TW491865B - Novel copolyester material having non-round cross-section - Google Patents
Novel copolyester material having non-round cross-section Download PDFInfo
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491865 五、發明說明(1) 本發明是合成一種共聚酯材料,可以紡成不規 形狀的纖維,尤其是具凹溝槽橢圓形貝殼狀截面, 不規則形狀的纖維織成的布,所做衣服會具有很好 球的特性,良好的手感(觸感)及乾爽的特性。 在2 0年前’就有一些專利文獻提到如何製造截 則化的纖維’如美國專利第3, 9 1 4, 488號,美國專身 4, 634, 625號和美國專利第4, 707, 407號等專利說明 告訴人們連續式製造截面不規則化纖維和棉的製造 另外,美國專利申請案號08/662, 804號(1996年) 08/778,462 號(1997年),〇8/778,458 號(1997 年 專利說明書’美國專利第5, 591,523和5, 626,96 1號 明書,及世界專利第WO 97/02374 (1997) 、WO 08/497,495 (1995) ^ff〇 97/02372 (1997) > WO 08/642,650 (1996) 、ff〇 97/02373 (1997)等專; 書中,告訴人們如何紡不規則截面的紡絲方法,條 嘴如何設計。但上述專利雖可以紡出不規則截面的 棉’卻無法改善不規則絲或棉所織布做成衣服之容 球的問題。 美國專利第3,3 3 5,2 11號專利說明書中,告訴 聚對本一曱酸二乙_中加入石夕酸乙醋(tetraethy silicate)來調整相對黏度(reiative viscosit 至17 ’及在275 °C,在熔融粘度為ι,〇〇〇至6,〇〇〇泊 )時,可改善起毛球現象。 美國專利第3, 018, 272和3, 104, 450號專利說! 則截面 因此, 抗起毛 面不規 J第 書,就 方法。 9 )等之 專利說 Μ說明 件及紡 絲和 易起毛 兔們在 )在10 (poise 書告訴 491865 五、發明說明(2) 我們於合成聚對苯二甲酸二乙酯之過程中,加入3,5一二 (間-經基乙氧基羰基)苯確酸納,可改善起毛球現象, 其合成共聚酯之相對黏度為14. 5〜17.5。491865 V. Description of the invention (1) The present invention is a synthetic polyester material that can be spun into irregularly shaped fibers, especially a cloth woven with irregular grooved oval shell-shaped cross-sections and irregularly shaped fibers. Making clothes will have good ball characteristics, good feel (touch) and dry characteristics. Twenty years ago, 'there are some patent documents mentioning how to make cut fibers', such as US Patent No. 3, 9 1 4, 488, US Patent No. 4, 634, 625, and US Patent No. 4, 707. No. 407 and other patent specifications tell people the continuous manufacturing of irregular cross-section fibers and cotton. In addition, U.S. Patent Application No. 08/662, 804 (1996) 08 / 778,462 (1997), 08 / 778,458 No. (1997 Patent Specification 'U.S. Patent Nos. 5,591,523 and 5,626,96 Certificate 1 and World Patent Nos. WO 97/02374 (1997), WO 08 / 497,495 (1995) ^ ff〇97 / 02372 ( (1997) > WO 08 / 642,650 (1996), ff〇97 / 02373 (1997) and other special books; the book tells people how to spin spinning methods with irregular cross-sections and how to design nozzles. But the above patents can be spun out Cotton with an irregular cross section does not improve the problem of voluminous balls made of irregular silk or cotton. US Patent No. 3,3 3,5,2 11 tells Poly _ Add tetraethy silicate to adjust the relative viscosity (reiative viscosit to 17 'and at 275 ° C, at a melt viscosity of ι, 6,000 to 6,000 poise), can improve the fluff phenomenon. US Patent Nos. 3,018,272 and 3,104,450 said! The cross section therefore, Anti-pilling surface irregularities J. Book, on the method. 9) and other patents say that M description parts and spinning and easy-piling rabbits are) at 10 (poise book tells 491865 V. Description of the invention (2) 5〜 During the process of diethyl phthalate, the addition of 3,5 one bis (m-transylethoxycarbonyl) sodium benzoate can improve the fluff phenomenon, and the relative viscosity of the synthetic copolyester is 14. 5 ~ 17.5.
美國專利第5, 559, 205和5, 607, 765號專利說明中,提 到加入0·5至5莫耳比之3, 5-二(間-羥基乙氧基羰基)苯 磺酸鈉後,其可改善起毛球現象,但卻不易紡絲,因此將 單體改為3, 5 -二(間-羥基乙氧基羰基)苯續酸鋰後,可 改善紡絲情形。而世界專利第⑽92/1 31 20號專利說明書 中提到上述加入3, 5-二(間-羥基乙氧基羰基)苯磺酸鈉 或鉀鹽類後’又可以加入三氧化二鈦,做為消光劑。 美國專利第3,3 3 5,2 11號專利提到可以用聚乙二醇來 改善加入3, 5 -二(間-羥基乙氧基幾基)苯磺酸鈉所合成 共聚酯之紡絲性和起毛球現象。但因加入聚乙二醇 (Polyethylene glycol )後,其紡絲物性及挺性不夠, 因此不易紡成特殊形狀的纖維,故再加入矽酸乙酯或三甲 醇丙烧(Trimethylel propane)和三氧化二鈦,用於調 整合成之相對粘度,改善紡絲性及起毛球現象。In US Patent Nos. 5,559,205 and 5,607,765, it is mentioned that after adding 0.5 to 5 moles of sodium 3,5-bis (m-hydroxyethoxycarbonyl) benzenesulfonate It can improve the fluffing phenomenon, but it is not easy to spin. Therefore, changing the monomer to 3,5-bis (m-hydroxyethoxycarbonyl) lithium benzoate can improve the spinning situation. And in the patent specification of World Patent No. 92/1 31 20, it is mentioned that after adding 3, 5-bis (m-hydroxyethoxycarbonyl) benzenesulfonic acid sodium or potassium salt, titanium dioxide can be added to make As a matting agent. U.S. Patent No. 3,3 3 5,2 11 mentions that polyethylene glycol can be used to improve the spinning of copolyesters synthesized by the addition of sodium 3,5-bis (m-hydroxyethoxyquinyl) benzenesulfonate. Silkiness and fluffing. But after adding polyethylene glycol (Polyethylene glycol), its spinning properties and stiffness are not enough, so it is not easy to spin into special-shaped fibers. Therefore, ethyl silicate or trimethylel propane and trioxide are added. Titanium is used to adjust the relative viscosity of the synthesis, improve the spinnability and fluffing phenomenon.
本發明是使用6至1 2個碳之三羧酸或三羧酸酐化合物 (可以脂肪族或芳香族)、3, 5-二(甲氧基羰基)苯磺酸 鹽或3, 5-二(間-羥基乙氧基羰基)苯磺酸鹽或間苯二甲 酸磺酸鹽、聚乙二醇和對苯二甲酸二乙基羥基酯[BHET ; bis (hydroxy ethoxy) terephalate]為反應物,再經由 _化或酯交換及聚縮合反應合成共聚酯,而合成共聚酯的 有酸相對枯度(Acid relative viscosity)為8至12,非The present invention uses 6 to 12 carbon tricarboxylic or tricarboxylic anhydride compounds (which can be aliphatic or aromatic), 3,5-bis (methoxycarbonyl) benzenesulfonate or 3,5-bis ( M-hydroxyethoxycarbonyl) benzenesulfonate or isophthalate sulfonate, polyethylene glycol and diethylhydroxyterephthalate [BHET; bis (hydroxy ethoxy) terephalate] as reactants, and then Co-polyesters are synthesized by chemical or transesterification and polycondensation reactions, and the synthetic copolyesters have an acid relative viscosity of 8 to 12, non-
第5頁 491865 五、發明說明(3) 酸相對枯度(Non- Acid relative viscosity)減掉有酸 相對粘度值在1至3間。 本發明所提到合成共聚酯,其有酸相對粘度值以在9 至11為較佳的範圍。 本發明所提到之6至12個碳之三羧酸或三羧酸酐化合 物,其中6至12個碳之三羧酸化合物可以為1,2, 3 -三羧酸 丙燒(Propane-1,2, 3-tricarboxylic acid )、1,2, 3-三 羧酸苯(Benzene-1,2,3- tricarboxylic acid)、 1,2, 4 -三羧酸苯(Benzene-1,2,4- tricarboxylic acid )、6至12個碳之三羧酸酐化合物可以為1,2, 4-苯三酸酐 (Tricarboxylic anhydride)等。 間苯二甲酸石黃酸鹽可以為間苯二甲酸磺酸鈉(Sod i um salt of sulfoisophthalic acid)、間苯二甲酸磺酸 鉀、間苯二甲酸磺酸鋰、間苯二甲酸磺酸鎂、2, 6-奈二酸 -4-績酸納(2,6-dicarboxylic acid-naphthalene-4 - sulfonic acid ) 、3, 5-環己烷二酸磺酸 鈉(3, 5-cyclohexane dicarboxylic acid-4-su1fonic acid),而3, 5-二(甲氧羰基)苯磺酸鹽可以為3, 5—二 (甲氧羰基)苯確酸鈉、3, 5-二(甲氧羰基)苯續酸鉀、 3, 5-二(甲氧羰基)苯磺酸鋰、3, 5 -二(甲氧羰基)苯磺 酸鎂、3, 5 -二(間-羥基乙氧基羰基)苯磺酸鹽可以 為3, 5 -二(間-經基乙氧基羰基)苯橫酸納、3,5 -二(間-經基乙氧基羰基)苯磺酸鉀、3,5 -二(間_羥基乙氧基羰 基)苯磺酸鋰、3, 5 -二(間-羥基乙氧基羰基)苯磺酸Page 5 491865 V. Description of the invention (3) Non-acid relative viscosity (Non-Acid relative viscosity) minus acid The relative viscosity value is between 1 and 3. The synthetic copolyester mentioned in the present invention has an acid relative viscosity value in a preferred range of 9 to 11. The tricarboxylic acid or tricarboxylic anhydride compound of 6 to 12 carbons mentioned in the present invention, wherein the tricarboxylic acid compound of 6 to 12 carbons may be 1,2,3-tricarboxylic acid propane (Propane-1, 2,3-tricarboxylic acid), Benzene-1,2,3-tricarboxylic acid, Benzene-1,2,4-tricarboxylic acid tricarboxylic acid), 6 to 12 carbon tricarboxylic anhydride compounds may be 1,2,4-tricarboxylic anhydride (Tricarboxylic anhydride) and the like. Isophthalic xanthate can be Sod i um salt of sulfoisophthalic acid, potassium isophthalate sulfonate, lithium isophthalate sulfonate, magnesium isophthalate sulfonate , 2,6-dicarboxylic acid-naphthalene-4-sulfonic acid, sodium 3,5-cyclohexanedicarboxylic acid -4-su1fonic acid), and the 3, 5-bis (methoxycarbonyl) benzenesulfonate can be 3,5-bis (methoxycarbonyl) benzenesulfonic acid sodium, 3,5-bis (methoxycarbonyl) benzene Potassium dibasic acid, lithium 3,5-bis (methoxycarbonyl) benzenesulfonate, magnesium 3,5-bis (methoxycarbonyl) benzenesulfonate, 3,5-bis (m-hydroxyethoxycarbonyl) benzenesulfonate The acid salt may be sodium 3,5-bis (m-xylethoxycarbonyl) benzene phthalate, potassium 3,5-bis (m-xylethoxycarbonyl) benzenesulfonate, 3,5-bis ( M-Hydroxyethoxycarbonyl) benzenesulfonic acid, 3,5-bis (m-hydroxyethoxycarbonyl) benzenesulfonic acid
第6頁 491865 五、發明說明(4) 鎮。 本發明所使用聚乙二醇(Polyethylene glycol)其 -分子量為20 0至5, 0 00,其中以分子量300至2, 00 0為較佳之 分子量。 本發明所使用之對苯二甲酸二乙基羥基酯,是從對苯 二甲酸和乙二醇經由酯化反應,在2 20〜260 t:反應溫度 下合成,或者經由對苯二甲酸二甲酯和乙二醇,在2〇〇〜 250 °C和酯交換觸媒下,反應合成。酯交換反應觸媒可以 為醋酸鎂、醋酸鈣、醋酸錳、醋酸鈷、醋酸鋅和醋酸鉛 本發明所用觸媒以録系化合物(如三氧化二銻、酸錄 等)’錫系化合物[如二丁基亞錫(dibudyltin oxide)、 丁基二月桂錫(dibutyl dilauryl tin)等等],鈦化合物 [如四丁基鈦(tetrabutyl titanate)、四-異丙基鈦 (tetraisopropyltitanate)]等等為聚縮合觸煤,以醋 酸#5、醋酸鎮、醋酸锰、醋酸鉛、醋酸辞、醋酸鉛為酯交 換反應觸媒,也可以聚合觸媒和酯交換反應觸媒和醋酸 鈉、醋酸鉀、醋酸鋰等合用。 本發明製程可以使用安定劑,如三甲基磷酸酯 (trimethyl phosphate)、三苯基磷酸酯(triphenyl phosphate )、磷酸、Irganoxl01〇 等等。 本發明所用之6至12個碳之三叛酸或三藏酸酐化合物 之用量為20〜100 ppm,(以對苯二甲酸二乙基羥基酯為 基準)。其中以40〜50 0 ppm為較佳的使用範圍,3, 5 -二Page 6 491865 V. Description of Invention (4) Town. Polyethylene glycol used in the present invention has a molecular weight of 200 to 5,000, with a molecular weight of 300 to 2,000 being the preferred molecular weight. The diethyl hydroxy terephthalate used in the present invention is synthesized from terephthalic acid and ethylene glycol through an esterification reaction at 2 20 to 260 t: reaction temperature, or via dimethyl terephthalate. Ester and ethylene glycol are synthesized by reaction at 2000 ~ 250 ° C and transesterification catalyst. The transesterification catalyst can be magnesium acetate, calcium acetate, manganese acetate, cobalt acetate, zinc acetate, and lead acetate. The catalysts used in the present invention are recording compounds (such as antimony trioxide, acid recording, etc.) 'tin compounds [such as two Butyl stannous oxide (dibudyltin oxide, dibutyl dilauryl tin, etc.), titanium compounds [such as tetrabutyl titanate, tetraisopropyltitanate], etc. are poly Condensed coal, using acetic acid # 5, acetic acid, manganese acetate, lead acetate, acetic acid, and lead acetate as transesterification reaction catalysts. It can also be used in combination with sodium acetate, potassium acetate, and lithium acetate. . The process of the present invention can use stabilizers, such as trimethyl phosphate, triphenyl phosphate, phosphoric acid, Irganox 100, and the like. The amount of the tri-acid or tri-zoic anhydride compound of 6 to 12 carbons used in the present invention is 20 to 100 ppm (based on diethylhydroxyterephthalate). Among them, 40 ~ 50 0 ppm is the best use range, 3, 5-2
491865 五、發明說明(5) (甲氧基羰基)苯磺酸鹽或3, 5-二(間-羥基乙氧基羰基 )苯確酸鹽或間苯二甲酸磺酸鹽之用量為0.5〜5莫耳% - (以對笨二甲酸二乙基羥基酯為〗〇 〇 % ),其中較佳之使 用量為0·5〜3莫耳%為較佳之使用量,聚乙二醇使用量 為0.5至10重量百分比(以對苯二甲酸二乙基羥基酯為1〇〇 % ),其中以0 · 5至5重量百分比為較佳使用範圍。 茲舉例數個實施例說明如下,所舉實施例僅係對本發 明方法作概括性例示,並無限制本發明範圍之意,就此先 作聲明。491865 V. Description of the invention (5) The amount of (methoxycarbonyl) benzenesulfonate or 3,5-bis (m-hydroxyethoxycarbonyl) benzoate or isophthalate sulfonate is 0.5 ~ 5 mol%-(Diethylhydroxyparaben dicarboxylate is 〇00%), of which the preferred amount is 0.5 ~ 3 mol% is the preferred amount, and the polyethylene glycol is used as 0.5 to 10 weight percent (100% based on diethylhydroxyterephthalate), with 0.5 to 5 weight percent being the preferred range of use. A few examples are described below. The examples described are merely general illustrations of the method of the present invention, and are not intended to limit the scope of the invention.
實施例1 A、 3, 5 -二(間-羥基乙氧基羰基)苯磺酸鈉可直接 從市面上購買(40%之乙二醇溶液)或自已合成如下: (1 )間苯二甲酸磺酸鈉和乙二醇直接酯化反應合成4〇 %之3, 5 -二(間-羥基乙氧基羰基)苯磺酸鈉之乙二醇溶 液’其合成過程需要加入醋酸鈉、醋酸鉀或醋酸鋰等抑制 二乙二醇之生成。其合成條件同一般酯化反應條件。反應 溫度約為2 3 0〜2 5 0 。(:。Example 1 Sodium A, 3, 5-bis (m-hydroxyethoxycarbonyl) benzenesulfonate can be purchased directly from the market (40% ethylene glycol solution) or synthesized as follows: (1) isophthalic acid Sodium sulfonate and ethylene glycol are directly esterified to synthesize 40% of 3,5-bis (m-hydroxyethoxycarbonyl) benzene sulfonate in ethylene glycol solution. The synthesis process requires the addition of sodium acetate and potassium acetate. Or lithium acetate can inhibit the formation of diethylene glycol. The synthesis conditions are the same as the general esterification reaction conditions. The reaction temperature is about 2 3 0 to 2 50. (:.
(2)3,5 -二(甲氧羰基)笨磺酸鈉和乙二醇在醋酸錳 等酯交換觸媒存在下,於14〇〜220 °C間進行酯交換反 應’在合成過程需要加入醋酸鋰、醋酸鉀或醋酸鈉等來抑 制二乙二醇之生成。 B、 共聚酯合成 將反應物對苯二甲酸和乙二醇(莫耳比1比丨· 4 )放入(2) Transesterification reaction between sodium 3,5-bis (methoxycarbonyl) benzylsulfonate and ethylene glycol in the presence of transesterification catalysts such as manganese acetate, etc., needs to be carried out between 14 ° C and 220 ° C. Lithium acetate, potassium acetate or sodium acetate are used to inhibit the formation of diethylene glycol. B. Copolyester synthesis Put the reactants terephthalic acid and ethylene glycol (Mole ratio 1 to 4)
$ 8頁 491865 五、發明說明(6)$ 8 pages 491865 V. Description of the invention (6)
反應槽,進行酯化反應合成對苯二甲酸二乙基酯後(反應 溫度240〜2 60 °C ),再加入3, 5-二(間-羥基乙氧基羰 )苯磺酸鈉和三羧酸酐化合物和聚乙二醇,其用量見表 1 ’及加入三氧化二錄/醋酸鋅/黯酸锰/醋酸鈉(3〇〇ppm /20 0ppm/20 0ppm / 20 0ppm ),和三甲基磷酸酯為安定劑, 等内溫上昇至24 0 °C後,開始抽真空,其抽真空速率以真 空度每隔10分鐘往下調10 cmHg,直至真空度達76 cmHg (76 cmHg為高真空度,〇 cmHg為1大氣壓)時,使接著用 馬力較大之馬達抽高真空,此時反應槽内溫約在2 7 0 °C附 維持此條件,直至攪拌扭力上昇至與合成聚對苯二甲酸二 乙酯之反應溫度( 280〜290 °c )下,攪拌扭力上昇至某 一定值後(在本合成反應中扭力上昇格數為4格)後,在 合成共聚酯在此攪拌應力上,其熔融粘度是相同下,使用 氣氣破真空,加壓下料,所得樣品分析有酸相對粘度和非 酸相對粘度,如表1。 *有酸相對粘度(AR V )測試方法。 以六氟異丙醇(hexafluoroisopropanol)中加入1〇〇 ppm之9 8 %減藥級濃硫酸為溶劑,把上述合成之共聚g旨溶 於六氟異丙醇(含PPM》農硫酸),在25 °c溶解且其濃 度為4.75 wt%溶液,於25 t下,使用canned型粘度管 測得樣品溶液流過粘度管時間為t ,純六氟異丙醇流過粘 度管時間為,則有酸相對粘度為t/ %,指共聚酯之部份In the reaction tank, after the esterification reaction to synthesize diethyl terephthalate (reaction temperature 240 ~ 2 60 ° C), add 3, 5-bis (m-hydroxyethoxycarbonyl) benzenesulfonate and three The amount of carboxylic anhydride compound and polyethylene glycol is shown in Table 1 ', and added with trioxide / zinc acetate / manganese / manganese acetate / sodium acetate (300ppm / 20ppm / 20ppm / 20ppm), and trimethylamine Phosphate is a stabilizer. After the internal temperature rises to 24 0 ° C, vacuum is started. The vacuum rate is adjusted down by 10 cmHg every 10 minutes at a vacuum degree until the vacuum reaches 76 cmHg (76 cmHg is high vacuum) (0cmHg is 1 atmosphere), then use a high-powered motor to draw a high vacuum. At this time, the temperature in the reaction tank is maintained at about 270 ° C. This condition is maintained until the stirring torque rises to that of the synthetic polyparaphenylene. At the reaction temperature of diethyl diformate (280 ~ 290 ° c), after the stirring torque rises to a certain value (in this synthesis reaction, the torque rise number is 4 divisions), the synthetic copolyester is stirred at this stress. The melt viscosity is the same, the gas is broken under vacuum, and the material is discharged under pressure. The obtained sample is analyzed for an acid phase. The viscosity and non-acid relative viscosity, as shown in Table 1. * With acid relative viscosity (AR V) test method. Using hexafluoroisopropanol as a solvent, adding 98 ppm of 98% reduced-grade concentrated sulfuric acid as a solvent, and dissolving the synthesized copolymerized polymer g in hexafluoroisopropanol (containing PPM) agricultural sulfuric acid). The solution is dissolved at 25 ° C and its concentration is 4.75 wt%. At 25 t, the time for the sample solution to flow through the viscosity tube is measured using a canned viscosity tube. The time for pure hexafluoroisopropanol to flow through the viscosity tube is Relative acid viscosity is t /%, refers to the part of copolyester
491865 五、發明說明(7) 交聯(crosslink)被濃硫酸分解後,測得相對枯度。 *非酸相對粘度(NR V )測試方法 把上述合成共聚酯溶於六氟異丙醇中,(2 5七下溶 解)’其濃度為4· 75 wt% ’於2 5 t:下,使用Cann〇n—!型 枯度管測得樣品溶液流過粘度管時間為ti,純六氟異丙醇 流過枯度管時間為tG ’則非酸相對點度為^ / ,指共 聚S旨只在六鼠異丙醇中溶解後(有部份交聯存在下),測 得相對粘度。 △ RV = NRV-ARV =非酸相對粘度~有酸相對黏度,相當描 述共聚酯之部份交聯。 表1 ·合成共聚酯之組成,有酸相對粘度(AR V ),非 酸相對粘度(NRV)和ARV (=NRV-ARV)之關係491865 V. Description of the invention (7) After the crosslink is decomposed by concentrated sulfuric acid, the relative dryness is measured. * Non-acid relative viscosity (NR V) test method The above synthetic copolyester is dissolved in hexafluoroisopropanol and (dissolved at 25 ° C) 'its concentration is 4.75 wt%' at 25 ° C: The time for the sample solution to flow through the viscosity tube was measured using a Cannon-! Type dehumidity tube, and the time for pure hexafluoroisopropanol to flow through the dehumidity tube was tG '. The purpose is to measure the relative viscosity only after dissolving in hexamethylene isopropanol (in the presence of some cross-linking). △ RV = NRV-ARV = non-acid relative viscosity ~ with acid relative viscosity, which quite describes the partial crosslinking of copolyester. Table 1 · Composition of synthetic copolyester, the relationship between acid relative viscosity (AR V), non-acid relative viscosity (NRV) and ARV (= NRV-ARV)
編號 組成(成分比* ) NRV ARV ARV 〇1 TPA/SIPE/PEG/TMAC100/2/1/300) 11.5 9.6 1·9 〇2 TPA/SIPE/PEG/BTCA(100/2/1/400) 12.4 9. 5 2.9 〇3 TPA/SIPE/PEG/TMA 12·2 10·1 2·1 (100/2.5/1.5/300) 〇4 TPA/SI PE/PEG/PTCA( 1 0 0/2/1 /360) 13 1 0.8 2.2 〇5 TPA(IOO) 11·5 - -Number composition (composition ratio *) NRV ARV ARV 〇1 TPA / SIPE / PEG / TMAC100 / 2/1/300) 11.5 9.6 1 · 9 〇 TPA / SIPE / PEG / BTCA (100/2/1/400) 12.4 9. 5 2.9 〇3 TPA / SIPE / PEG / TMA 12.2 10 · 1 2 · 1 (100 / 2.5 / 1.5 / 300) 〇4 TPA / SI PE / PEG / PTCA (1 0 0/2/1 / 360) 13 1 0.8 2.2 〇5 TPA (IOO) 11.5--
第10頁 ^1865 、發明說明(8) 註:(1 ) TPA為對苯二甲酸。 ^ (2)SiPE為3, 5-二(間-羥基乙氧基碳基)磺酸鈉用 量以莫耳%為主,以對苯二甲酸用量為100莫耳% )。 (3) PEG為聚乙醚分子量為60()(以對苯二甲酸重 為100% ;用量以重量% )。 (4) TMA為1,2,4-苯三酸酐,其用董以ppm為單位, 以相對於對苯二甲酸重量為主。 (5 )BTCA為1,2, 4 -三羧酸苯,其用量以ppm為單位, 以相對於對苯二甲酸重量為主。 (6) PTCA為1,2, 3 -三羧酸丙烷,其用量以ppm為單 位,以相對於對笨二甲酸重量為主。 實施例2 乾燥後之實施例編號〇1,〇3和05,於285〜29 0 °C下 紡絲’其紡嘴有7 2個紡口,每個紡口直徑〇 · 3mm,其捲取 速率為1,370 m/min (其中編號05之捲取速率為2, 400 m/min ),在85 °C 的滾輪(R〇i 1 er )延伸3 倍(PET 2· 4 倍 );150 °C的電熱板上做定型捲縮(Crimp),其單束絲 為150丹尼/72根,冷卻風為19 °C。 將上述紡絲後之絲和棉花絲併絲後(5〇/5〇 ),測其 起毛球的量:^ 1865, Description of the invention (8) Note: (1) TPA is terephthalic acid. ^ (2) The amount of SiPE used is 3,5-bis (m-hydroxyethoxycarbon) sodium sulfonate mainly in mole%, and the amount of terephthalic acid is 100 mole%). (3) PEG is polyether with a molecular weight of 60 () (100% by weight of terephthalic acid; weight% by weight). (4) TMA is 1,2,4-trimellitic anhydride, and its unit is ppm, which is mainly relative to the weight of terephthalic acid. (5) BTCA is 1,2,4-tricarboxylic acid benzene, the amount of which is used as a unit of ppm, and it is mainly relative to the weight of terephthalic acid. (6) PTCA is 1,2,3-tricarboxylic acid propane, and its amount is expressed in ppm, which is mainly relative to the weight of p-dicarboxylic acid. Example 2 Example Nos. 〇1, 〇3, and 05 after spinning were spun at 285 ~ 2900 ° C. The spinning nozzle had 72 spinning orifices, each spinning orifice was 0.3mm in diameter, and was wound up. The speed is 1,370 m / min (the winding speed of No. 05 is 2,400 m / min), and the roller (Roi 1 er) at 85 ° C is extended 3 times (PET 2 · 4 times); 150 Crimp is applied to the heating plate at ° C. The single bundle of filament is 150 denier / 72, and the cooling air is 19 ° C. After the spun silk and cotton silk were combined (50/50), the amount of fluff balls was measured:
491865 五、發明說明(9) 氺測單束絲強度和伸度是採用J IS-L-1 017號方法測 試。 氺測起毛球量是依據ASTM D 3512號方法測試。 表2、紡絲後測得物性 編號1 斷裂點強度 斷裂點伸度 01 3.8克/丹尼 25%491865 V. Description of the invention (9) The single strand strength and elongation are measured by J IS-L-1 017 method. The amount of fluff is measured according to ASTM D 3512. Table 2.Physical properties measured after spinning No. 1 Breaking point strength Breaking point elongation 01 3.8 g / Denny 25%
03 3· 5克/丹尼 23 % 05 4. 0克/丹尼 30 % *為實施例1所合成之共聚酯編號 表3、與棉絲混紡後,測得起毛球量03 3.5 grams / denier 23% 05 4.0 grams / denier 30% * is the number of the copolyester synthesized in Example 1 Table 3. After blending with cotton yarn, the amount of wool balls was measured
編號氺 測量時間 起毛球量 01 60分 1. 4 03 60分 1 . 5 05 30分 1. 3No. 氺 Measurement time Pilling volume 01 60 minutes 1. 4 03 60 minutes 1. 5 05 30 minutes 1. 3
第12頁 1 為實施例1合成之共聚酯編號紡絲與棉混紡。Page 12 1 is the copolyester number spinning and cotton blending synthesized in Example 1.
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