stirred for 30 minutes. Anhydrous sodium carbonate (123 g) was added. _ Maintain a nitrogen atmosphere in the flask. Toluene is used as an azeotropic solvent. The rest of the procedure was the same as described in the first part of Example 1. The homoblock had a GPC molecular weight of 8,000 18,000 and Mw of 22,000 1.22. Intermediate segment copolymerization detailed segment copolymerization copolymerization

£ ( 1000 至 45〇C :523 克 ^加於燒 :應混合 ί氣洗於 所得之 且 MWD -41 - 200724571 (38) 第2部分:TMPSS均嵌段之製備 TMPSS係使用TMDHDPS及CSB作爲單體製得。 將環丁颯(4410克,3500毫升/莫耳)及甲苯(1000 毫升/莫耳)置入燒瓶中,連續通以氮氣泡,加熱至4 5 °C 。將4,4,雙[(4 —氯苯基)磺醯基]聯苯(CSB) (503克 )及四甲基二羥基二苯基楓( 3 09克TMDHDPS)添加於 燒瓶中,TMDHDPS: CSB係爲1.01: 1·〇〇莫耳比,反應 混合物攪拌30分鐘。添加無水碳酸鈉(123克)。甲苯 作爲共沸溶劑。 其餘方法係與實施例1第2部分所述者相同。所得之 均嵌段具有GPC分子量Μη 29,000,Mw 3 8,000且MWD 1.31。 第3部分:嵌段共聚物之製備 於等重量比例下混合第1部分及第2部分之反應混 合物,於23 0°C進行嵌段聚合。達到所需之MW (如GPC 所示)後,反應混合物以環丁颯(504克,400毫升/莫耳 )中止反應,溫度降至210 °C。之後使甲基氯氣體冒泡通 經反應混合物歷經3小時,以確定完成末端封蓋。反應混 合物隨之以環丁礪(400毫升/莫耳)稀釋第二次。聚合物 溶液於壓濾器漏斗中使用2公斤/厘米2氮壓力經1 5微米 濾器過濾以移除鹽類。最後藉著於高速攪拌下緩緩添加不 含鹽之聚合物溶液於去離子水(1 3毫升/克聚合物)中 而回收嵌段共聚物。之後藉過濾回收沉澱之聚合物。沉澱 -42- 200724571 (39) 之聚合物經硏磨且於9 0 °C使用去離子水回流三次’以完 全移除所有鹽類及環丁碾。之後過濾沉澱之聚合物並於 140 °C爐中乾燥,直至藉Karl Fischer滴定決定之水含量 < 0.5%。 嵌段共聚物基於聚苯乙烯標準物之GPC分析顯示Μη 爲 8 5,000,Mw 爲 1 20,000 且 MWD 爲 1.41。因此,所製 之共聚物具有遠高於作爲單體單元之兩均嵌段的分子量’ | 表示製備嵌段共聚物。嵌段共聚物粉末隨後與0.25%熱安 定劑混合且使用雙螺桿擠塑機造粒。PSSD之Tg及比重個 別係爲259 °C及1.29,而TMPSS者係爲268 1:及1.31。嵌 段共聚物(TMDPSS)之透明顆粒顯示DSC Tg爲264t:且 比重爲1 .3 1。產物之顆粒透明性、單一 GP C波峰、中間 Tg及比重明確顯示確實已形成PSSD及TMPSS之嵌段共 聚物且產物不僅是兩均聚物PSSD及TMPPS之摻合物。 詳細性質列於表1。詳細化學反應顯示於(圖IV )。 實施例8: TMBPSS : 50: 50 PSSB : TMPSS之嵌段共聚物 使用以下三部分方法製備TMBPSS(PSSB: TMPSS) 嵌段共聚物。 第1部分·· PSSB均嵌段之製備 PS SB係使用聯苯酚及CSB作爲單體而製得。 使用如同實施例1所述之實驗配置。 將環丁颯(4410克,3500毫升/莫耳)及甲苯(1〇〇〇 -43- 200724571 (40) 毫升/莫耳)置入燒瓶中,連續通以氮氣泡,加熱至45 。將4,4’雙[(4 —氯苯基)磺醯基]聯苯(CSB) (523克 )及聯苯酚(;[86克)添加於燒瓶中,CSB : DHDPS係爲 1·〇4 : 1·〇〇莫耳比,反應混合物攪拌3〇分鐘。添加無水 碳酸鈉(1 23克)。藉氣洗於燒瓶中保持氮氛圍。甲苯係 作爲共沸溶劑。 其餘方法係與實施例1第1部分所述者相同。所得之 均嵌段具有GPC分子量Μη 19,000,Mw 23,000且MWD 1.21。 第2部分:TMPSS均嵌段之製備 TMPSS係使用TMDHDPS及CSB作爲單體製得。 將環丁颯(4410克,3500毫升/莫耳)及甲苯(1〇〇〇 毫升/莫耳)置入燒瓶中,連續通以氮氣泡,加熱至45 °C 。將4,4’雙[(4 —氯苯基)磺醯基]聯苯(CSB) (503克 )及四甲基二羥基二苯基颯( 3 09克TMDHDPS)添加於 燒瓶中,TMDHDPS: CSB係爲1.01: 1.00莫耳比,反應 混合物攪拌30分鐘。添加無水碳酸鈉(123克)。甲苯 作爲共沸溶劑。 其餘方法係與實施例1第2部分所述者相同。所得之 均嵌段具有GPC分子量Μη 23,000,Mw 26,000且MWD 1.11。 第3部分··嵌段共聚物之製備 -44- 200724571 (41) 於等重量比例下混合第1部分及第2部分之反應混 合物,於2 3 0 °C進行嵌段聚合。達到所需之M W (如GP C 所示)後,反應混合物以環丁颯(504克,400毫升/莫耳 )中止反應,溫度降至2 1 0 °C。之後使甲基氯氣體冒泡通 經反應混合物歷經3小時,以確定完成末端封蓋。反應混 合物隨之以環丁颯(4 0 0毫升/莫耳)稀釋第二次。聚合物 溶液於壓濾器漏斗中使用2公斤/厘米2氮壓力經1 5微米 濾器過濾以移除鹽類。最後藉著於高速攪拌下緩緩添加不 含鹽之聚合物溶液於去離子水(1 3毫升/克聚合物)中 而回收嵌段共聚物。之後藉過濾回收沉澱之聚合物。沉澱 之聚合物經硏磨且於9 0 °C使用去離子水回流三次,以完 全移除所有鹽類及環丁颯。之後過濾沉澱之聚合物並於 140°C爐中乾燥,直至藉Karl Fischer滴定決定之水含量 < 0.5%。 嵌段共聚物基於聚苯乙烯標準物之GPC分析顯示Μη 爲 88,000,Mw 爲 124,000 且 MWD 爲 1.40。因此,所製 之共聚物具有遠高於作爲單體單元之兩均嵌段的分子量’ 表示製備嵌段共聚物。嵌段共聚物粉末隨後與0.25%熱安 定劑混合且使用雙螺桿擠塑機造粒。PS SB之Tg及比重個 別係爲270°C及1.33,而TMPSS者係爲268 °C及1.31。嵌 段共聚物(TMBPSS)之透明顆粒顯示DSC Tg爲268 °C且 比重爲1 .3 2。產物之顆粒透明性、單一 GP C波峰、中間 Tg及比重明確顯示確實已形成PSSB及TMPSS之嵌段共 聚物且產物不僅是兩均聚物PSSB及TMPPS之摻合物。 -45- 200724571 (42) 詳細性質列於表1。詳細化學反應顯示於(圖V )。 實施例 9: TMDPPSU : 50: 50 PPSU: TMPSS 之嵌段共聚 物 使用以下三部分方法製備此PPSU-TMPSS嵌段共聚物 〇 第1部分:PPSU均嵌段之製備 PPSU係使用聯苯酚及DCDPS作爲單體而製得。 使用如同實施例1所述之實驗配置。 將環丁颯(44 10克,3500毫升/莫耳)及甲苯(1000 毫升/莫耳)置入燒瓶中,連續通以氮氣泡,加熱至45°C 。將4,4’ —二氯二苯基颯(DCDPS) (298克)及聯苯酚 (186克)添加於燒瓶中,DCDPS: DHDPS係爲 1.04: 1.00莫耳比,反應混合物攪拌30分鐘。添加無水碳酸鈉 (1 23克)。藉氣洗於燒瓶中保持氮氛圍。甲苯係作爲共 沸溶劑。 其餘方法係與實施例1第1部分所述者相同。所得之 均嵌段具有GPC分子量Mn 23,000,Mw 29,〇〇〇且MWD 1.26。 第2部分:TMPSS均嵌段之製備 TMPSS係使用TMDHDPS及CSB作爲單體製得。 將環丁颯(4410克,3500毫升/莫耳)及甲苯(1〇00 -46- 200724571 (43) 毫升/莫耳)置入燒瓶中,連續通以氮氣泡,加熱至45。〇 。將4,4,雙[(4 —氯苯基)磺醯基]聯苯(CSB ) ( 5 03克 )及四甲基二羥基二苯基颯( 3 09克TMDHDPS)添加於 燒瓶中,TMDHDPS: CSB係爲1.01: 1.00莫耳比,反應 混合物攪拌3 〇分鐘。添加無水碳酸鈉(1 23克)。甲苯 作爲共沸溶劑。 其餘方法係與實施例1第2部分所述者相同。所得之 .均嵌段具有GPC分子量Μη 25,000,Mw 35,000且MWD 1.40。 第3部分:嵌段共聚物之製備 於等重量比例下混合第1部分及第2部分之反應混 合物,於23(TC進行嵌段聚合。達到所需之MW (如GPC 所示)後,反應混合物以環丁颯(504克,400毫升/莫耳 )中止反應,溫度降至2 1 0 °C。之後使甲基氯氣體冒泡通 經反應混合物歷經3小時,以確定完成末端封蓋。反應混 合物隨之以環丁颯(400毫升/莫耳)稀釋第二次。聚合物 溶液於壓濾器漏斗中使用2公斤/厘米2氮壓力經1 5微米 濾器過濾以移除鹽類。最後藉著於高速攪拌下緩緩添加不 含鹽之聚合物溶液於去離子水(1 3毫升/克聚合物)中 而回收嵌段共聚物。之後藉過濾回收沉澱之聚合物。沉澱 之聚合物經硏磨且於90 °C使用去離子水回流三次,以完 全移除所有鹽類及環丁颯。之後過濾沉澱之聚合物並於 1 4 0 C爐中乾燥’直至藉 Karl Fischer滴定決疋之水含重 -47- 200724571 (44) < 0.5%。 嵌段共聚物基於聚苯乙烯標準物之GPC分析顯示Μη 爲 82,000,Mw 爲 115,000 且 MWD 爲 1.40。因此,所製 之共聚物具有遠高於作爲單體單元之兩均嵌段的分子量, 表示製備嵌段共聚物。嵌段共聚物粉末隨後與0.25%熱安 定劑混合且使用雙螺桿擠塑機造粒。PPSU之Tg及比重個 別係爲220 °C及1.29,而TMPSS者係爲268 1:及1.31。嵌 段共聚物(TMDPPSU)之透明顆粒顯示DSC Tg爲240°C 且比重爲1.30。產物之顆粒透明性、單一 GPC波峰、中 間Tg及比重明確顯示確實已形成PPSU及TMPSS之嵌段 共聚物且產物不僅是兩均聚物PPSU及TMPPS之摻合物 。詳細性質列於表1。詳細化學反應顯示於(圖VI )。 實施例1〇 ·· TMDPES ·_ 50 : 50 PES : TMPSS之嵌段共聚物 使用以下三步驟方法製備此PES-TMPSS嵌段共聚物 第1部分:PES均嵌段之製備 PES係使用DHDPS及DCDPS作爲單體製得。 使用如同實施例1所述之實驗配置。 將環丁颯(4410克,3 500毫升/莫耳)及甲苯(1〇〇() 毫升/莫耳)置入燒瓶中,連續通以氮氣泡,加熱至45χ: 。將4,4’ 一二氯二苯基楓(DCDPS) (298克)及4,4,〜 二羥基二苯基礪(DHDPS ) ( 25 0克)添加於燒瓶中, -48- 200724571 (45) DCDPS ·· DHDPS係爲1 · 〇 4 : 1 · 0 0莫耳比,反應混合物攪 拌3 0分鐘。添加無水碳酸鈉(1 2 3克)。藉氣洗於燒瓶 中保持氮氛圍。甲苯係作爲共沸溶劑。 其餘方法係與實施例1第1部分所述者相同。所得之 均嵌段具有GPC分子量Μη 25,000,Mw 29,000且MWD 1.16。 第2部分:TMPSS均嵌段之製備 TMPSS係使用TMDHDPS及CSB作爲單體製得。 將環丁颯(4410克,3500毫升/莫耳)及甲苯(1000 毫升/莫耳)置入燒瓶中,連續通以氮氣泡,加熱至45 °C 。將4,4’雙[(4 一氯苯基)磺醯基]聯苯(CSB) (503克 )及四甲基二羥基二苯基礪( 3 09克TMDHDPS)添加於 燒瓶中,TMDHDPS: CSB係爲1.01: 1.00莫耳比,反應 混合物攪拌30分鐘。添加無水碳酸鈉(1 23克)。甲苯 作爲共沸溶劑。 其餘方法係與實施例1第2部分所述者相同。所得之 均嵌段具有GPC分子量Μη 25,000,Mw 35,000且MWD 1.40。 第3部分:嵌段共聚物之製備 於等重量比例下混合第1部分及第2部分之反應混 合物,於23(TC進行嵌段聚合。達到所需之MW (如GPC 所示)後,反應混合物以環丁颯(504克,400毫升/莫耳 -49- 200724571 (46) )中止反應,溫度降至210 °C。之後使甲基氯氣體冒泡通 經反應混合物歷經3小時’以確定完成末端封蓋。反應混 合物隨之以環丁颯(400毫升/莫耳)稀釋第二次。聚合物 溶液於壓濾器漏斗中使用2公斤/厘米2氮壓力經1 5微米 濾器過濾以移除鹽類。最後藉著於高速攪拌下緩緩添加不 含鹽之聚合物溶液於去離子水(13毫升/克聚合物)中 而回收嵌段共聚物。之後藉過濾回收沉澱之聚合物。沉澱 之聚合物經硏磨且於90 °C使用去離子水回流三次,以完 全移除所有鹽類及環丁颯。之後過濾沉澱之聚合物並於 140°C爐中乾燥,直至藉Karl Fischer滴定決定之水含量 < 0.5%。 嵌段共聚物基於聚苯乙烯標準物之GPC分析顯示Μη 爲 85,000,Mw 爲 115,000 且 M WD 爲 1.35。因此,所製 之共聚物具有遠高於作爲單體單元之兩均嵌段的分子量, 表示製備嵌段共聚物。嵌段共聚物粉末隨後與0.25%熱安 定劑混合且使用雙螺桿擠塑機造粒。PES之Tg及比重個 別係爲225 t:及1.29,而TMPSS者係爲26 8 °C及1.31。嵌 段共聚物(TMDPES )之透明顆粒顯示DSC Tg爲2 5 5 °C且 比重爲1.30。產物之顆粒透明性、單一 GPC波峰、中間 Tg及比重明確顯示確實已形成PES及TMPSS之嵌段共聚 物且產物不僅是兩均聚物PES及TMPPS之摻合物。詳細 性質列於表1。詳細化學反應顯示於(圖VII )。 實施例11: BPSK : 50: 50 PSSB : PESK之嵌段共聚物 -50- 200724571 (47) 使用以下三部分方法製備此PSSB-PESK嵌段共聚物 第1部分:P S S B均嵌段之製備 PSSB係使用聯苯酚及CSB作爲單體而製得。 使用如同實施例1所述之實驗配置。 將環丁礪(4410克,3500毫升/莫耳)及甲苯(1〇〇〇 毫升/莫耳)置入燒瓶中,連續通以氮氣泡,加熱至45 °C 。將4,4’雙[(4 一氯苯基)磺醯基]聯苯(CSB) (523克 )及聯苯酚(1 8 6克)添加於燒瓶中,C S B : D H D P S係爲 1.04 : 1.00莫耳比,反應混合物攪拌30分鐘。添加無水 碳酸鈉(1 2 3克)。藉氣洗於燒瓶中保持氮氛圍。甲苯係 作爲共沸溶劑。 其餘方法係與實施例1第1部分所述者相同。所得之 均嵌段具有GPC·分子量Μη 19,000,Mw 23,000且MWD 1.21。 第2部分:PESK均嵌段之製備 PESK係使用DCB及DHDPS作爲單體製得。 將環丁礪(4410克,3500毫升/莫耳)及甲苯(1〇〇〇 毫升/莫耳)置入燒瓶中,連續通以氮氣泡,加熱至45 °C 。將4,4’ —二氯二苯基二苯基甲酮(DCB) (251克)及 4,4’—二羥基二苯基砸(DHDPS) ( 25 3克)添加於燒瓶 中,DHDPS : DCB係爲1.01 : 1·〇〇莫耳比,反應混合物 -51 - 200724571 (48) 攪拌30分鐘。添加無水碳酸鈉(123克)。甲苯作爲共 沸溶劑。 其餘方法係與實施例1第2部分所述者相同。所得之 均嵌段具有GPC分子量Μη 25,000,Mw 35,000且MWD 1.40。 第3部分:嵌段共聚物之製備 φ 於等重量比例下混合第1部分及第2部分之反應混 合物,於2 3 0 °C進行嵌段聚合。達到所需之M W (如GP C 所示)後,反應混合物以環丁颯(5 04克,400毫升/莫耳 )中止反應,溫度降至210 °C。之後使甲基氯氣體冒泡通 經反應混合物歷經3小時,以確定完成末端封蓋。反應混 合物隨之以環丁颯(400毫升/莫耳)稀釋第二次。聚合物 溶液於壓濾器漏斗中使用2公斤/厘米2氮壓力經1 5微米 濾器過濾以移除鹽類。最後藉著於高速攪拌下緩緩添加不 ® 含鹽之聚合物溶液於去離子水(1 3毫升/克聚合物)中 而回收嵌段共聚物。之後藉過濾回收沉澱之聚合物。沉澱 之聚合物經硏磨且於90 °C使用去離子水回流三次,以完 全移除所有鹽類及環丁颯。之後過濾沉澱之聚合物並於 140°C爐中乾燥,直至藉Karl Fischer滴定決定之水含量 < 〇·5% 〇 嵌段共聚物基於聚苯乙烯標準物之GPC分析顯示Μη 爲 8 8,000,Mw 爲 124,000 且 MWD 爲 1.40。因此,所製 之共聚物具有遠高於作爲單體單元之兩均嵌段的分子量, -52- 200724571 (49) 表示製備嵌段共聚物。嵌段共聚物粉末隨後與0.25%熱安 定劑混合且使用雙螺桿擠塑機造粒。PS SB之Tg及比重個 別係爲2 7 0 °C及1 . 3 3,而P E S K者係爲1 8 5 °C及1.2 8。嵌 段共聚物(BPSK)之透明顆粒顯示DSC Tg爲23 5 °C且比 重爲1 · 3 2。產物之顆粒透明性、單一 G P C波峰、中間T g 及比重明確顯示確實已形成PS SB及PESK之嵌段共聚物 且產物不僅是兩均聚物PS SB及TESK之摻合物。詳細性 質列於表1。詳細化學反應顯示於(圖VIII )。 實施例 12: TMDPSU : 50: 50 PSU : TMPSS之嵌段共聚 物 使用以下三部分方法製備此PSU-TMPSS嵌段共聚物 第1部分:PSU均嵌段之製備 # PSU係使用雙酚A及DCDPS作爲單體而製得。 使用如同實施例1所述之實驗配置。 將環丁颯(4410克,3500毫升/莫耳)及甲苯(1000 毫升/莫耳)置入燒瓶中,連續通以氮氣泡,加熱至45°C 。將4,4’〜二氯二苯基颯(DCDPS) (298克)及雙酚A (250克)添加於燒瓶中,DCDPS:雙酚A係爲1·〇4: 1.00莫耳比,反應混合物攪拌30分鐘。添加無水碳酸鈉 (I54克)。藉氣洗於燒瓶中保持氮氛圍。甲苯係作爲共 沸溶劑。 -53- 200724571 (50) 其餘方法係與實施例1第1部分所述者相同。所得之 均嵌段具有GPC分子量Μη 20,000,MW 25,000且MWD 1.25。 第2部分:TMPSS均嵌段之製備 TMPSS係使用TMDHDPS及CSB作爲單體製得。 將環丁颯(44 10克,3500毫升/莫耳)及甲苯(1〇〇〇 毫升/莫耳)置入燒瓶中,連續通以氮氣泡,加熱至45t: 。將4,4,雙[(4 —氯苯基)磺醯基]聯苯(CSB) (503克 )及四甲基二羥基二苯基颯(3 09克TMDHDPS)添力口於 燒瓶中,TMDHDPS: CSB係爲 1·〇1: 1.00莫耳比,反應 混合物攪拌30分鐘。添加無水碳酸鈉(123克)。甲苯 作爲共沸溶劑。 其餘方法係與實施例1第2部分所述者相同。所得之 均嵌段具有GPC分子量Μη 25,000,Mw 35,000且MWD 1.40。 第3部分:嵌段共聚物之製備 於等重量比例下混合第1部分及第2部分之反應混 合物,於2 2 0 °C進行嵌段聚合。達到所需之M W (如G P C 所示)後,反應混合物以環丁颯(504克,400毫升/莫耳 )中止反應,溫度降至200 °C。之後使甲基氯氣體冒泡通 經反應混合物歷經3小時,以確定完成末端封蓋。反應混 合物隨之以環丁礪(4〇〇毫升/莫耳)稀釋第二次。聚合物 -54- 200724571 (51) 溶液於壓濾器漏斗中使用2公斤/厘米2氮壓力經1 5微米 濾器過濾以移除鹽類。最後藉著於高速攪拌下緩緩添加不 含鹽之聚合物溶液於去離子水(13毫升/克聚合物)中 而回收嵌段共聚物。之後藉過濾回收沉澱之聚合物。沉澱 之聚合物經硏磨且於90 °C使用去離子水回流三次,以完 全移除所有鹽類及環丁礪。之後過濾沉澱之聚合物並於 140°C爐中乾燥,直至藉Karl Fischer滴定決定之水含量 < 0.5%。 嵌段共聚物基於聚苯乙烯標準物之GPC分析顯示Μη 爲 80,000,Μη 爲 115,000 且 M WD 爲 1.44。因此,所製 之共聚物具有遠高於作爲單體單元之兩均嵌段的分子量, 表示製備嵌段共聚物。嵌段共聚物粉末隨後與0.25%熱安 定劑混合且使用雙螺桿擠塑機造粒。PSU之Tg及比重個 別係爲190°C及1.29,而TMPSS者係爲268 °C及1.31。嵌 段共聚物(TMDPSU)之透明顆粒顯示DSC Tg爲23 0°C 且比重爲1.30。產物之顆粒透明性、單一 GPC波峰、中 間Tg及比重明確顯示確實已形成PES及TMPSS之嵌段 共聚物且產物不僅是兩均聚物PSU及TMPPS之摻合物。 詳細性質列於表1。詳細化學反應顯示於(圖IX )。 使用一或多種二氯化合物及一或多種二羥基化合物製 備各種均嵌段,其中部分列於下文: 芳族二鹵基化合物: 二氯二苯基碾(DCDPS) 、4,4’ —雙(4 —氯苯基磺 醯基)聯苯(CSB)、二氯二苯基甲酮、二氯二苯基醚、 -55- 200724571 (52) 二氯聯苯、二氯二苯基亞甲基、二甲基二氯二苯基礪、四 甲基二氯二苯基颯、二鹵基二苯基聯苯、二鹵基二苯氧基 聯苯、二鹵基二苯基聯苯二醚(二颯或二_) (ci-c6h4-c6h4-x-c6h4-c6h4-x-c6h4-c6h4-cl),£ (1000 to 45〇C: 523 g ^ added to the burn: should be mixed with ί gas and obtained from MWD -41 - 200724571 (38) Part 2: Preparation of TMPSS homoblocks TPSPS uses TMDHDPS and CSB as single The system was prepared. Put the cyclohexane (4410 g, 3500 ml/mole) and toluene (1000 ml/mole) into the flask, continuously pass nitrogen bubbles, and heat to 45 ° C. 4, 4, Bis[(4-chlorophenyl)sulfonyl]biphenyl (CSB) (503 g) and tetramethyldihydroxydiphenyl maple (3 09 g TMDHDPS) were added to the flask, TMDHDPS: CSB was 1.01: 1. The molar ratio of the mixture was stirred for 30 minutes, anhydrous sodium carbonate (123 g) was added, and toluene was used as the azeotropic solvent. The remaining methods were the same as those described in the second part of Example 1. The resulting homoblock has GPC molecular weight Μ 29,000, Mw 3 8,000 and MWD 1.31. Part 3: Preparation of block copolymer The reaction mixture of the first part and the second part was mixed at an equal weight ratio, and block polymerization was carried out at 23 ° C. After the desired MW (as indicated by GPC), the reaction mixture was quenched with cyclobutyl hydrazine (504 g, 400 ml/mole) at temperature. The temperature was lowered to 210 ° C. Methyl chloride gas was then bubbled through the reaction mixture over 3 hours to confirm completion of the end cap. The reaction mixture was then diluted a second time with cyclobutyl hydrazine (400 mL / mol). The solution was filtered through a 15 μm filter using a 2 kg/cm 2 nitrogen pressure in a filter press funnel to remove salt. Finally, a salt-free polymer solution was slowly added to the deionized water by high-speed stirring. The block copolymer was recovered in 3 ml/g of polymer. The precipitated polymer was recovered by filtration. The polymer of Precipitate-42-200724571 (39) was honed and refluxed three times with deionized water at 90 °C. 'To completely remove all salts and ring mills. The precipitated polymer was then filtered and dried in a 140 ° C oven until the water content determined by Karl Fischer titration was < 0.5%. Block copolymer based polystyrene The GPC analysis of the standard showed a Μη of 8 5,000, a Mw of 1 20,000 and an MWD of 1.41. Therefore, the copolymer produced had a molecular weight much higher than the two homoblocks as monomer units. Block copolymer powder It was then mixed with 0.25% heat stabilizer and granulated using a twin-screw extruder. The Tg and specific gravity of PSSD were 259 °C and 1.29, respectively, while those of TMSSS were 268 1: and 1.31. Block copolymer (TMDPSS) The transparent particles showed a DSC Tg of 264t: and a specific gravity of 1.31. The particle transparency of the product, the single GP C peak, the intermediate Tg and the specific gravity clearly indicate that the block copolymer of PSSD and TMPSS has indeed been formed and the product is not only a blend of the two homopolymers PSSD and TMPPS. The detailed properties are listed in Table 1. The detailed chemical reaction is shown in (Figure IV). Example 8: TMBPSS: 50: 50 PSSB: Block copolymer of TMPSS The TMBPSS (PSSB: TMPSS) block copolymer was prepared using the following three-part process. Part 1 · Preparation of PSSB Blocks PS SB was prepared using biphenol and CSB as monomers. The experimental configuration as described in Example 1 was used. Cyclopentane (4410 g, 3500 ml/mole) and toluene (1〇〇〇-43-200724571 (40) ml/mole) were placed in a flask, and nitrogen bubbles were continuously passed through and heated to 45 liters. Add 4,4' bis[(4-chlorophenyl)sulfonyl]biphenyl (CSB) (523 g) and biphenol ([86 g) to the flask, CSB: DHDPS is 1·〇4 : 1·〇〇莫耳比, the reaction mixture was stirred for 3 minutes. Anhydrous sodium carbonate (1 23 g) was added. Wash in a flask to maintain a nitrogen atmosphere. Toluene is used as an azeotropic solvent. The remaining methods are the same as those described in the first part of Example 1. The resulting homoblock had a GPC molecular weight of 19η 19,000, Mw of 23,000 and MWD 1.21. Part 2: Preparation of TMPSS homoblocks TMPSS was prepared using TMDHDPS and CSB as monomers. Cyclopentane (4410 g, 3500 ml/mole) and toluene (1 ml/mol) were placed in a flask, and nitrogen bubbles were continuously passed through and heated to 45 °C. Add 4,4' bis[(4-chlorophenyl)sulfonyl]biphenyl (CSB) (503 g) and tetramethyldihydroxydiphenyl hydrazine (3 09 g TMDHDPS) to the flask, TMDHDPS: The CSB was 1.01: 1.00 molar ratio and the reaction mixture was stirred for 30 minutes. Anhydrous sodium carbonate (123 g) was added. Toluene is used as an azeotropic solvent. The remaining methods are the same as those described in the second part of Example 1. The resulting homoblock had a GPC molecular weight of 3,000 23,000, Mw of 26,000 and MWD 1.11. Part 3 · Preparation of block copolymer -44- 200724571 (41) The reaction mixture of the first part and the second part was mixed at an equal weight ratio, and block polymerization was carried out at 230 °C. After the desired M W (as indicated by GP C) was reached, the reaction mixture was quenched with cyclohexane (504 g, 400 mL / m) and the temperature was reduced to 210 °C. Methyl chloride gas was then bubbled through the reaction mixture over a period of 3 hours to determine completion of the end cap. The reaction mixture was then diluted a second time with cyclobutyl hydrazine (400 ml/mole). The polymer solution was filtered through a 15 micron filter using a 2 kg/cm 2 nitrogen pressure in a filter press funnel to remove salts. Finally, the block copolymer was recovered by slowly adding a salt-free polymer solution to deionized water (13 ml/g polymer) under high-speed stirring. The precipitated polymer is then recovered by filtration. The precipitated polymer was honed and refluxed three times with deionized water at 90 °C to completely remove all salts and cyclopentane. The precipitated polymer was then filtered and dried in a 140 ° C oven until the water content determined by Karl Fischer titration < 0.5%. GPC analysis of the block copolymer based on polystyrene standards showed a Μη of 88,000, a Mw of 124,000 and an MWD of 1.40. Therefore, the copolymer produced has a molecular weight ' much higher than that of the two homoblocks as a monomer unit. The block copolymer powder was then mixed with 0.25% thermal stabilizer and granulated using a twin screw extruder. The Tg and specific gravity of PS SB are 270 ° C and 1.33, while those of TMSSS are 268 ° C and 1.31. The transparent particles of the block copolymer (TMBPSS) showed a DSC Tg of 268 ° C and a specific gravity of 1.32. The particle transparency of the product, the single GP C peak, the intermediate Tg and the specific gravity clearly indicate that the block copolymer of PSSB and TMPSS has indeed been formed and the product is not only a blend of the two homopolymers PSSB and TMPPS. -45- 200724571 (42) The detailed properties are listed in Table 1. The detailed chemical reaction is shown in (Figure V). Example 9: TMDPPSU: 50: 50 PPSU: Block copolymer of TMPSS The PPSU-TMPSS block copolymer was prepared using the following three-part method. Part 1: Preparation of PPSU homoblocks PPSU is based on biphenol and DCDPS. Made from monomers. The experimental configuration as described in Example 1 was used. Cyclopentane (44 10 g, 3500 ml/mole) and toluene (1000 ml/mole) were placed in a flask, and nitrogen bubbles were continuously passed through and heated to 45 °C. 4,4'-Dichlorodiphenyl hydrazine (DCDPS) (298 g) and biphenol (186 g) were added to the flask, and the DCDPS: DHDPS system was 1.04: 1.00 mol ratio, and the reaction mixture was stirred for 30 minutes. Anhydrous sodium carbonate (1 23 g) was added. Wash in a flask to maintain a nitrogen atmosphere. Toluene is used as a boiling solvent. The remaining methods are the same as those described in the first part of Example 1. The resulting homoblock had a GPC molecular weight of Mn 23,000, Mw 29, and MWD 1.26. Part 2: Preparation of TMPSS homoblocks TMPSS was prepared using TMDHDPS and CSB as monomers. Cyclopentane (4410 g, 3500 ml/mole) and toluene (1〇00 -46-200724571 (43) ml/mole) were placed in a flask, and nitrogen bubbles were continuously passed through and heated to 45. Oh. Add 4,4, bis[(4-chlorophenyl)sulfonyl]biphenyl (CSB) (5 03 g) and tetramethyldihydroxydiphenyl hydrazine (3 09 g TMDHDPS) to the flask, TMDHDPS : CSB is 1.01: 1.00 molar ratio, and the reaction mixture is stirred for 3 minutes. Anhydrous sodium carbonate (1 23 g) was added. Toluene is used as an azeotropic solvent. The remaining methods are the same as those described in the second part of Example 1. The resulting homoblock has a GPC molecular weight of 5,000 25,000, Mw of 35,000 and MWD 1.40. Part 3: Preparation of block copolymers The reaction mixture of Part 1 and Part 2 is mixed at equal weight ratios and block polymerization is carried out at 23 (TC). After reaching the desired MW (as indicated by GPC), the reaction is carried out. The mixture was quenched with cyclobutyl hydrazine (504 g, 400 mL / m) and the temperature was reduced to 210 ° C. The methyl chloride gas was then bubbled through the reaction mixture over 3 hours to complete the end closure. The reaction mixture was then diluted a second time with cyclobutyl hydrazine (400 ml/mol). The polymer solution was filtered through a 15 micron filter using a 2 kg/cm 2 nitrogen pressure in a filter press funnel to remove salts. The block copolymer was recovered by slowly adding a salt-free polymer solution to deionized water (13 ml/g polymer) under high-speed stirring, and then the precipitated polymer was recovered by filtration. Honing and refluxing with deionized water three times at 90 ° C to completely remove all salts and cyclobutyl hydrazine. The precipitated polymer was then filtered and dried in a 1 40 C oven until it was titrated by Karl Fischer. Water weight -47- 200724571 (44) < 0.5%. The GPC analysis of the segment copolymer based on polystyrene standards showed a Μη of 82,000, a Mw of 115,000 and an MWD of 1.40. Therefore, the copolymer produced had a molecular weight much higher than the two homoblocks as monomer units, indicating preparation. The block copolymer. The block copolymer powder was then mixed with a 0.25% thermal stabilizer and granulated using a twin-screw extruder. The Tg and specific gravity of the PPSU were 220 ° C and 1.29, respectively, while the TMSSS was 268 1: And 1.31. The transparent particles of the block copolymer (TMDPPSU) showed a DSC Tg of 240 ° C and a specific gravity of 1.30. The particle transparency of the product, the single GPC peak, the intermediate Tg and the specific gravity clearly indicate that the blocks of PPSU and TMPSS have indeed been formed. The copolymer and the product are not only a blend of the two homopolymers PPSU and TMPPS. The detailed properties are listed in Table 1. The detailed chemical reaction is shown in (Figure VI). Example 1 〇·· TMDPES · _ 50 : 50 PES : TMPSS The block copolymer was prepared using the following three-step process: Part 1 of the PES-TMPSS block copolymer: Preparation of the PES homoblock The PES system was prepared using DHDPS and DCDPS as monomers. The experiment as described in Example 1 was used. Configuration. Cyclobutane (4410 g, 3 500 ml/mole) and toluene (1 〇〇 () ml/mole) were placed in a flask, continuously passed through a nitrogen bubble, and heated to 45 χ: 4, 4' one two Chlorodiphenyl maple (DCDPS) (298 g) and 4,4,~ dihydroxydiphenyl hydrazine (DHDPS) (250 g) were added to the flask, -48- 200724571 (45) DCDPS ·· DHDPS is 1 · 〇4 : 1 · 0 0 molar ratio, the reaction mixture was stirred for 30 minutes. Anhydrous sodium carbonate (1 2 3 g) was added. Wash in a flask to maintain a nitrogen atmosphere. Toluene is used as an azeotropic solvent. The remaining methods are the same as those described in the first part of Example 1. The resulting homoblock had a GPC molecular weight of 5,000 25,000, Mw 29,000 and MWD 1.16. Part 2: Preparation of TMPSS homoblocks TMPSS was prepared using TMDHDPS and CSB as monomers. Cyclopentane (4410 g, 3500 ml/mole) and toluene (1000 ml/mole) were placed in a flask, and nitrogen bubbles were continuously passed through and heated to 45 °C. Add 4,4' bis[(4-chlorophenyl)sulfonyl]biphenyl (CSB) (503 g) and tetramethyldihydroxydiphenyl hydrazine (3 09 g TMDHDPS) to the flask, TMDHDPS: The CSB was 1.01: 1.00 molar ratio and the reaction mixture was stirred for 30 minutes. Anhydrous sodium carbonate (1 23 g) was added. Toluene is used as an azeotropic solvent. The remaining methods are the same as those described in the second part of Example 1. The resulting homoblock had a GPC molecular weight of 5,000 25,000, Mw of 35,000 and MWD 1.40. Part 3: Preparation of block copolymers The reaction mixture of Part 1 and Part 2 is mixed at equal weight ratios and block polymerization is carried out at 23 (TC). After reaching the desired MW (as indicated by GPC), the reaction is carried out. The mixture was quenched with cyclobutyl hydrazine (504 g, 400 ml/mol-49-200724571 (46)) and the temperature was lowered to 210 ° C. The methyl chloride gas was then bubbled through the reaction mixture over 3 hours to determine The end cap was completed. The reaction mixture was then diluted a second time with cyclobutyl hydrazine (400 mL/mol). The polymer solution was filtered through a 15 micron filter using a 2 kg/cm 2 nitrogen pressure in a filter press funnel. Salt. Finally, the block copolymer was recovered by slowly adding a salt-free polymer solution to deionized water (13 ml/g polymer) under high-speed stirring, and then the precipitated polymer was recovered by filtration. The polymer was honed and refluxed three times with deionized water at 90 ° C to completely remove all salts and cyclobutyl hydrazine. The precipitated polymer was then filtered and dried in a 140 ° C oven until Karl Fischer titration Determined water content < 0.5%. Block GPC analysis of the copolymer based on polystyrene standards showed Μη of 85,000, Mw of 115,000 and M WD of 1.35. Therefore, the copolymer produced had a molecular weight much higher than the two homoblocks as monomer units, indicating preparation The block copolymer. The block copolymer powder was then mixed with 0.25% thermal stabilizer and granulated using a twin-screw extruder. The Tg and specific gravity of the PES were 225 t: and 1.29, while the TMSSS was 26 8 °. C and 1.31. The transparent particles of the block copolymer (TMDPES) showed a DSC Tg of 2 5 5 ° C and a specific gravity of 1.30. The particle transparency of the product, the single GPC peak, the intermediate Tg and the specific gravity clearly indicate that PES and TMPSS have indeed been formed. The block copolymer and the product are not only a blend of two homopolymers PES and TMPPS. The detailed properties are listed in Table 1. The detailed chemical reaction is shown in (Figure VII). Example 11: BPSK: 50: 50 PSSB: PESK Block copolymer-50-200724571 (47) The PSSB-PESK block copolymer was prepared using the following three-part method. Part 1: Preparation of PSSB homoblocks PSSB was prepared using biphenol and CSB as monomers. Use as described in Example 1. The configuration was carried out. Put the ring guanidine (4410 g, 3500 ml/mole) and toluene (1 〇〇〇 ml/mole) into the flask, continuously pass nitrogen bubbles, and heat to 45 ° C. 4, 4 'bis[(4-chlorophenyl)sulfonyl]biphenyl (CSB) (523 g) and biphenol (1 86 g) were added to the flask, CSB: DHDPS was 1.04: 1.00 mol ratio, reaction The mixture was stirred for 30 minutes. Anhydrous sodium carbonate (1 2 3 g) was added. Wash in a flask to maintain a nitrogen atmosphere. Toluene is used as an azeotropic solvent. The remaining methods are the same as those described in the first part of Example 1. The resulting homoblock had GPC·molecular weight 19η 19,000, Mw 23,000 and MWD 1.21. Part 2: Preparation of PESK homoblocks PESK is produced using DCB and DHDPS as monomers. Cyclopentane (4410 g, 3500 ml/mole) and toluene (1 ml/mol) were placed in a flask, and nitrogen bubbles were continuously passed through and heated to 45 °C. Add 4,4'-dichlorodiphenyldiphenyl ketone (DCB) (251 g) and 4,4'-dihydroxydiphenyl hydrazine (DHDPS) (25 3 g) to the flask, DHDPS: The DCB system was 1.01 : 1 · 〇〇 molar ratio, and the reaction mixture -51 - 200724571 (48) was stirred for 30 minutes. Anhydrous sodium carbonate (123 g) was added. Toluene was used as the azeotropic solvent. The remaining methods are the same as those described in the second part of Example 1. The resulting homoblock had a GPC molecular weight of 5,000 25,000, Mw of 35,000 and MWD 1.40. Part 3: Preparation of block copolymer φ The reaction mixture of the first part and the second part was mixed at an equal weight ratio, and block polymerization was carried out at 230 °C. After reaching the desired M W (as indicated by GP C), the reaction mixture was quenched with cyclohexane (5,04 g, 400 ml/m) and the temperature was reduced to 210 °C. Methyl chloride gas was then bubbled through the reaction mixture over a period of 3 hours to determine completion of the end cap. The reaction mixture was then diluted a second time with cyclobutyl hydrazine (400 ml/mole). The polymer solution was filtered through a 15 micron filter using a 2 kg/cm 2 nitrogen pressure in a filter press funnel to remove salts. Finally, the block copolymer was recovered by slowly adding a non-salted polymer solution to deionized water (13 ml/g polymer) under high-speed stirring. The precipitated polymer is then recovered by filtration. The precipitated polymer was honed and refluxed three times with deionized water at 90 °C to completely remove all salts and cyclopentane. The precipitated polymer was then filtered and dried in a 140 ° C oven until the water content determined by Karl Fischer titration < 〇·5% 〇 block copolymer based on polystyrene standards by GPC analysis showed Μη 88,000, The Mw is 124,000 and the MWD is 1.40. Therefore, the copolymer produced has a molecular weight much higher than that of the two homoblocks as a monomer unit, and -52-200724571 (49) represents the preparation of a block copolymer. The block copolymer powder was then mixed with 0.25% thermal stabilizer and granulated using a twin screw extruder. The Tg and specific gravity of PS SB are 270 °C and 1.33, while those of P E S K are 185 °C and 1.2 8. The transparent particles of the block copolymer (BPSK) showed a DSC Tg of 23 5 ° C and a specific gravity of 1 · 3 2 . The particle transparency of the product, the single G P C peak, the intermediate T g and the specific gravity clearly indicate that the block copolymer of PS SB and PESK has indeed been formed and the product is not only a blend of the two homopolymers PS SB and TESK. The details are listed in Table 1. The detailed chemical reaction is shown in (Figure VIII). Example 12: TMDPSU: 50: 50 PSU: Block copolymer of TMPSS The PSU-TMPSS block copolymer was prepared using the following three-part method. Part 1: Preparation of PSU homoblocks # PSU using bisphenol A and DCDPS Made as a monomer. The experimental configuration as described in Example 1 was used. Cyclopentane (4410 g, 3500 ml/mole) and toluene (1000 ml/mole) were placed in a flask, continuously bubbled with nitrogen, and heated to 45 °C. 4,4'~Dichlorodiphenyl hydrazine (DCDPS) (298 g) and bisphenol A (250 g) were added to the flask, DCDPS: bisphenol A was 1·〇4: 1.00 mol ratio, reaction The mixture was stirred for 30 minutes. Anhydrous sodium carbonate (I54 g) was added. Wash in a flask to maintain a nitrogen atmosphere. Toluene is used as a boiling solvent. -53- 200724571 (50) The remaining methods are the same as those described in the first part of the first embodiment. The resulting homoblock has a GPC molecular weight Μ 20,000, MW 25,000 and MWD 1.25. Part 2: Preparation of TMPSS homoblocks TMPSS was prepared using TMDHDPS and CSB as monomers. Cyclopentane (44 10 g, 3500 ml / mol) and toluene (1 ml / mol) were placed in a flask, and nitrogen bubbles were continuously passed through and heated to 45 t:. Add 4,4, bis[(4-chlorophenyl)sulfonyl]biphenyl (CSB) (503 g) and tetramethyldihydroxydiphenyl hydrazine (3 09 g of TMDHDPS) to the flask. TMDHDPS: CSB is 1·〇1: 1.00 molar ratio, and the reaction mixture is stirred for 30 minutes. Anhydrous sodium carbonate (123 g) was added. Toluene is used as an azeotropic solvent. The remaining methods are the same as those described in the second part of Example 1. The resulting homoblock had a GPC molecular weight of 5,000 25,000, Mw of 35,000 and MWD 1.40. Part 3: Preparation of block copolymer The reaction mixture of the first part and the second part was mixed at an equal weight ratio, and block polymerization was carried out at 2200 °C. After reaching the desired M W (as indicated by G P C), the reaction mixture was quenched with cyclohexane (504 g, 400 mL / m) and the temperature was reduced to 200 °C. Methyl chloride gas was then bubbled through the reaction mixture over a period of 3 hours to determine completion of the end cap. The reaction mixture was then diluted a second time with cyclobutyl hydrazine (4 mL/mole). Polymer -54- 200724571 (51) The solution was filtered through a 15 μm filter using a 2 kg/cm 2 nitrogen pressure in a filter press funnel to remove salts. Finally, the block copolymer was recovered by slowly adding a salt-free polymer solution to deionized water (13 ml/g of polymer) under high-speed stirring. The precipitated polymer is then recovered by filtration. The precipitated polymer was honed and refluxed three times with deionized water at 90 °C to completely remove all salts and cyclopentane. The precipitated polymer was then filtered and dried in a 140 ° C oven until the water content determined by Karl Fischer titration < 0.5%. GPC analysis of the block copolymer based on polystyrene standards showed a Μη of 80,000, a Μη of 115,000 and a M WD of 1.44. Therefore, the copolymer produced has a molecular weight far higher than the two homoblocks as monomer units, indicating the preparation of the block copolymer. The block copolymer powder was then mixed with 0.25% thermal stabilizer and granulated using a twin screw extruder. The Tg and specific gravity of the PSU are 190 ° C and 1.29, while the TMSSS is 268 ° C and 1.31. The transparent particles of the block copolymer (TMDPSU) showed a DSC Tg of 23 0 ° C and a specific gravity of 1.30. The particle transparency of the product, the single GPC peak, the intermediate Tg and the specific gravity clearly indicate that the block copolymer of PES and TMPSS has indeed been formed and the product is not only a blend of the two homopolymers PSU and TMPPS. The detailed properties are listed in Table 1. The detailed chemical reaction is shown in (Figure IX). Various homoblocks are prepared using one or more dichloro compounds and one or more dihydroxy compounds, some of which are listed below: Aromatic dihalogen compounds: Dichlorodiphenyl milling (DCDPS), 4,4'-double ( 4-chlorophenylsulfonyl)biphenyl (CSB), dichlorodiphenyl ketone, dichlorodiphenyl ether, -55- 200724571 (52) dichlorobiphenyl, dichlorodiphenylmethylene , dimethyldichlorodiphenyl hydrazine, tetramethyldichlorodiphenyl fluorene, dihalodiphenylbiphenyl, dihalodiphenoxybiphenyl, dihalodiphenylbiphenyl diether (二飒 or 二_) (ci-c6h4-c6h4-x-c6h4-c6h4-x-c6h4-c6h4-cl),

C1-C6H4-X-C6H4-C6H4-Y-C6H4-C6H4-C1-, C1-C6H4-X-C6H4-C6H4-Y-C6H4-C1-, C1-C6H4-C6H4-X-C6H4-Y-C6H4-C6H4-C1-, C1-C6H4-C6H4-X-C6H4-Y-C6H4-C1,其中 X= -Ο-,-so2-,-CO-,-ch2- 或任何兩種 C1-C6H4-C6H4-X-C6H4-C6H4-Y-C6H4-C6H4-CL 其中 X = -so2-, -CO-, -ch2-且 Y 二 :-0 -, -S Ο 2 - ’ -CO-, -CH2-, 且-Cl係表示任何鹵素; 之組合物。 芳族二羥基化合物: 二羥基二苯基楓(DHDPS )、雙酚A、聯苯酚、氫醌 、二甲基二羥基二苯基颯、四甲基二羥基二苯基颯、四甲 基雙酚A、四甲基聯苯酚、二羥基二苯基酮、雙(羥基苯 基磺醯基)聯苯、雙(羥基苯基酮)聯苯、雙(羥基苯氧 基)聯苯、HO-C6H4X-C6H4-C6H4-Y-C6H4-OH 其中 X & Y = -0-,-S02-,-CO-,-ch2 -且苯基或聯苯環可具有一或 兩個甲基取代,HO-C6H4-X-C6H4-Y-C6H4-OH,具有或不 具有甲基取代。 -56-C1-C6H4-X-C6H4-C6H4-Y-C6H4-C6H4-C1-, C1-C6H4-X-C6H4-C6H4-Y-C6H4-C1-, C1-C6H4-C6H4-X-C6H4-Y-C6H4- C6H4-C1-, C1-C6H4-C6H4-X-C6H4-Y-C6H4-C1, where X=-Ο-, -so2-, -CO-, -ch2- or any two C1-C6H4-C6H4-X -C6H4-C6H4-Y-C6H4-C6H4-CL where X = -so2-, -CO-, -ch2- and Y two:-0 -, -S Ο 2 - ' -CO-, -CH2-, and - Cl is a composition representing any halogen; Aromatic dihydroxy compounds: dihydroxydiphenyl maple (DHDPS), bisphenol A, biphenol, hydroquinone, dimethyl dihydroxy diphenyl hydrazine, tetramethyl dihydroxy diphenyl hydrazine, tetramethyl bis Phenol A, tetramethylbiphenol, dihydroxydiphenyl ketone, bis(hydroxyphenylsulfonyl)biphenyl, bis(hydroxyphenyl ketone)biphenyl, bis(hydroxyphenoxy)biphenyl, HO- C6H4X-C6H4-C6H4-Y-C6H4-OH wherein X & Y = -0-, -S02-, -CO-, -ch2 - and the phenyl or biphenyl ring may have one or two methyl substitutions, HO -C6H4-X-C6H4-Y-C6H4-OH, with or without methyl substitution. -56-

Claims (1)

200724571 (1) 十、申請專利範圍 1 · ~種製備嵌段共聚物之方法,該嵌段共聚物包含 ’ 至少兩種均嵌段,該均嵌段選自PSSD、PSSB、TPES、 · pss、TMPSS 或 PESK 或選自至少一種 PSSD、PSSB、 TPES > PSS > TMPSS 或 PESK 及至少一種 PPSU、PES 或 PSU ’其中該均嵌段各具有至少爲1〇〇〇之相同或相異分子 量且具有總重量之至少5 %,其中該嵌段共聚物具有至少 φ 2000之分子量,該方法步驟包含: (a )藉著於至少一種鹼之存在下並視情況於至少一 種溶劑中且另外視情況於共沸劑之存在下加熱至少一種芳 族二醇/二羥基化合物與至少一種芳族二鹵基化合物(其 中一種含有至少一個硼基)以製備前述各種均嵌段, (b )令前述均嵌段一起於介於1 3 (TC至2 5 (TC間之溫 度下並視情況於至少一種溶劑中反應,且另外視情況接著 將該嵌段共聚物之末端封蓋,及 # ( c )回收該嵌段共聚物。 2.如申請專利範圍第1項之方法,其中該嵌段共聚 物係藉由洗滌該反應物質以去除鹽及鹼及視情況存在之溶 劑而回收。 ' 3.如申請專利範圍第1項之方法,其中在至少一種 溶劑中所製備之嵌段共聚物係藉著濾出該鹽並於水或 MeOH或水與MeOH之混合物中沉澱該嵌段共聚物且進一 步經過濾、洗滌及乾燥該嵌段共聚物而自溶劑回收。 4.如申請專利範圍第1項之方法,其中在至少一種 -57- 200724571 (2) 溶劑中所製備之嵌段共聚物係藉由過濾該鹽並餾除溶劑而 回收。200724571 (1) X. Patent Application No. 1 - A method for preparing a block copolymer comprising 'at least two homoblocks selected from the group consisting of PSSD, PSSB, TPES, · pss, TMPSS or PESK or selected from at least one of PSSD, PSSB, TPES > PSS > TMPSS or PESK and at least one PPSU, PES or PSU 'where the homoblocks each have an identical or different molecular weight of at least 1 Å and Having at least 5% by weight, wherein the block copolymer has a molecular weight of at least φ 2000, the method step comprising: (a) by the presence of at least one base and optionally in at least one solvent and optionally Heating at least one aromatic diol/dihydroxy compound and at least one aromatic dihalogen compound (one of which contains at least one boron group) in the presence of an entraining agent to prepare the aforementioned various homoblocks, (b) The blocks are together at a temperature between 1 and 3 (TC to 2 5 (between TC and optionally in at least one solvent, and optionally the end of the block copolymer is then capped, and # ( c ) Recycling the block 2. The method of claim 1, wherein the block copolymer is recovered by washing the reaction material to remove salts and bases and optionally solvents. The method of claim 1, wherein the block copolymer prepared in at least one solvent is precipitated by the salt and the block copolymer is precipitated in water or MeOH or a mixture of water and MeOH and further filtered and washed. The block copolymer is dried and recovered from the solvent. 4. The method of claim 1, wherein the block copolymer prepared in at least one solvent of -57-200724571 (2) is filtered by the salt and The solvent was distilled off and recovered. 5 .如申請專利範圍第1項之方法,其中該芳族二鹵 基化合物係選自二氯二苯基楓(DCDPS) 、4,4’一雙(4一 氯苯基磺醯基)聯苯(CSB)、二氯二苹基酮、二氯二苯 基醚、二氯聯苯、二氯二苯基亞甲基、二甲基二氯二苯基 楓、四甲基二氯二苯基颯、二鹵基二苯基聯苯、二鹵基二 苯氧基聯苯、二鹵基二苯基聯苯二醚(二颯或二酮) (C1-C6H4-C6H4-X-C6H4-C6H4-X-C6H4-C6H4-CL), C1-C6H4-X-C6H4-C6H4-Y-C6H4-C6H4-C1-, C1-C6H4-X-C6H4-C6H4-Y-C6H4-C1-, C1-C6H4-C6H4-X-C6H4-Y-C6H4-C6H4-C1-, C1-C6H4-C6H4-X-C6H4-Y-C6H4-C1,其中 X = -0- ’ -S〇2- ’ -CO- ’ -CH〗· 或任何兩種 C1-C6H4-C6H4-X-C6H4-C6H4-Y-C6H4-C6H4-CL 其中 x = =-0 -, -S 0 2 - 5 -CO-, -ch2-且 Y: =-0 -, -S 0 2 - ’ -CO-, -CH2-, 且-Cl係表示任何鹵素; 之組合物。 6.如申請專利範圍第1項之方法,其中該芳族二醇 /二羥基化合物係選自二羥基二苯基颯(DHDPS )、雙酚 A、聯苯酚、氫醌、二甲基二羥基二苯基楓、四甲基二羥 基二苯基礪(TMDHDPS)、四甲基雙酚A、四甲基聯苯酚 -58- 200724571 (3) 、一經基一苯基嗣、雙(經基苯基礦酶基)聯苯(HSB) 、雙(羥基苯基酮)聯苯、雙(羥基苯氧基)聯苯、 HO-C6H4X-C6H4-C6H4-Y-C6H4-OH 其中 X & Y二-〇-, ·· -S02-,-CO-,-CH2-且苯基或聯苯環可具有一或兩個甲基 - 取代, HO-C6H4-X-C6H4-Y-C6H4-OH,具有或不具有甲基取 代。 φ 7.如申請專利範圍第1項之方法,其中該芳族二醇 或該芳族一鹵基化合物係等莫耳數量或一種較另一種多出 高達15莫耳%。 8 ·如申請專利範圍第1項之方法,其中該均嵌段各 具有該嵌段共聚物總重之至少10%。 9 .如申請專利範圍第1項之方法,其中該均嵌段各 具有該嵌段共聚物總重之至少25%。 10·如申請專利範圍第1項之方法,其中該均嵌段各 • 具有該嵌段共聚物總重之至少4 0 %。 11.如申請專利範圍第1項之方法,其中該溶劑係爲 二甲基乙醯胺(DMA c)、二甲基亞礪(DMSO)、環丁礪 、N -甲基吡咯啶酮、二苯基颯、二甲基颯或其混合物。 ~ 12.如申請專利範圍第1項之方法,其中該鹼係爲金 屬氫氧化物或二或多種金屬氫氧化物之混合物。 1 3 ·如申請專利範圍第1 2項之方法,其中該金屬氫 氧化物係爲N a Ο Η、Κ Ο Η或其混合物。 14.如申請專利範圍第1項之方法,其中該鹼係爲金 -59- 200724571 (4) 屬碳酸鹽或二或多種金屬碳酸鹽之混合物。 15·如申請專利範圍第1 4項之方法,其中該金屬碳 酸鹽係爲Na2C03、K2C03或其混合物。 1 6 ·如申請專利範圍第1項之方法,其中該鹼係爲金 屬氫氧化物與金屬碳酸鹽之混合物。 17.如申請專利範圍第1項之方法,其中該方法步驟 (a)或(b)或該兩步驟皆於介於160°C至250°C間之溫 I 度下進行。 18·如申請專利範圍第1項之方法,其中該共沸劑係 爲甲苯。 1 9 ·如申請專利範圍第1項之方法,其中該共沸劑係 爲單氯苯。 20.如申請專利範圍第1項之方法,其中該末端封蓋 係使用MeCl進行。 2 1 · —種製備實質上參照說明書之實施例所描述的嵌 t 段共聚物之方法。 22. —種包含至少兩種均嵌段之嵌段共聚物,該均嵌 段選自 PSSD、PSSB、TPES、PSS、TMPSS 或 PESK 或選 白至少一種 PSSD、PSSB、TPES、PSS、TMPSS 或 PESK 及至少一種PPSU、PES或PSU,該等均嵌段係直接鍵合 或藉鍵合基團鍵合以形成嵌段共聚物鏈,其中該均嵌段各 具有至少爲1 000之相同或相異分子量且具有總重量之至 少5%且其中該嵌段共聚物係具有至少2000之分子量。 2 3 ·如申請專利範圍第2 2項之嵌段共聚物,其中該 -60- 200724571 (5) 均嵌段各具有2000至10000之分子量。 24.如申請專利範圍第2 2項之嵌段共聚物,其中該 • 均嵌段各具有15000至50000之分子量。 ' 25.如申請專利範圍第22項之嵌段共聚物,其中該 - 嵌段共聚物具有5000至150000之分子量。 26.如申請專利範圍第22項之嵌段共聚物,其中該 嵌段共聚物具有30000至150000之分子量。 φ 2 7.如申請專利範圍第2 2項之嵌段共聚物,其中該 均嵌段各具有總重之至少1 〇 %。 28 .如申請專利範圍第22項之嵌段共聚物,其中該 均嵌段各具有總重之至少2 5 %。 2 9.如申請專利範圍第22項之嵌段共聚物,其中該 均嵌段各具有總重之至少4 0 %。 30.如申請專利範圍第22項之嵌段共聚物,其中該 鍵合基團係藉由二醇或二醇鹽與二鹵化物反應而形成。 # 3 1 .如申請專利範圍第3 0項之嵌段共聚物,其中該 二醇或二醇鹽係選自芳族二羥基化合物。 3 2.如申請專利範圍第30項之嵌段共聚物,其中該 二鹵化物係爲芳基二氯化物。 — 3 3.如申請專利範圍第22項之嵌段共聚物,其中該 均嵌段係使用至少一種芳族二醇/二羥基化合物與至少一 種芳族二鹵基化合物製備,其中之一係含有至少一個碾1基 〇 3 4.如申請專利範圍第33項之嵌段共聚物,其中該 -61 - 200724571 (6) 芳族二鹵基化合物係選自二氯二苯基颯(DCDPS ) 、4,4’ 一雙(4 一氯苯基磺醯基)聯苯(CSB)、二氯二苯基酮、 二氯二苯基醚、二氯聯苯、二氯二苯基亞甲基、二甲基二 氯二苯基礪、四甲基二氯二苯基礪、二鹵基二苯基聯苯、 二鹵基二苯氧基聯苯、二鹵基二苯基聯苯二醚(二颯或二 酮) (C1-C6H4-C6H4-X-C6H4-C6H4-X-C6H4-C6H4-CL), , C1-C6H4-X-C6H4-C6H4-Y-C6H4-C6H4-C1-, C1_C6H4-X-C6H4-C6H4-Y-C6H4-C1-, C1-C6H4-C6H4-X-C6H4-Y-C6H4-C6H4-C1-, C1-C6H4-C6H4-X-C6H4-Y-C6H4-C1,其中 χ= -Ο-,-S02-,-CO-,-CH2- 或任何兩種 ci-c6h4-c6h4-x-c6h4-c6h4-y-c6h4-c6h4-cl 其中 X = -S ◦ 2 - ’ -CO-, -ch2- Y 二 :-0 -, -S 0 2 - 5 -CO-, -ch2 且-Cl係表示任何鹵素; 之組合物。 3 5 .如申請專利範圍第3 3項之嵌段共聚物,其中該 芳族二醇/二羥基化合物係選自二羥基二苯基颯(DHDPS )、雙酚a、聯苯酚、氫醌、二甲基二羥基二苯基礪、四 甲基二羥基二苯基楓(TMDHDPS)、四甲基雙酚A、四甲 基聯苯酚、二羥基二苯基酮、雙(羥基苯基磺醯基)聯苯 (HSB )、雙(羥基苯基酮)聯苯、雙(羥基苯氧基)聯 -62- 200724571 (7) 苯、 HO-C6H4X-C6H4-C6H4-Y-C6H4-OH 其中 X & Y =-ο-,-so2-,-CO-,-CH2-且苯基或聯苯環可具有 一或兩個甲基取代, HO-C6H4-X-C6H4-Y-C6H4-OH,具有或不具有甲基取 代。 3 6 . —種實質上參照說明書實施例所描述之嵌段共聚 物。5. The method of claim 1, wherein the aromatic dihalogen compound is selected from the group consisting of dichlorodiphenyl maple (DCDPS) and 4,4'-double (4-chlorophenylsulfonyl). Benzene (CSB), dichlorodiyl ketone, dichlorodiphenyl ether, dichlorobiphenyl, dichlorodiphenylmethylene, dimethyldichlorodiphenyl maple, tetramethyldichlorodiphenyl Base, dihalodiphenylbiphenyl, dihalodiphenoxybiphenyl, dihalodiphenylbiphenyl diether (dioxa or diketone) (C1-C6H4-C6H4-X-C6H4- C6H4-X-C6H4-C6H4-CL), C1-C6H4-X-C6H4-C6H4-Y-C6H4-C6H4-C1-, C1-C6H4-X-C6H4-C6H4-Y-C6H4-C1-, C1-C6H4 -C6H4-X-C6H4-Y-C6H4-C6H4-C1-, C1-C6H4-C6H4-X-C6H4-Y-C6H4-C1, where X = -0- ' -S〇2- ' -CO- ' - CH〗· or any two of C1-C6H4-C6H4-X-C6H4-C6H4-Y-C6H4-C6H4-CL where x ==-0 -, -S 0 2 - 5 -CO-, -ch2- and Y: =-0 -, -S 0 2 - '-CO-, -CH2-, and -Cl represents any halogen; 6. The method of claim 1, wherein the aromatic diol/dihydroxy compound is selected from the group consisting of dihydroxydiphenyl hydrazine (DHDPS), bisphenol A, biphenol, hydroquinone, dimethyl dihydroxyl Diphenyl maple, tetramethyldihydroxydiphenyl hydrazine (TMDHDPS), tetramethyl bisphenol A, tetramethylbiphenol-58- 200724571 (3), mono-phenyl hydrazine, bis(phenylphenyl) Mineral enzyme) biphenyl (HSB), bis(hydroxyphenylketone)biphenyl, bis(hydroxyphenoxy)biphenyl, HO-C6H4X-C6H4-C6H4-Y-C6H4-OH wherein X & Y di- 〇-, ···-S02-,-CO-,-CH2- and the phenyl or biphenyl ring may have one or two methyl-substituted, HO-C6H4-X-C6H4-Y-C6H4-OH, with or Does not have a methyl substitution. Φ 7. The method of claim 1, wherein the aromatic diol or the aromatic monohalogen compound is in an amount of more than or equal to 15 mol% more than the other. 8. The method of claim 1, wherein the homoblocks each have at least 10% of the total weight of the block copolymer. 9. The method of claim 1, wherein the homoblocks each have at least 25% of the total weight of the block copolymer. 10. The method of claim 1, wherein the homoblock each has at least 40% of the total weight of the block copolymer. 11. The method of claim 1, wherein the solvent is dimethylacetamide (DMA c), dimethyl hydrazine (DMSO), cyclobutyl hydrazine, N-methyl pyrrolidone, two Phenylhydrazine, dimethylhydrazine or a mixture thereof. The method of claim 1, wherein the base is a metal hydroxide or a mixture of two or more metal hydroxides. The method of claim 12, wherein the metal hydroxide is N a Ο Η, Κ Η or a mixture thereof. 14. The method of claim 1, wherein the base is a mixture of gold-59-200724571 (4) carbonate or two or more metal carbonates. The method of claim 14, wherein the metal carbonate is Na2C03, K2C03 or a mixture thereof. The method of claim 1, wherein the base is a mixture of a metal hydroxide and a metal carbonate. 17. The method of claim 1, wherein the method step (a) or (b) or both steps are carried out at a temperature between 160 ° C and 250 ° C. 18. The method of claim 1, wherein the entrainer is toluene. The method of claim 1, wherein the entrainer is monochlorobenzene. 20. The method of claim 1, wherein the end capping is performed using MeCl. 2 1 - A method of preparing a t-stacked copolymer substantially as described in the examples of the specification. 22. A block copolymer comprising at least two homoblocks selected from the group consisting of PSSD, PSSB, TPES, PSS, TMPSS or PESK or at least one PSSD, PSSB, TPES, PSS, TMPSS or PESK And at least one PPSU, PES or PSU, the homoblocks being bonded directly or by a bonding group to form a block copolymer chain, wherein the homoblocks each have at least 1,000 identical or different Molecular weight and having a total weight of at least 5% and wherein the block copolymer has a molecular weight of at least 2000. 2 3 · The block copolymer of claim 2, wherein the -60-200724571 (5) homoblock each has a molecular weight of from 2,000 to 10,000. 24. The block copolymer of claim 22, wherein the homoblocks each have a molecular weight of from 15,000 to 50,000. 25. The block copolymer of claim 22, wherein the block copolymer has a molecular weight of from 5,000 to 150,000. 26. The block copolymer of claim 22, wherein the block copolymer has a molecular weight of from 30,000 to 150,000. Φ 2 7. The block copolymer of claim 22, wherein the homoblocks each have at least 1% by weight of the total weight. 28. The block copolymer of claim 22, wherein the homoblocks each have at least 25 % of the total weight. 2. The block copolymer of claim 22, wherein the homoblocks each have at least 40% of the total weight. 30. The block copolymer of claim 22, wherein the bonding group is formed by reacting a diol or a glycol salt with a dihalide. #3 1 . The block copolymer of claim 30, wherein the diol or glycol salt is selected from the group consisting of aromatic dihydroxy compounds. 3. The block copolymer of claim 30, wherein the dihalide is an aryl dichloride. The block copolymer of claim 22, wherein the homoblock is prepared using at least one aromatic diol/dihydroxy compound and at least one aromatic dihalogen compound, one of which contains At least one of the bases of the invention, wherein the block copolymer of claim 33, wherein the -61 - 200724571 (6) aromatic dihalogen compound is selected from the group consisting of dichlorodiphenyl hydrazine (DCDPS), 4,4' a pair of (4-chlorophenylsulfonyl)biphenyl (CSB), dichlorodiphenyl ketone, dichlorodiphenyl ether, dichlorobiphenyl, dichlorodiphenylmethylene, Dimethyldichlorodiphenyl hydrazine, tetramethyldichlorodiphenyl fluorene, dihalodiphenylbiphenyl, dihalodiphenoxybiphenyl, dihalodiphenylbiphenyl diether ( Di- or diketone) (C1-C6H4-C6H4-X-C6H4-C6H4-X-C6H4-C6H4-CL), , C1-C6H4-X-C6H4-C6H4-Y-C6H4-C6H4-C1-, C1_C6H4- X-C6H4-C6H4-Y-C6H4-C1-, C1-C6H4-C6H4-X-C6H4-Y-C6H4-C6H4-C1-, C1-C6H4-C6H4-X-C6H4-Y-C6H4-C1, where χ = -Ο-,-S02-,-CO-,-CH2- or any two of ci-c6h4-c6h4-x-c6h4-c6h4-y-c6h4-c6h4-cl where X = -S ◦ 2 - '-CO-, -ch2- Y 2 :-0 -, -S 0 2 -5 -CO-, -ch2 and -Cl represents any halogen; 3. The block copolymer of claim 3, wherein the aromatic diol/dihydroxy compound is selected from the group consisting of dihydroxydiphenyl hydrazine (DHDPS), bisphenol a, biphenol, hydroquinone, Dimethyldihydroxydiphenylphosphonium, tetramethyldihydroxydiphenyl Maple (TMDHDPS), tetramethylbisphenol A, tetramethylbiphenol, dihydroxydiphenyl ketone, bis(hydroxyphenylsulfonate) Biphenyl (HSB), bis(hydroxyphenylketone)biphenyl, bis(hydroxyphenoxy)-62-200724571 (7) benzene, HO-C6H4X-C6H4-C6H4-Y-C6H4-OH where X & Y =-ο-, -so2-, -CO-, -CH2- and the phenyl or biphenyl ring may have one or two methyl substitutions, HO-C6H4-X-C6H4-Y-C6H4-OH, With or without methyl substitution. 3 6. A block copolymer substantially as described with reference to the specification examples. -63- 200724571 七、指定代表圖: (一) 、本案指定代表圖為:無 (二) 、本代表圖之元件代表符號簡單說明:無-63- 200724571 VII. Designated representative map: (1) The representative representative of the case is: None (2), the representative symbol of the representative figure is a simple description: None 八、本案若有化學式時,請揭示最能顯示發明特徵的化學 式:無8. If there is a chemical formula in this case, please reveal the chemical formula that best shows the characteristics of the invention: none
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