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TW201002907A - Method for producing dyed fabric structure - Google Patents

Method for producing dyed fabric structure Download PDF

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Publication number
TW201002907A
TW201002907A TW97149824A TW97149824A TW201002907A TW 201002907 A TW201002907 A TW 201002907A TW 97149824 A TW97149824 A TW 97149824A TW 97149824 A TW97149824 A TW 97149824A TW 201002907 A TW201002907 A TW 201002907A
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TW
Taiwan
Prior art keywords
fiber
fiber structure
polylactic acid
poly
acid
Prior art date
Application number
TW97149824A
Other languages
Chinese (zh)
Inventor
Ryo Yasumitsu
Hirokazu Hayashi
Manabu Toyao
Midori Ikegame
Original Assignee
Teijin Ltd
Teijin Fibers Ltd
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Publication date
Application filed by Teijin Ltd, Teijin Fibers Ltd filed Critical Teijin Ltd
Publication of TW201002907A publication Critical patent/TW201002907A/en

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Classifications

    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/58Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products
    • D01F6/62Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyesters
    • D01F6/625Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyesters derived from hydroxy-carboxylic acids, e.g. lactones
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F1/00General methods for the manufacture of artificial filaments or the like
    • D01F1/02Addition of substances to the spinning solution or to the melt
    • D01F1/10Other agents for modifying properties
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06PDYEING OR PRINTING TEXTILES; DYEING LEATHER, FURS OR SOLID MACROMOLECULAR SUBSTANCES IN ANY FORM
    • D06P3/00Special processes of dyeing or printing textiles, or dyeing leather, furs, or solid macromolecular substances in any form, classified according to the material treated
    • D06P3/34Material containing ester groups
    • D06P3/52Polyesters

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  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Biological Depolymerization Polymers (AREA)
  • Coloring (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Chemical Or Physical Treatment Of Fibers (AREA)
  • Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
  • Woven Fabrics (AREA)

Abstract

Disclosed is a method for producing a dyed fabric structure which has not only biodegradability but also excellent wear resistance and soft texture. Also disclosed are a fabric structure and an automobile interior material. Specifically, a fabric structure which contains polylactic acid fibers having a melting point as measured by DSC of not less than 195 DEG C is dyed, and then, if necessary, formed into an automobile interior material.

Description

201002907 九、發明說明 【發明所屬之技術領域】 本發明係關於經染色之纖維構造體之製造方法,更詳 言之,係關於含有聚乳酸纖維之纖維構造體之經染色之纖 維構造體之製造方法。 【先前技術】 聚乳酸纖維由於具有所謂生物分解性優異之特徵,因 此多方面的用作汽車內裝材、家居用品、衣料等(參照專 利文獻1、專利文獻2、專利文獻3 )。 然而,由於聚乳酸纖維之熔點比聚對苯二甲酸乙二醇 酯等芳香族聚酯低,因此將含有聚乳酸纖維之纖維構造體 染色時,由於熱色時之熱經歷使聚乳酸纖維之絲強度降低 ,而產生耐磨耗性降低之問題。因此,在要求耐磨耗性之 領域中幾乎無法使用聚乳酸纖維。 另外,本申請人在特願2007- 1 44736號中提出含有高 熔點之聚乳酸纖維之過濾器。 (專利文獻1)特開2002-41 5 1號公報 (專利文獻2 )特許第3 73 1 432號公報 (專利文獻3)特開2003 - 1 05 629號公報 【發明內容】 本發明之目的係提供一種具有柔軟質感’且耐磨耗性 及洗滌堅牢度優異之經染色纖維構造體。 -5- 201002907 本發明人針對聚乳酸之製造方法積極檢討,結果發現 ,對含有聚乳酸纖維之纖維構造體染色時,採用高熔點之 聚乳酸纖維作爲聚乳酸纖維時,可獲得具有柔軟質感,且 耐磨耗性及洗滌堅牢度優異之經染色纖維構造體,而完成 本發明。 因此,依據本發明’係提供一種經染色之纖維構造體 之製造方法,其特徵爲將包含熔點爲195 °C以上之聚乳酸 纖維之纖維構造體染色。 此時,聚乳酸纖維較好含有(i)重量平均分子量5萬 至30萬之聚L -乳酸(A成分)、(ii)重量平均分子量5萬 至30萬之聚D-乳酸(B成分)及(iii)每a成分與B成分之 合計100重量份’含有0.〇5〜5重量份之以下述式(i)或( 2)表示之磷酸酯金屬鹽:201002907 IX. OBJECT OF THE INVENTION [Technical Field] The present invention relates to a method for producing a dyed fiber structure, and more particularly to the manufacture of a dyed fiber structure of a fiber structure containing polylactic acid fibers method. [Prior Art] The polylactic acid fiber is excellent in so-called biodegradability, and is therefore used in various aspects such as automobile interior materials, household articles, clothing materials, and the like (see Patent Document 1, Patent Document 2, and Patent Document 3). However, since the melting point of the polylactic acid fiber is lower than that of the aromatic polyester such as polyethylene terephthalate, when the fiber structure containing the polylactic acid fiber is dyed, the polylactic acid fiber is caused by the thermal history of the hot color. The wire strength is lowered, resulting in a problem of reduced wear resistance. Therefore, polylactic acid fibers are hardly used in the field where abrasion resistance is required. Further, the present applicant proposed a filter containing a high-melting polylactic acid fiber in Japanese Patent Application No. 2007-1 44736. (Patent Document 1) Japanese Laid-Open Patent Publication No. Hei. No. Hei. No. Hei. No. 2003-105. A dyed fiber structure having a soft texture and excellent abrasion resistance and washing fastness is provided. -5-201002907 The inventors of the present invention have conducted a review on the production method of the polylactic acid, and found that when the polylactic acid fiber having a high melting point is used as the polylactic acid fiber in the dyeing of the fiber structure containing the polylactic acid fiber, a soft texture can be obtained. The present invention has been completed by a dyed fiber structure excellent in abrasion resistance and washing fastness. Therefore, according to the present invention, there is provided a method for producing a dyed fibrous structure, characterized in that a fibrous structure comprising a polylactic acid fiber having a melting point of 195 ° C or higher is dyed. In this case, the polylactic acid fiber preferably contains (i) poly L-lactic acid (component A) having a weight average molecular weight of 50,000 to 300,000, and (ii) poly D-lactic acid (component B) having a weight average molecular weight of 50,000 to 300,000. And (iii) a total of 100 parts by weight of each of the a component and the B component, containing 0.5 to 5 parts by weight of the phosphate metal salt represented by the following formula (i) or (2):

式(1)中,R!表示氫原子或碳數1〜4之烷基,R2、r3各獨 立表不氫原子或碳數1〜12之院基,Μι表示驗金屬原子或鹼 土類金屬原子,p表示1或2, -6 - 201002907In the formula (1), R! represents a hydrogen atom or an alkyl group having 1 to 4 carbon atoms, and R2 and r3 each independently represent a hydrogen atom or a hospital group having a carbon number of 1 to 12, and Μι represents a metal atom or an alkaline earth metal atom. , p means 1 or 2, -6 - 201002907

(2) 式(2)中,R4、R5及r6各獨立表示氫原子或碳數1〜η之 烷基,M2表示鹼金屬原子或鹼土類金屬原子,p表示丨或2 〇 又,聚乳酸纖維較好以聚L-乳酸成分與聚D-乳酸成分 之合計每100重量份,含有0.1〜5重量份之碳醯亞胺化合物 ,且在1 3 0 °C之沸水中處理3 0分鐘後之分子量維持率爲8 5 % 以上。 聚乳酸纖維之單絲纖度較好在0.01〜20dtex之範圍內。 又,聚乳酸纖維之絲強度以2.5 cN/dtex以上較佳。纖維構 造體中亦可含有其他纖維。其他纖維以聚對苯二甲酸乙二 醇酯纖維較佳。纖維構造體以織物或編物較佳。 染色溫度在110〜140 °c之範圍內較佳。經染色處理後 ,較好實施還原洗淨處理。還原洗淨處理較好在pH 8〜2之 還原浴中,於溫度6〇〜98 °C之範圍內進行。染色後,較好 於纖維構造體上賦予矽樹脂、聚乙烯樹脂或聚對苯二甲酸 乙二醇酯樹脂。 本發明係包含以上述製造方法製造之經染色纖維構造 體。纖維構造體中所含之聚乳酸纖維之纖維強度較好在 -7- 201002907 2 · 3 cN/dtex以上。 在溫度7 〇 °C、濕度9 0 %RH之環境下處理一週後’纖維 構造體中所含之聚乳酸纖維之纖維強度較好爲〇·5 cN/dtex 以上。 纖維構造體較好爲基量在30〜l,000g/m2之範圍內之布 帛。纖維構造體較好爲平面磨耗性爲3級以上之布帛。纖 維構造體之亮度指數(L値)較好在80以下。纖維構造體 藉由AATCC IIA法測定之洗滌堅牢度較好在3級以上。 本發明包含選自由使用上述纖維構造體構成之衣料、 衣料資材、汽車內裝材、家居用品、產業資材及小物品類 組成之群組之纖維製品。 【實施方式】 以下詳細說明本發明。 <聚乳酸> 本發明中使用之聚乳酸較好爲由含有聚L-乳酸成分及 聚D -乳酸成分之聚乳酸構成之纖維。尤其,較好爲由結晶 性聚L-乳酸成分、聚D-乳酸成分構成之纖維較佳。較好爲 由光學純度高之聚L-乳酸成分、聚D-乳酸成分之聚乳酸成 分構成之纖維。又更好,可適當的使用熔點在160 t:以上 之結晶性聚L -乳酸成分、聚D -乳酸成分。 本發明中使用之聚L -乳酸成分較好含90〜100莫耳%, 更好95〜100莫耳%之L-乳酸單位,另外爲了實現高熔點較 -8- 201002907 好爲99〜100莫耳%,另外若以立體化度爲優先 95〜99莫耳%2L-乳酸單位構成較佳。至於其他 D-乳酸單位、除乳酸以外之共聚合成分單位。 、乳酸以外之共聚合成分單位爲0〜1 0莫耳%,Μ 耳%,更好爲〇~1莫耳%。 聚D -乳酸成分較好爲90-100莫耳%,更好 耳%之D -乳酸單位,另外爲了實現高熔點較好 耳%,另外若以立體化度爲優先考量則以由9 5〜 D-乳酸單位構成較佳。至於其他單位舉例爲L-除乳酸以外之共聚合成分單位。L-乳酸單位、 共聚合成分單位爲〇〜10莫耳%,較好爲0〜5莫耳 0 ~ 1莫耳%。 共聚合成分單位例示爲源自具有可形成兩 鍵之官能基之二羧酸、多價醇、羥基羧酸、內 以及源自由該等各種構成成分所成之各種聚酯 、各種聚碳酸酯等之單位。 二羧酸舉例爲丁二酸、己二酸、壬二酸、 苯二甲酸、間苯二甲酸等。至於多價醇舉例爲 二醇、丙烷二醇、丁烷二醇、戊烷二醇、己烷 二醇、甘油、山梨糖醇酐、新戊二醇、二乙二 醇、聚乙二醇、聚丙二醇、聚四亞甲基二醇等 醇等,或於雙酚上加成環氧乙烷而成者等芳香 。至於羥基羧酸舉例爲乙醇酸、羥基丁酸、4-等。至於內酯舉例爲乙交酯、ε-己內醋乙交g 考量則以由 單位舉例爲 D-乳酸單位 之好爲〇〜5莫 爲95〜1 〇〇莫 爲99~1 〇〇莫 〃 9 9莫耳%之 乳酸單位、 乳酸以外之 %,更好爲 個以上之酯 酯等之單位 、各種聚醚 癸二酸、對 乙二醇、丙 二醇、辛烷 醇、三乙二 脂肪族多價 族多價醇等 羥基苯甲酸 旨、ε -己內 -9- 201002907 酯、yS-丙內酯、(5-丁內酯、/3-或7-丁內酯、戊內酯、 5 -戊內酯等。 聚L-乳酸成分及聚D-乳酸成分較好重量平均分子量均 爲1 0萬至5 0萬,更好爲1 5萬至3 5萬。另外,相對於聚合物 重量只要其他成分量爲1 〇重量%以下,則摻合其他成分亦 無妨。 聚L-乳酸及聚D-乳酸可以習知方法製造。 例如,可使L-或D-交酯在金屬聚合觸媒存在下加熱開 環聚合製造。另外,可使含有金屬聚合觸媒之低分子量聚 乳酸結晶化後,於減壓或惰性氣體氣流下加熱固相聚合而 製造。再者,可在有機溶劑存在/不存在下,以使乳酸經 脫水聚合之直接聚合法製造。 聚合反應可在過去習知之反應容器中實施,例如可單 獨或者並列使用具備螺旋帶翼等之高黏度用攪拌翼之縱型 反應器或橫型反應器。另外,可爲批式或連續式或半批式 之任一種,亦可爲該等之組合。 亦可使用醇作爲聚合起始劑。該等醇以不會阻礙聚乳 酸聚合之不揮發性者較佳,例如可適當的使用癸醇、十二 烷醇、十四烷醇、十六烷醇、十八烷醇等。 固相聚合法係使用上述開環聚合法或乳酸直接聚合法 獲得之較低分子量乳酸聚酯作爲預聚物。預聚物爲在未達 其玻璃轉移溫度(Tg )以上之熔點(Tm )之溫度範圍內 會預結晶化,但就防止熔著方面而言可爲較佳形態。將結 晶化之預聚物充塡於固定之縱型或橫型反應器,或者滾筒 -10- 201002907 或窯爐狀之容器本身可旋轉之反應容器(旋轉窯 ,且加熱至預聚物之玻璃轉移溫度(Tg )以上、 (Tm )之溫度範圍。聚合溫度即使伴隨著聚合之 段性升溫亦不會有任何問題。另外,爲了有效去 合中產生之水而亦可較佳地倂用將上述反應容器 減壓或使經加熱之惰性氣體氣流流通之方法。 聚乳酸聚合時使用之金屬觸媒較好最後以過 失活劑與以惰性化。該等失活劑舉例爲例如由具 且配位於聚合金屬觸媒上獲得之螯合配位子之群 有機配位體。又二氫噁喹磷(I )酸、二氫四噁 II,II )酸、氫三噁喹磷(III )酸、二氫五噁喹二 酸、氫五噁喹二磷(Π,ιν )酸、十二噁喹六磷 、氫八噁喹三磷(ΙΠ,ΐν,ΐν )酸、八噁喹三磷( )酸、氫六噁喹二磷(III,V)酸、六噁喹二磷( 十噁唾四磷(IV )酸、十一噁喹四磷(IV )酸 喹三磷(V,IV,IV)酸等酸價數5以下之低氧化數 外列舉爲以式χΗ20· yP2〇5表示之x/y = 3之原磷酸 爲2>x/y>l,由縮合度而稱爲二磷酸、三磷酸、 五磷酸等之聚磷酸以及該等之混合物。又舉例尤 表示之偏磷酸,尤其是三偏磷酸、四偏磷酸。又 l>x/y>0表示之五氧化磷構造之一部分具有籠型 之超磷酸(該等統稱爲偏磷酸系化合物)。又可 等酸之酸性鹽。又可舉例爲該等酸與一價、多價 聚伸烷二醇類之部分酯、完全酯。又例示有該等 爐等)中 未達熔點 進行而階 除固相聚 類之內部 去習知之 有亞胺基 組組成之 喹二磷( 磷(III ) (III)酸 IV,III,IV IV )酸、 > ENEA噁 磷酸。另 。又舉例 四磷酸、 專以x/y=i 舉例爲以 網目構造 舉例爲該 之醇類或 酸之磷取 -11 - 201002907 代低級脂肪族羧酸衍生物等。 由觸媒失活能觀之,較好爲以式xH20 . yP2〇5表 x/y = 3之原磷酸。又較好爲2>X/y>l,由縮合度而稱爲 酸、三磷酸、四磷酸、五磷酸等之聚磷酸以及該等之 物。又較好爲以x/y=l表示之偏磷酸,尤其是三偏磷 四偏憐酸。較好爲以l>x/y>〇表示之五氧化磷構造之 分具有籠型網目構造之超磷酸(該等統稱爲偏磷酸系 物)。又較好爲該等酸之酸性鹽。又較好爲該等酸與 、多價之醇類或聚伸烷二醇類之部分酯。又較好爲該 之磷噁喹酸或該等之酸性酯類等。又較好爲該等酸之 代低級脂肪族羧酸衍生物等。又較好使用上述偏磷酸 合物。 本發明中使用之偏磷酸系化合物包含3〜200左右 酸單位縮合而成之環狀偏磷酸或具有立體網目構造之 域偏磷酸或該等之(鹼金屬鹽、鹼土類金屬鹽、鑰鹽: 尤其較好使用環狀偏磷酸鈉或超領域之偏磷酸鈉 取代之低級脂肪族羧酸衍生物之二己基磷乙基乙酸鹽 下簡稱爲DHPA)等。 本發明中使用之聚乳酸之乳交酯含量係選擇在〇 ppm之範圍。又較好在0~500ppm,更好在〇〜200ppm, 在0~ 10Oppm之範圍內選擇。藉由使聚乳酸具有該範圍 乳交酯含量,可提高熔融時之安定性,可獲得具有效 好並安定地紡絲之優點及提高纖維製品之耐水解性。 交酯含量降低於該範圍,可藉由在由聚L-乳酸及聚D- 示之 二磷 混合 酸、 一部 化合 一價 等酸 磷取 系化 之磷 超領 ► ° 、磷 (以 -700 最好 內之 率良 使乳 乳酸 -12- 201002907 之聚合時點至聚乳酸製造結束爲止之任意階段中,實施過 去習知之乳交酯減輕處理或組合該等而達成。 本發明中使用之聚乳酸之重量平均分子量較好爲1〇萬 〜50萬,更好爲10萬〜30萬,又更好爲10.5萬〜25萬。 以聚乳酸之重量平均分子量(Mw)與數平均分子量 (Μη )之比作爲分子量分散(Mw/Mn )。所謂分子量分 散大,意指相較於平均分子量,大的分子與小的分子之比 例多。亦即,分子量分散大的聚乳酸,例如重量平均分子 量爲25萬左右下,分子量分散超過3之聚乳酸會有其重量 平均分子量値大於2 5萬之分子比例較大之情況,該情況下 ,由於熔融黏度變大,因而在紡絲、延伸步驟方面較不佳 。又於10萬左右之較小重量平均分子量之分子量分散大之 聚乳酸會有其重量平均分子量値小於1 〇萬之分子比例大之 情況,該情況下,纖維之機械物性之耐久性變小,於使用 上較不佳。就該觀點而言分子量分散範圍較好爲1 .5〜3.0, 更好爲1 .5~2.5,又更好爲1.6〜2.5之範圍。 重量平均分子量、數平均分子量係藉由使用氯仿作爲 溶離液之凝膠滲透層析法(GPC )測定換算成標準聚苯乙 烯之重量平均分子量、數平均分子量之値。 聚乳酸中之聚L-乳酸成分與聚D-乳酸成分之重量比爲 90:10〜10:90之範圍。較好爲7 5:2 5〜25:7 5之範圍,更好爲 60:40〜40:60之範圍,且盡可能接近50:50較佳。 聚乳酸較好含有由聚L-乳酸成分及聚D-乳酸成分組成 之立體錯合聚乳酸。立體錯合聚乳酸之含有率,亦即立體 -13- 201002907 化度係在示差掃描熱量計(DSC)測定中’於升溫過程溶 解峰値中,對應於立體錯合結晶之溶解峰値之比例’以下 述式(a)表示較好爲80〜100%,更好爲95~100°/。。 本發明中所謂熔點爲以D S C測定之結晶熔解峰値溫度 ,在存在有低溫結晶熔解峰値溫度與立體錯合結晶熔解峰 値溫度之情況下使用後者。聚乳酸之熔點爲195°c以上’ 較好爲195〜2 5 0 °C,更好爲200〜240 °C極爲重要。立體錯合 結晶熔解焓較好爲20J/g以上,更好爲30J/g以上。 立體化度= [(AHms/AHmsO)/(AHmh/AHmsO + AHms/ AHmsO)]x 1 00 (a) (其中,AHms0 = 203.4J/g,AHmhO=142J/g,AHms =立體錯 合物熔點之熔解焓,ΔΗηι1ι =均結晶之熔解焓)。 聚乳酸可藉由聚L -乳酸成分單獨,或者使聚L -乳酸成 分與聚D-乳酸成分以特定重量比共存混合而製造。 混合可在溶劑存在下進行。溶劑只要是可溶解聚L —乳 酸與聚D -乳酸者,則無特別限制,但較好爲例如氯仿、二 氯甲烷、二氯乙烷、四氯乙烷、苯酚 '四氫呋喃、N_甲基 耻略卩定酮、N,N-二甲基甲醯胺、丁內酯、三噁烷、六氟異 丙醇等之單獨或混合兩種以上者。 又混合可在無溶劑存在下進行。亦即可採用以特定量 混合聚L-乳酸與聚D_乳酸後熔融混練之方法,使任—者熔 融後加入剩下一者並混煉之方法。 -14- 201002907 或者,可結合聚L-乳酸片段與聚D-乳酸片段,亦可適 當的使用立體嵌段聚乳酸作爲聚乳酸。立體嵌段聚乳酸爲 聚L-乳酸片段與聚D-乳酸片段於分子內結合而成之嵌段聚 合物。 如此般之嵌段聚合物可預先使用例如藉由逐次開環聚 合而製造之方法;使聚L-乳酸與聚D-乳酸聚合接著結合鏈 交換反應或鏈延長劑之方法;使聚L-乳酸與聚D-乳酸聚合 並摻合後,經固相聚合之鏈延長方法;使用立體選擇開環 聚合觸媒自外消旋乳交酯製造之方法等製造具有上述基本 構成之嵌段共聚物之方法。 然而,藉由逐次開環聚合獲得之高熔點之立體嵌段聚 合物由於使用以固相聚合法獲得之聚合物時製造容易故而 較佳。 本發明中使用之聚乳酸及立體嵌段聚乳酸,其立體化 度較好爲90%以上,更好爲100%。立體化度可藉由比較 D S C測定之熔點之焓,以上述式(a )加以決定。 本發明中使用之聚乳酸較好爲添加特定添加物以安定 且高度進行立體錯合物相之形成較佳。例如,可舉例爲例 如下述式(1 )、( 2 )中所示之磷酸金屬鹽爲較佳例: -15- 201002907(2) In the formula (2), R4, R5 and r6 each independently represent a hydrogen atom or an alkyl group having a carbon number of 1 to η, M2 represents an alkali metal atom or an alkaline earth metal atom, and p represents ruthenium or ruthenium, polylactic acid. The fiber preferably contains 0.1 to 5 parts by weight of the carbonium imine compound per 100 parts by weight of the total of the L-lactic acid component and the poly-D-lactic acid component, and is treated in boiling water at 130 ° C for 30 minutes. The molecular weight retention rate is 85 % or more. The monofilament fineness of the polylactic acid fiber is preferably in the range of 0.01 to 20 dtex. Further, the filament strength of the polylactic acid fiber is preferably 2.5 cN/dtex or more. Other fibers may also be included in the fibrous structure. Other fibers are preferably polyethylene terephthalate fibers. The fibrous structure is preferably woven or knitted. The dyeing temperature is preferably in the range of 110 to 140 °C. After the dyeing treatment, the reduction washing treatment is preferably carried out. The reduction washing treatment is preferably carried out in a reduction bath having a pH of from 8 to 2 at a temperature of from 6 Torr to 98 °C. After dyeing, it is preferred to impart an enamel resin, a polyethylene resin or a polyethylene terephthalate resin to the fiber structure. The present invention encompasses a dyed fiber structure produced by the above production method. The fiber strength of the polylactic acid fiber contained in the fiber structure is preferably from -7 to 201002907 2 · 3 cN/dtex or more. The fiber strength of the polylactic acid fiber contained in the fiber structure after one week of treatment in an environment of a temperature of 7 C ° C and a humidity of 90% RH is preferably 〇·5 cN/dtex or more. The fibrous structure is preferably a fabric having a basis weight of from 30 to 1,000 g/m2. The fiber structure is preferably a fabric having a planar wear resistance of 3 or more. The brightness index (L値) of the fiber structure is preferably 80 or less. Fiber structure The washing fastness measured by the AATCC IIA method is preferably at least grade 3. The present invention comprises a fiber product selected from the group consisting of a clothing material, a clothing material, an automobile interior material, a household product, an industrial material, and a small article composed of the above-mentioned fiber structure. [Embodiment] Hereinafter, the present invention will be described in detail. <Polylactic acid> The polylactic acid used in the present invention is preferably a fiber composed of polylactic acid containing a poly-L-lactic acid component and a poly-D-lactic acid component. In particular, a fiber composed of a crystalline poly-L-lactic acid component or a poly-D-lactic acid component is preferred. It is preferably a fiber composed of a poly-L-lactic acid component having a high optical purity and a polylactic acid component of a poly-D-lactic acid component. Further, a crystalline poly L-lactic acid component having a melting point of 160 t: or more or a poly D-lactic acid component can be suitably used. The poly L-lactic acid component used in the present invention preferably contains 90 to 100 mol%, more preferably 95 to 100 mol% of the L-lactic acid unit, and is preferably 99 to 100 m in order to achieve a high melting point. The % of the ear is preferably composed of a 95% to 99 mol% 2 L-lactic acid unit with a degree of stereochemistry. As for other D-lactic acid units, units of copolymerization other than lactic acid. The unit of the copolymerization component other than lactic acid is 0 to 1 mol%, Μ%, more preferably 〇1 mol%. The poly-D-lactic acid component is preferably 90-100 mol%, more preferably the ear D-lactic acid unit, and in order to achieve a high melting point, the ear% is additionally obtained, and if the stereoscopic degree is taken as a priority, the The D-lactic acid unit is preferably constituted. As for other units, an example of a copolymerization component other than L-lactic acid is used. The unit of the L-lactic acid unit and the copolymerization component is 〇 10 10 mol%, preferably 0 to 5 mol 0 to 1 mol %. The unit of the copolymerization component is exemplified by a dicarboxylic acid having a functional group capable of forming a double bond, a polyvalent alcohol, a hydroxycarboxylic acid, various polyesters, various polycarbonates, and the like which are formed by the various constituent components. Unit. Examples of the dicarboxylic acid are succinic acid, adipic acid, sebacic acid, phthalic acid, isophthalic acid and the like. The polyvalent alcohol is exemplified by a diol, a propane diol, a butane diol, a pentane diol, a hexane diol, glycerin, sorbitan, neopentyl glycol, diethylene glycol, polyethylene glycol, An aromatic substance such as an alcohol such as polypropylene glycol or polytetramethylene glycol or an addition of ethylene oxide to bisphenol. As the hydroxycarboxylic acid, for example, glycolic acid, hydroxybutyric acid, 4-, etc. As for the lactone, for example, glycolide, ε-hexine vinegar, and g, the amount of the unit is D-lactic acid, and the unit is 〇~5, which is 95~1, 〇〇莫为99~1 〇〇莫〃 9 9 mole % of lactic acid unit, % other than lactic acid, more preferably more than one ester ester unit, various polyether azelaic acid, ethylene glycol, propylene glycol, octane alcohol, triethylene di-aliphatic Valence of polyvalent alcohols such as hydroxybenzoic acid, ε-hexene-9- 201002907 ester, yS-propiolactone, (5-butyrolactone, /3- or 7-butyrolactone, valerolactone, 5 - Valerolactone, etc. The poly-L-lactic acid component and the poly-D-lactic acid component preferably have a weight average molecular weight of from 1,000,000 to 50,000, more preferably from 15,000 to 350,000. In addition, as long as the weight of the polymer is When the amount of other components is 1% by weight or less, it is also possible to blend other components. Poly L-lactic acid and poly-D-lactic acid can be produced by a known method. For example, L- or D-lactide can be present in a metal polymerization catalyst. It is produced by heating under a ring-opening polymerization. Further, after the low molecular weight polylactic acid containing a metal polymerization catalyst is crystallized, the solid phase is heated under a reduced pressure or an inert gas stream. Further, it can be produced by polymerization, and can be produced by direct polymerization of lactic acid by dehydration polymerization in the presence/absence of an organic solvent. The polymerization can be carried out in a conventional reaction vessel, for example, a spiral belt can be used alone or in parallel. A vertical reactor or a horizontal reactor with a high-viscosity stirring wing, etc. Alternatively, it may be either batch or continuous or semi-batch, or a combination thereof. Alcohol may also be used as the polymerization. The initiator is preferably one which does not inhibit the polymerization of the polylactic acid. For example, decyl alcohol, dodecanol, tetradecanol, cetyl alcohol, stearyl alcohol, etc. may be suitably used. The solid phase polymerization method uses a lower molecular weight lactic acid polyester obtained by the above ring-opening polymerization method or direct lactic acid polymerization method as a prepolymer. The prepolymer is a melting point (Tm) which is less than the glass transition temperature (Tg) thereof. It will be pre-crystallized in the temperature range, but it can be better in terms of preventing melting. The crystallized prepolymer is charged to a fixed vertical or horizontal reactor, or a drum-10-201002907 or Kiln-shaped container The rotatable reaction vessel (rotary kiln and heated to a temperature range of the glass transition temperature (Tg) of the prepolymer or more, (Tm). The polymerization temperature does not cause any problem even if the temperature is raised with the polymerization. In order to effectively remove the water generated in the combination, a method of decompressing the above reaction vessel or circulating a heated inert gas stream may be preferably employed. The metal catalyst used in the polymerization of the polylactic acid is preferably a final deactivator. Insulating. The deactivating agents are exemplified by, for example, a group of organic ligands derived from a chelating ligand obtained on a polymeric metal catalyst. Dihydroquinoxaline (I) acid, dihydrogen Tetracalyx II, II) acid, hydrogen trioxoquine (III) acid, dihydropentaquinic acid, hydrogen pentaquine diphosphonate (Π, ιν) acid, tauquinine hexaphosphate, hydrogen octacidine Triphosphorus (ΙΠ, ΐν, ΐν) acid, octosaquivalent triphosphoric acid, hydrogen hexahydroquine diphosphorus (III, V) acid, hexahydroquine diphosphorus (decapine tetraphosphoric acid) The low oxidation number of acid number valence of 5 or less such as quinoxaphosphoric acid tetrakis(VI) acid (V, IV, IV) acid is exemplified by the formula χΗ20· yP2〇5 The orthophosphoric acid represented by x/y = 3 is 2 > x / y > 1, a polyphosphoric acid called diphosphoric acid, triphosphoric acid, pentaphosphoric acid or the like and a mixture thereof. Further examples include metaphosphoric acid, especially trimoephosphoric acid and tetrametaphosphoric acid. Further, a part of the phosphorus pentoxide structure represented by l>x/y>0 has a cage-type superphosphoric acid (collectively referred to as a metaphosphoric acid compound). Also wait for the acidic acid salt. Further, a partial ester or a complete ester of the acid and the monovalent or polyvalent polyalkylene glycol can be exemplified. Further, in the furnaces and the like, the quinodiphosphine (phosphorus (III) (III) acid IV, III, IV IV composed of an imine group is not known as the internal melting point of the solid phase clustering. ) Acid, > ENEA Phosphoric Acid. Another. Further, an example of tetraphosphoric acid, which is specifically represented by x/y = i, is a molecular structure of the alcohol or an acid of the phosphorus -11 - 201002907 generation of a lower aliphatic carboxylic acid derivative. It is better to be deactivated by the catalyst, preferably by the formula xH20. yP2〇5, x/y = 3 orthophosphoric acid. Further, it is preferably 2>X/y>l, which is called polyphosphoric acid such as acid, triphosphate, tetraphosphoric acid or pentaphosphoric acid, and the like by the degree of condensation. Further, it is preferably a metaphosphoric acid represented by x/y = 1, especially a trimetaphosphorus. Preferably, the phosphorus pentoxide structure represented by l>x/y> 具有 has a cage-mesh structure of superphosphoric acid (these are collectively referred to as metaphosphoric acid compounds). Further preferred are acidic salts of such acids. Further preferred are partial esters of such acids with polyvalent alcohols or polyalkylene glycols. Further, it is preferably such a phosphorus oxaquine acid or such an acidic ester. Further, it is preferably a lower aliphatic carboxylic acid derivative or the like. It is also preferred to use the above metaphosphate. The metaphosphoric acid-based compound used in the present invention comprises a cyclic metaphosphoric acid obtained by condensing an acid unit of about 3 to 200 or a domain metaphosphoric acid having a three-dimensional network structure or the like (alkali metal salt, alkaline earth metal salt, key salt: In particular, it is preferred to use a cyclic aliphatic sodium hydride or a super-aliphatic carboxylic acid derivative substituted with a sodium metaphosphate in the super field to be referred to as DHPA). The lactide content of the polylactic acid used in the present invention is selected in the range of 〇 ppm. It is preferably in the range of 0 to 500 ppm, more preferably in the range of 0 to 10 ppm, and in the range of 0 to 10 ppm. By making the polylactic acid have the lactide content in the range, the stability at the time of melting can be improved, and the advantage of being effective and stable spinning can be obtained and the hydrolysis resistance of the fiber product can be improved. The content of the lactide is lowered in this range, and can be obtained by the phosphorous super-collar of the acid-phosphorus, such as poly-L-lactic acid and poly-D-diphosphide mixed acid, a monovalent monovalent acid, etc. In the optimum stage of the polymerization of the lactolactic acid -12-201002907 to the end of the production of the polylactic acid, it is achieved by performing the conventional lactide mitigation treatment or combining the above. The polylactic acid used in the present invention. The weight average molecular weight is preferably from 100,000 to 500,000, more preferably from 100,000 to 300,000, and even more preferably from 105,000 to 250,000. The weight average molecular weight (Mw) and the number average molecular weight (Μη) of the polylactic acid. The ratio is referred to as molecular weight dispersion (Mw/Mn). The large molecular weight dispersion means that the ratio of large molecules to small molecules is larger than the average molecular weight, that is, polylactic acid having a large molecular weight dispersion, for example, a weight average molecular weight is Under the condition of about 250,000, the polylactic acid having a molecular weight dispersion of more than 3 has a large molecular weight ratio of 2 more than 250,000, and in this case, since the melt viscosity becomes large, the spinning and elongation steps are involved. Poor. The polylactic acid having a small weight average molecular weight and a large molecular weight dispersion of about 100,000 has a weight average molecular weight of less than 1 million. In this case, the mechanical properties of the fiber are durable. It is smaller and less preferable to use. From this point of view, the molecular weight dispersion range is preferably from 1.5 to 3.0, more preferably from 1.5 to 2.5, still more preferably from 1.6 to 2.5. The number average molecular weight is measured by gel permeation chromatography (GPC) using chloroform as a solution to determine the weight average molecular weight and number average molecular weight of the standard polystyrene. Poly L-lactic acid component and poly in polylactic acid The weight ratio of the D-lactic acid component is in the range of 90:10 to 10:90, preferably in the range of 7 5:2 5 to 25:7 5 , more preferably in the range of 60:40 to 40:60, and as much as possible It is preferably close to 50:50. Polylactic acid preferably contains a sterically miscible polylactic acid composed of a poly-L-lactic acid component and a poly-D-lactic acid component. The content of the sterically misaligned polylactic acid, that is, the stereo-13-201002907 degree It is dissolved in the temperature rising process in the differential scanning calorimeter (DSC) measurement In the crucible, the ratio of the dissolution peak 对应 corresponding to the steric miscible crystal is preferably from 80 to 100%, more preferably from 95 to 100°, in the following formula (a). The melting point in the present invention is determined by DSC. The crystal melting peak temperature is used in the presence of a low temperature crystal melting peak temperature and a steric misaligned crystal melting peak temperature. The melting point of the polylactic acid is 195 ° C or more ' preferably 195 to 2 50 ° C, more preferably 200 to 240 ° C is extremely important. The steric miscible crystal melting enthalpy is preferably 20 J/g or more, more preferably 30 J/g or more. Stereotacticity = [(AHms/AHmsO)/(AHmh/AHmsO + AHms/ AHmsO)]x 1 00 (a) (where AHms0 = 203.4J/g, AHmhO=142J/g, AHms = steric complex melting point Melting 焓, ΔΗηι1ι = melting of crystallization). The polylactic acid can be produced by mixing the poly L-lactic acid component alone or by coexisting and mixing the poly L-lactic acid component and the poly D-lactic acid component in a specific weight ratio. Mixing can be carried out in the presence of a solvent. The solvent is not particularly limited as long as it can dissolve poly-L-lactic acid and poly-D-lactic acid, but is preferably, for example, chloroform, dichloromethane, dichloroethane, tetrachloroethane, phenol 'tetrahydrofuran, N-methyl group. A single or a mixture of two or more of succinyl ketone, N,N-dimethylformamide, butyrolactone, trioxane, and hexafluoroisopropanol. Further mixing can be carried out in the absence of a solvent. Alternatively, a method of mixing and mixing poly-L-lactic acid and poly-D-lactic acid in a specific amount may be employed, and any one of them may be melted and added to the other and kneaded. -14- 201002907 Alternatively, a poly-L-lactic acid fragment and a poly-D-lactic acid fragment may be combined, and a stereoblock polylactic acid may be suitably used as the polylactic acid. The stereoblock polylactic acid is a block polymer in which a poly-L-lactic acid fragment and a poly-D-lactic acid fragment are combined in a molecule. Such a block polymer may be previously used, for example, by a method of successive ring-opening polymerization; a method of polymerizing poly-L-lactic acid and poly-D-lactic acid followed by a chain exchange reaction or a chain extender; and making poly-L-lactic acid A method of polymerizing and blending poly-D-lactic acid, a chain extension method by solid phase polymerization, a method of producing a block copolymer having the above basic constitution by a method of stereoselective ring-opening polymerization catalyst production from racemic lactide . However, a high-melting-point solid block polymer obtained by sequential ring-opening polymerization is preferred because it is easy to manufacture when a polymer obtained by a solid phase polymerization method is used. The polylactic acid and the stereoblock polylactic acid used in the present invention preferably have a stereochemistry of 90% or more, more preferably 100%. The degree of stereochemistry can be determined by the above formula (a) by comparing the melting point of the D S C measurement. The polylactic acid used in the present invention is preferably formed by adding a specific additive to stabilize and highly forming a stereo compound phase. For example, a metal phosphate salt represented by the following formulas (1) and (2) is exemplified as a preferred example: -15- 201002907

式(1)中,R,表示氫原子或碳數1〜4之烷基〔 示之碳數1〜4之烷基例示爲甲基、乙基、正丙基、 、正丁基、第二丁基、異丁基等。 R_2、R3各獨丛表不氨原子或碳數1〜12之院_ 1〜12之烷基舉例爲甲基、乙基、正丙基、異丙基’ 、第二丁基、異丁基、第三丁基、戊基、第三戊i 、庚基、辛基、異辛基、第三辛基、2-乙基己基、 異壬基、癸基、異癸基、第三癸基、十一烷基、一 、第三-十二烷基等。 M,表示Na、K、Li等鹼金屬原子或Mg、Ca等鹵 屬原子。P表示1或2。 以式(1)表示之磷酸酯金屬鹽中較佳者舉傾 Ri爲氫原子,R2、R3均爲第三丁基者。 以1表 異丙基 。碳數 正丁基 、己基 壬基、 一院基 土類金 爲例如 -16- 201002907In the formula (1), R represents a hydrogen atom or an alkyl group having 1 to 4 carbon atoms (the alkyl group having 1 to 4 carbon atoms is exemplified as methyl group, ethyl group, n-propyl group, n-butyl group, second group). Butyl, isobutyl and the like. R_2, R3, each of which is a single atomic group or a carbon number of 1 to 12, and the alkyl group of 1 to 12 is exemplified by methyl, ethyl, n-propyl, isopropyl', second butyl, isobutyl. , tert-butyl, pentyl, third pentylene, heptyl, octyl, isooctyl, trioctyl, 2-ethylhexyl, isodecyl, fluorenyl, isodecyl, third fluorenyl , undecyl, mono-, tert-dodecyl and the like. M represents an alkali metal atom such as Na, K or Li or a halogen atom such as Mg or Ca. P represents 1 or 2. The phosphate metal salt represented by the formula (1) preferably has a hydrogen atom and R2 and R3 are all a third group. Take 1 isopropyl group. Carbon number n-butyl group, hexyl fluorenyl group, one yard base soil type gold for example -16- 201002907

(2) 式(2 )中,R4、R5、R6各獨立表示氫原子 1~12之烷基。碳數1〜12之烷基舉例爲甲基、乙基、 、異丙基、正丁基、第二丁基、異丁基、第三丁基 、第三戊基、己基、庚基、辛基、異辛基、第三寺 乙基己基、壬基、異壬基、癸基、異癸基、第三癸 一烷基、十二烷基、第三·十二烷基等。 M2表示Na、K、Li等鹼金屬原子或Mg、Ca等鹼 屬原子。P表示1或2。 以式(2)表示之磷酸酯金屬鹽中較佳者舉例 R4、R6爲甲基,R5爲第三丁基者。磷酸酯金屬鹽 ADEKA (股)製之商品名NA-11及NA-71。磷酸酯 可藉習知方法合成。 如特開2003 - 1 928 84號公報中所記載,以式(] 2 )表示之化合物爲已知作爲聚乳酸乏結晶核劑之 。但,本發明中,以式(1)、式(2)中之%及 金屬原子或鹼土類金屬原子爲特徵。式(1)、式 之Μ!及M2爲鋁等其他金屬之情況下,化合物本身 性低,紡絲時會發生昇華物,而有難以紡絲之情況 、碳數 正丙基 、戊基 :基、2- 基、十 土類金 爲例如 舉例爲 金屬鹽 )或( 化合物 M2爲驗 (2)中 之耐熱 -17- 201002907 磷酸酯金屬鹽(C成分)之平均一次粒徑較好爲0.01 〜10#m,更好爲〇·〇5〜7//m。粒徑小於O.Oiym在工業上有 其困難,也沒有必要那麼小。又若大於1 0 μ m,則紡絲、 延伸時斷絲之頻率變高。 磷酸酯金屬鹽之含量對每聚L-乳酸成分與聚D-乳酸成 分之合計1〇〇重量份,較好爲0.05〜5重量份,更好爲 0.05〜0.5重量份’又更好爲0.05〜0.2重量份。太少時,提 升立體化度之效果小,太多時樹脂本身會劣化而不好。 本發明中使用之聚乳酸可適當使用具有特定官能基之 羧基封阻劑作爲耐濕耐熱性改善劑。其中,就可有效封阻 羧基同時促進聚乳酸纖維構造體之色相、立體錯合物相之 形成、耐濕熱性等之觀點而言,較好選擇特定官能基爲碳 二醯亞胺基之碳二醯亞胺化合物。 亦即’碳—釀亞0女化合物例不爲二環己基碳二釀亞胺 、二異丙基碳二醯亞胺、二甲基碳二醯亞胺、二異丁基碳 二醯亞胺、二辛基碳二醯亞胺、辛基癸基碳二醯亞胺、 二-第三丁基碳二醯亞胺、第三丁基異丙基碳二醯亞胺、 二节基碳二醯亞胺、二苯基碳二酿亞胺、N -辛基癸基-N,-苯基碳二醯亞胺、N -节基-Ν’ -苯基碳二酿亞胺、N -节基_ Ν’ -甲苯基碳二醯亞胺、二-鄰-甲苯醯基碳二醯亞胺、二_ k寸-甲本醯基fe —酿亞fee '雙(對-硝基苯基)碳二醯亞胺 、雙(對-胺基苯基)碳二醯亞胺、雙(對-羥基苯基)碳 二醯亞胺、雙(對-氯苯基)碳二醯亞胺、雙(鄰-氯苯基 )碳二醯亞胺、雙(鄰-乙基苯基)碳二醯亞胺、雙(對_ -18- 201002907 乙基苯基)碳二醯亞胺、雙(鄰-異丙基苯基)碳二醯亞 胺、雙(對-異丙基苯基)碳二醯亞胺、雙(鄰-異丁基苯 基)碳二醯亞胺、雙(對-異丁基苯基)碳二醯亞胺、雙 (2,5-二氯苯基)碳二醯亞胺、對-伸苯基雙(鄰-甲苯醯 基碳二醯亞胺)、對-伸苯基雙(環己基碳二醯亞胺)、 對-伸苯基雙(對-氯苯基碳二醯亞胺)、2,6,2’,6’-四異丙 基二苯基碳二醯亞胺、六亞甲基雙(環己基羰二醯亞胺) 、伸乙基雙(苯基碳二醯亞胺)、伸乙基雙(環己基碳二 醯亞胺)、雙(2,6-二甲基苯基)碳二醯亞胺、雙(2,6-二乙基苯基)碳二醯亞胺、雙(2-乙基-6-異丙基苯基)碳 二醯亞胺、雙(2 -丁基-6 -異丙基苯基)碳二醯亞胺、雙( 2,6-二異丙基苯基)碳二醯亞胺、雙(2,6-二-第三丁基苯 基)碳二醯亞胺、雙(2,4,6 -三甲基苯基)碳二醯亞胺、 雙(2,4,6-三異丙基苯基)碳二醯亞胺、雙(2,4,6 -三丁基 苯基)碳二醯亞胺、二- /3-萘碳二醯亞胺、N -甲苯基-Ν’· 環己基碳二醯亞胺、Ν -甲苯基-Ν’ -苯基碳二醯亞胺等之單 或二碳二醯亞胺化合物。 其中就反應性、安定性之觀點而言以以雙(2,6-二異 丙基苯基)碳二醱亞胺、2,6,2’,6’-四異丙基一本基碳一酸 亞胺較佳。又該等中亦較好使用工業上可取得之二環己基 碳二醯亞胺、二異丙基碳二醯亞胺。 另外,舉例爲聚(1 ,6-環己烷碳二醯亞胺)、聚( 4,4,-亞甲基雙環己基碳二醯亞胺)、聚(1,3_伸環己基碳 二醯亞胺)、聚(I,4-伸環己基碳二醯亞胺)、聚(4,4’- -19- 201002907 二苯基甲烷碳二醯亞胺)、聚(3,3’-二甲基-4,4’-二 甲烷碳二醯亞胺)、聚(萘碳二醯亞胺)'聚(對_ 基碳二醯亞胺)、聚(間-伸苯基碳二醯亞胺)、聚 甲苯基碳二醯亞胺)、聚(二異丙基碳二醯亞胺)、 甲基二異丙基伸苯基碳二醯亞胺)、聚(三乙基伸苯 二醯亞胺)等聚碳二醯亞胺等。 至於市售聚碳二醯亞胺化合物可使用例如由曰清 (股)銷售之「CARBOZILITE」,具體而言可例示爲 聚乳酸樹脂改質劑銷售之「CARBOZILITE」LA-1、 作爲聚酯樹脂改質劑銷售之「CARBOZILITE」HMV 等。 碳二醯亞胺化合物可藉由過去習知之方法製造。 可藉由使用有機磷化合物或有機金屬化合物作爲觸媒 7(TC以上之溫度下,無溶劑或在惰性溶劑中使有機異 酯進行脫碳酸縮合反應製造。又聚碳二醯亞胺化合物 由過去已知之聚碳二醯亞胺化合物之製造方法製造, 美國專利第294 1 956號說明書' 特公昭47-33279號公幸1 0 r g. Chem. 28, 2069-2075(1963) ' Chemical Review Vol. 8 1 No. 4,p6 1 9-62 1 等。 碳二醯亞胺化合物之含量以聚L-乳酸成分與聚D_ 成分之合計每100重量份,較好爲0.1〜5重量份,更 0.5〜2重量份。含有該範圍之碳二醯亞胺化合物之立 合聚乳酸纖維在1 〇 〇 °C之沸水中處理3 0分鐘後可獲得 量維持率成爲9 5 %以上之進而較佳纖維。又亦可適當 苯基 仲苯 (對-聚( 基碳 紡績 作爲 或者 -8C A 例如 ,於 氰酸 可藉 例如 臺,J. 1981, -乳酸 好爲 體錯 分子 的選 -20- 201002907 擇過去習知之羧基末端封阻劑。 本發明中之該等羧基反應性之末端封阻劑不僅使聚乳 酸之末端羧基封阻,亦可封阻以聚乳酸或各種添加劑之分 解反應產生之羧基或乳酸、曱酸等低分子化合物之羧基。 又上述封阻劑較好爲不僅封止羧基且亦可封阻藉由熱分解 產生酸性低分子化合物之羥基末端,或者封阻侵入樹脂組 成物中之水分之化合物。 至於羧基末端封阻劑較好使用選自環氧化合物、噁唑 啉化合物、噁唑啶化合物、異氰酸酯化合物之至少一種化 合物,其中以環氧化合物、噁唑啉化合物、異氰酸酯化合 物較佳。 至於環氧化合物可適當地使用縮水甘油醚化合物、縮 水甘油酯化合物、縮水甘油胺化合物、縮水甘油基醯亞胺 化合物、縮水甘油基醯胺化合物、脂環式環氧化合物。 藉由含有末端羧基封阻劑,不僅可提升羧醯胺化合物 之作用,且可獲得紡絲性、力學特性、耐熱性、耐久性優 異之纖維。 聚乳酸中,末端封阻劑及後述之各種添加劑可在開環 聚合法中聚合之任意階段中,且較好爲聚合後期添加於直 接反應容器內混練而調配。考慮聚乳酸中之均勻分散、色 相惡化防止能時,以擠出機或捏合機混練較佳。亦即亦可 使反應器之聚合物排出口連結於單軸或多軸擠出機上而添 加。又例示爲將各種劑類添加於聚合後之經顆粒化聚乳酸 或固相聚合後之聚乳酸粉體中,且以擠出機或捏合機混練 -21 - 201002907 之方法。 此時各種添加劑亦可以熔融液體、水溶液或有機溶劑 溶液或分散液直接計量添加於擠出機或捏合機中,或者以 側饋入器緩慢添加於聚乳酸中。又以擠出機或捏合機以顆 粒或微粉狀之主批次與聚乳酸混練亦爲較佳之實施樣態。 <聚乳酸纖維> 聚乳酸纖維可依據慣用方法藉由將上述聚乳酸紡絲、 延伸而獲得。此時,延伸可爲一段或兩段以上之多段延伸 ,且就製造高強度纖維之觀點而言,延伸倍率較好爲3倍 以上,更好爲4倍以上,又更好爲4〜10倍。延伸預熱除了 輥之升溫以外,亦可爲平板狀或針狀之接觸式加熱。延伸 溫度較好爲7〇〜140°C,更好爲80〜130°c。又,延伸後之熱 處理係在張力下,較好爲170〜200 °C,更好在180〜2 00 °C下 進行。熱處理可以加熱輥、接觸式加熱器、非接觸式加熱 板等進行。 由如此般獲得之聚乳酸構成之纖維以示差掃描熱量計 (DSC)測定,熔解峰値溫度(熔點)爲1 9 5 t以上極爲 重要。當熔點低於1 95 °C時,染色時由於熱經歷使纖維之 絲強度降低,由於會收縮變硬而不佳。另外,該熔點雖愈 高愈好,但240°C以下即足夠。 又,聚乳酸纖維之絲強度較好爲2.5 cN/dt ex以上,較 好爲3.0 cN/dtex左右。上限愈高愈好,但實際上爲10 cN/dtex左右。另外,以纖維構造體之質感觀點觀之,聚乳 -22- 201002907 酸纖維之單絲纖度較好爲0.01〜20dtex ’更好爲0.1〜7dtex 。總纖度爲30〜500dtex,纖維數爲20〜200根之範圍內較佳 <纖維構造體> 纖維構造體可藉由製編織上述之聚乳酸纖維獲得。此 時,亦可對該纖維施以撚絲或空氣加工、假撚捲縮加工等 。尤其,對該纖維施加100〜600T/m左右之撚絲不僅可提升 纖維構造體之耐磨耗性,亦可使製編織纖維構造體時之操 作性獲得提升故而較佳。 又,較好僅使用聚乳酸纖維製編織纖維構造體,但其 中含有其他纖維亦無妨。其他纖維之含量相對於纖維構造 體重量,以5.0重量%以下較佳。至於其他纖維舉例爲聚對 苯二甲酸乙二醇酯纖維等。 又,纖維構造體之構造並無特別限制,但較好爲藉由 一般織機或編機製編織而成之織物或編物。無論如何,較 好爲由不織布或基質纖維與熱接著性纖維構成之纖維構造 體。例如,織物之織組織例示爲平織、斜織、锻織等之三 原組織,變化組織、經雙重織、緯雙重織等平紋二重組織 、經編絲滅等。編物種類可爲圓編物(緯編物)亦可爲經 編物。圓編物(緯編物)之組織,較好例示爲平紋針織、 羅紋針織、兩面編織、雙反面編織、掛針編織、浮線編織 、半睦編織、紗維編織、添毛編織等’作爲經編組織,例 示有單梳櫛經平編織、單梳櫛經緞針織、雙梳橘經滅、經 -23- 201002907 平編織、起絨經編'提花編織等。層數可怎 層以上之多層。再者,亦可爲由割絨(cut 圈絨(1 ο 〇 p p i 1 e )所構成之立毛部及底組織 毛纖維構造體。 <染色> 染色前,亦可在溫度50〜100 °C於弱鹼性 度80〜100 °C於鹼條件下進行減量加工。又, 染色後較好於溫度140〜180°C進行乾熱處理。 纖維構造體可以下列方法進行染色。染 染料進行染色處理。作爲染料,雖較好例示 良好的偶氮系分散染料,但並未特別限定於 爲於後述洗淨處理液中溶液分解的分散染料 二酯基之分散染料、偶氮系分散染料,其中 、噻吩型。再者,亦可舉例有蒽酮系分散染 喃酮型分散染料、具有烷胺基之分散染料等 染色溫度較好爲110〜140°c,更好於120 進行。染色時間較好爲20〜40分鐘。 於纖維構造體中含有聚對苯二甲酸乙二 芳香族聚酯纖維作爲其他纖維時,較好於除 又含均染劑、pH調整劑等之染料水溶液中, 以上,更好120〜135 °C以上之溫度,進行20〜 〇 經染色處理之纖維構造體較好施以還原 ^單層亦可爲2 pile )及/或毛 部所構成之立 下精練或於溫 染色前及/或 色宜使用分散 爲洗滌堅牢度 此。尤其,作 ,例示有具有 較好爲噻唑型 料、苯并二呋 〇 〜1 3 5 °C之溫度 醇酯纖維等之 分散染料以外 較好於1 2 0 °C 40分鐘之染色 洗淨處理。此 -24- 201002907 時,較好於pH8〜2之還原浴中進行還原洗淨處理。於大於 p Η 8之鹼性區域,有聚乳酸纖維會分解,使纖維強度降低 之情況。 作爲還原劑’舉例有錫系還原劑、雕白粉C、雕白粉Ζ 、氣化錫、亞磺酸系還原劑、氫硫酸鹽等。還原劑之使用 濃度較好爲1〜10克/升,宜依據使用染料種類、染色濃度 、還原浴溫度選定濃度。還原浴之處理溫度並無特別限制 ’但較好爲60〜98 °C之範圍,處理時間較好爲10〜40分鐘。 因此’還原洗淨處理,較好於PH8〜2之還原浴中,於溫度 60〜98°C的範圍進行。 再者,於還原浴中處理之際,作爲纖維膨潤劑,亦可 使用一般使用之導染劑(carrier ),例如氯苯系導染劑、 甲基萘系導染劑、鄰苯基酚系導染劑、芳香族醚系導染劑 、芳香族酯系導染劑等。該等纖維膨潤劑可舉例有認爲對 纖維具有親和性之聚氧乙烯烷基芳基醚、聚氧乙烯烷基胺 、聚氧乙烯烷基酚醚、聚氧乙烯烷基醚、聚氧乙烯烷基胺 醚、聚氧乙烯氯化烷基苄基銨、氯化烷基甲基吡啶鑰等, 但不限定於此。 還原洗淨處理若在pH8以下之弱鹼性至酸性區域處理 ,則還原洗淨處理之際,聚乳酸纖維不會水解,而可還原 分解剩餘纖維表層部之染料。 又’染色後’較好於纖維構造體上賦予矽樹脂、聚乙 烯樹脂或聚對苯二甲酸乙二醇酯樹脂。樹脂可藉由軋染髮 等賦予至纖維構造體上。若於纖維構造體上賦予樹脂可提 -25- 201002907 高纖維構造體之耐磨耗性而較佳。此時’樹脂之附著量對 於纖維構造體重量較好爲0.5〜5.0重量%之範圍。 再者,染色步驟之前及/或之後,亦可附加使用吸水 加工、撥水加工、起毛加工、難燃劑、紫外線遮蔽或抗靜 電劑、抗菌劑、消臭劑、防蟲劑、蓄光劑、逆反射劑、負 離子發生劑等賦予機能之各種加工。 <纖維構造體特性> 本發明包含以上述方法獲得之纖維構造體。所得之纖 維構造體中,纖維構造體中所含之聚乳酸纖維之絲強度較 好爲2.3 cN/dtex以上。尤其,較好爲可保持染色前之聚乳 酸纖維之絲強度之9 0 %以上。 又,此纖維構造體之基量較好在30〜l,0 00g/m2之範圍 內。 又’纖維構造體爲織物時,由纖維構造體之耐磨耗性 及質感方面而言,由下式算出之覆蓋因子(CF)爲500〜 4,000 ° CF = (DWp/l.i)1/2xMWp + (DWf/1.1) 1/2xMWf 其中’ D W p爲經絲總纖度(d t e χ ) ,m W p爲經絲織密度( 根/2.54cm ) ’ DWf爲緯絲總纖度(dtex ) ,MWf爲緯絲織 密度(根 /2.54cm)。 χ ’ 1¾ I隹構造體爲編物時,由纖維構造體之耐磨耗性 -26- 201002907 及質感方面而言,較好爲30~100橫列針數(course) /2.54 cm、20〜60縱列針數(wale) /2.54cm之密度。 此種纖維構造體,由於使用含有藉由DSC測定之熔點 如1 95 °C以上之高熔點聚乳酸纖維之纖維構造體加以染色 者,故由於不會因染色之際之熱經歷使纖維構造體中所含 之纖維過度損傷,因此呈現優異之耐磨耗性。作爲此耐磨 耗性,較好爲依據JIS L 1 096.8.1 7.3 C法測定之平面磨耗性 爲3級以上。又,亦不會於染色之際因熱經歷使纖維構造 體收縮而變硬,因此亦不會損及柔軟質感。當然亦具有生 物分解性。 經染色之纖維構造體,爲染色堅牢度優異且於濕熱環 境下之纖維強度降低亦小之纖維構造體。經染色之纖維構 造體於溫度7〇°C、濕度90%RH之環境下處理1週後,纖維 構造體中所含之聚乳酸纖維之纖維強度較好爲0.5 cN/dtex 以上,更好爲3〜10gr/dtex。 本發明中,強度係使用ORI ΕΝ TEC公司製造之「 TENSIRON」(商品名),自測定對象之纖維構造體隨意 拔取10根對象單絲(纖絲),於絲試料長度50mm (夾具 間長度)、伸長速度500mm/分鐘之條件,於環境溫度20°C 、相對濕度6 5 %條件下測定歪斜-應力曲線,由破裂點時之 應力及伸長度求得強度(cN/根)後,以該強度除以纖度 作爲纖維強度(cN/dtex )。 又,於70°Cx90%RH處理1週,係使用tabAI ESPEC( 股)製之恆溫恆濕器LHU-11 2M,將試料放置於作成該設 -27- 201002907 定之機器內之環境中1週實施處理。 又,經染色之纖維構造體之亮度指數(L値)較好爲 8 0以下。 又經染色之纖維構造體之依據AATCC ΠΑ法測定之洗 滌堅牢度爲3級以上較佳。 又,本發明之經染色纖維構造體,亦可附加使用一般 方法之撥水加工、起毛加工、紫外線遮蔽或抗菌劑、消臭 劑、防蟲劑、蓄光劑、逆反射劑、負離子產生劑等賦予機 能之各種加工。 <纖維製品> 本發明之經染色纖維構造體可使用於各種纖維製品。 作爲纖維製品,舉例有衣料、衣料資材、汽車內裝材、家 居用品、產業資材、小物品類。 作爲衣料,舉例有襯衫、夾克、短褲、大衣等。衣料 資材舉例爲包縫料、襯墊等。汽車內裝材舉例有座椅表皮 材、地板材、天花板材等。居家用品舉例爲窗簾、地毯、 席墊、豕具等。產業資材舉例爲皮帶、網、繩纜、重布、 袋類、毛耗、過據器等。小物品舉例爲服飾用品、形態吊 帶、眼鏡擦拭、食器擦拭、齒墊、塡充玩具、玩具襯裡、 帽子、手袋、白板清潔布、筆記本表紙等。 該等纖維製品因使用本發明之經染色纖維構造體,故 不僅具有生物分解性,且亦呈現優異之耐磨耗性及柔軟質 感。 -28- 201002907 實施例 以下詳述本發明之實施例及比較例,但本發明並不受 該等之限制。再者,實施例中之各測定項目係以下述方法 測定。 (1) 重量平均分子量(Mw) 聚合物之重量平均分子量係以GPC (管柱溫度40 °C, 氯仿)’與聚苯乙烯標準樣品比較求得。 (2) 玻璃轉移點、溶點、立體化度 使用TA德儀製之TA-2920示差掃描熱量測定計DSC。 測定係使l〇mg試料在氮氣氛圍氣體下,以1〇 °C /分鐘之升 溫速度自室溫升溫至260 °C。以第一次掃瞄求得均結晶熔 解溫度、玻璃轉移溫度、立體錯合物結晶熔解溫度。立體 化度係以下述式計算出。 S(%) = [(AHms/AHmsO)/(AHmhMHmhO + AHms/AHmsO)] X 1 00 (其中,^110^0 = 203.41/^, AHmhO= 142J/g > △Hms:立體錯 合物熔點之熔解焓,△Hmhi均結晶之熔解焓) (3 )纖維之強伸長度 -29- 201002907 以HS-L-1013爲準,且使用〇IUENTEC公司製造之 TENSIR〇N之定速伸長拉伸試驗機,以夾具間隔爲2〇公分 ,拉伸速度20公分/分鐘測定。 (4 )基量 以 JIS L 1 096. 8_ 5. 1測定基量(g/m2)。 (5 )纖維構造體之耐磨耗性 以JIS L 1 09 6. 8. 1 7_ 3 C法分級判定平面磨耗。5級爲 最高,1級爲最低。 (6)纖維構造體之質感 由3位試驗者進行感官評價’評價爲(3級)柔軟,( 2級)普通’(1級)硬三等級。 (7 )立體化率(Sc化率)(2) In the formula (2), R4, R5 and R6 each independently represent an alkyl group having 1 to 12 hydrogen atoms. The alkyl group having 1 to 12 carbon atoms is exemplified by methyl, ethyl, isopropyl, n-butyl, t-butyl, isobutyl, tert-butyl, tert-pentyl, hexyl, heptyl, octyl Base, isooctyl, third temple ethylhexyl, decyl, isodecyl, fluorenyl, isodecyl, tert-alkyl, dodecyl, tert-dodecyl and the like. M2 represents an alkali metal atom such as Na, K or Li or an alkali atom such as Mg or Ca. P represents 1 or 2. Preferred among the phosphate metal salts represented by the formula (2) are those in which R4 and R6 are a methyl group and R5 is a third butyl group. Phosphate metal salt ADEKA (shares) trade names NA-11 and NA-71. Phosphate esters can be synthesized by conventional methods. The compound represented by the formula (2) is known as a polylactic acid-depleted crystal nucleating agent, as described in JP-A-2003-128884. However, in the present invention, it is characterized by % in the formula (1), the formula (2), and a metal atom or an alkaline earth metal atom. In the case of formula (1), formula Μ! and M2 is other metals such as aluminum, the compound itself is low, sublimation occurs during spinning, and it is difficult to spin, carbon number n-propyl, pentyl: The base, the 2-base, the ten earth-based gold is, for example, a metal salt) or (the compound M2 is the heat-resistant -17-201002907 phosphate metal salt (component C) in the test (2), and the average primary particle diameter is preferably 0.01. ~10#m, more preferably 〇·〇5~7//m. The particle size is less than O.Oiym has difficulty in the industry, and it is not necessary to be so small. If it is larger than 10 μm, it is spun and extended. The frequency of the broken metal wire becomes high. The content of the phosphate metal salt is 1 part by weight, preferably 0.05 to 5 parts by weight, more preferably 0.05 to 0.5, per 1 part by weight of the poly-L-lactic acid component and the poly-D-lactic acid component. The part by weight is more preferably 0.05 to 0.2 part by weight. When the amount is too small, the effect of increasing the degree of stereochemistry is small, and when it is too much, the resin itself may be deteriorated and not good. The polylactic acid used in the present invention may suitably have a specific functional group. The carboxyl blocking agent acts as a moisture and heat resistance improving agent, wherein the carboxyl group is effectively blocked and the polylactic acid fiber is promoted From the viewpoints of the hue of the dimensional structure, the formation of the stereocomplex phase, the heat and humidity resistance, etc., it is preferred to select a carbodiimide compound having a specific functional group of a carbodiimide group. Examples of sub-zero female compounds are dicyclohexylcarbodiimide, diisopropylcarbodiimide, dimethylcarbodiimide, diisobutylcarbodiimide, dioctylcarbamate Yttrium, octyl decyl carbodiimide, di-t-butyl carbodiimide, tert-butyl isopropyl carbodiimide, bis- carbodiimide, diphenyl Carbodicarbonimine, N-octyldecyl-N,-phenylcarbodiimide, N-nodal-fluorene-p-phenylene diimenimine, N-pyringyl Ν -'-toluene Carbon bis quinone imine, di-o-tolyl fluorenyl carbodiimide, bis-k-carbyl hydrazinyl fe-fee 'bis(p-nitrophenyl) carbodiimide, Bis(p-aminophenyl)carbodiimide, bis(p-hydroxyphenyl)carbodiimide, bis(p-chlorophenyl)carbodiimide, bis(o-chlorophenyl) ) carbodiimide, bis(o-ethylphenyl)carbodiimide, double (pair _ -18- 2010029) 07 ethyl phenyl) carbodiimide, bis(o-isopropylphenyl)carbodiimide, bis(p-isopropylphenyl)carbodiimide, bis(o-iso-butyl) Phenyl)carbodiimide, bis(p-isobutylphenyl)carbodiimide, bis(2,5-dichlorophenyl)carbodiimide, p-phenylene O-tolylhydrylcarbodiimide), p-phenylene bis(cyclohexylcarbodiimide), p-phenylene bis(p-chlorophenylcarbodiimide), 2,6 , 2',6'-tetraisopropyldiphenylcarbodiimide, hexamethylenebis(cyclohexylcarbodiimide), ethylidene bis(phenylcarbodiimide), stretch Ethyl bis(cyclohexylcarbodiimide), bis(2,6-dimethylphenyl)carbodiimide, bis(2,6-diethylphenyl)carbodiimide, double (2-ethyl-6-isopropylphenyl)carbodiimide, bis(2-butyl-6-isopropylphenyl)carbodiimide, bis(2,6-diisopropyl) Phenyl)carbodiimide, bis(2,6-di-t-butylphenyl)carbodiimide, bis(2,4,6-trimethylphenyl)carbodiimide , bis(2,4,6-triisopropyl Carbodiimide, bis(2,4,6-tributylphenyl)carbodiimide, di-/3-naphthylcarbodiimide, N-tolyl-oxime'·cyclohexyl A mono- or dicarbodiimide compound such as carbodiimide or fluorenyl-tolyl-fluorene-p-phenylcarbodiimide. Among them, in terms of reactivity and stability, bis(2,6-diisopropylphenyl)carbodiimide, 2,6,2',6'-tetraisopropyl-based carbon Monoacid imide is preferred. Further, industrially available dicyclohexylcarbodiimide and diisopropylcarbodiimide are preferably used. In addition, examples are poly(1,6-cyclohexanecarbodiimide), poly(4,4,-methylenebiscyclohexylcarbodiimide), poly(1,3_cyclohexylenecarbyl)醯imine), poly(I,4-cyclohexylenecarbodiimide), poly(4,4'--19- 201002907 diphenylmethane carbodiimide), poly(3,3'- Dimethyl-4,4'-dimethane carbodiimide), poly(naphthalene carbodiimide) 'poly(p- carbodiimide), poly(m-phenylene carbene) Imine), polytolylcarbodiimide, poly(diisopropylcarbodiimide), methyldiisopropylphenylene carbodiimide, poly(triethylbenzenediamine) Imino), such as polycarbodiimide. As for the commercially available polycarbodiimide compound, for example, "CARBOZILITE" sold by Minqing (share) can be used, and specifically, "CARBOZILITE" LA-1, which is sold as a polylactic acid resin modifier, can be exemplified as the polyester resin. "CARBOZILITE" HMV, etc. for the sale of modifiers. The carbodiimide compound can be produced by a conventional method. It can be produced by using an organic phosphorus compound or an organometallic compound as the catalyst 7 (at a temperature above TC, without solvent or by decarbonation condensation reaction of the organic isomer in an inert solvent. Further, the polycarbodiimide compound is used in the past The production method of the known polycarbodiimide compound is manufactured, and the specification of U.S. Patent No. 2,941,956 is known as 'Tokyo Sho 47-33279. 1 0 r g. Chem. 28, 2069-2075 (1963) ' Chemical Review Vol. 8 1 No. 4, p6 1 9-62 1 , etc. The content of the carbodiimide compound is preferably 0.1 to 5 parts by weight, more preferably 0.5 parts by weight per 100 parts by weight of the total of the poly-L-lactic acid component and the poly-D component. 〜2 parts by weight. The ligated polylactic acid fiber containing the carbodiimide compound in the range is treated with boiling water at 1 ° C for 30 minutes to obtain a fiber having a retention rate of 95% or more. It is also possible to use phenyl phenyl benzene (p-poly (based on carbon spinning as -8C A, for example, in cyanic acid, for example, J. 1981, - lactic acid is good as a choice of 00-201002907) A conventional carboxy terminal blocking agent. The carboxyl group in the present invention The reactive terminal blocking agent not only blocks the carboxyl group at the end of the polylactic acid, but also blocks the carboxyl group generated by the decomposition reaction of polylactic acid or various additives or the carboxyl group of a low molecular compound such as lactic acid or citric acid. It is preferred to block not only the carboxyl group but also the hydroxyl terminal of the acidic low molecular compound by thermal decomposition or to block the moisture invading the resin composition. The carboxyl terminal blocking agent is preferably selected from the ring. At least one compound of an oxygen compound, an oxazoline compound, an oxazolidine compound, and an isocyanate compound is preferably an epoxy compound, an oxazoline compound, or an isocyanate compound. As the epoxy compound, a glycidyl ether compound can be suitably used, and the compound can be used. a glyceride compound, a glycidylamine compound, a glycidyl ruthenium compound, a glycidyl decylamine compound, or an alicyclic epoxy compound. By containing a terminal carboxyl blocking agent, not only the action of the carbamide compound can be enhanced, Further, fibers excellent in spinnability, mechanical properties, heat resistance, and durability can be obtained. In the lactic acid, the terminal blocking agent and various additives described later may be blended in any stage of polymerization in the ring-opening polymerization method, and preferably added to the direct reaction vessel at the later stage of polymerization. Considering uniform dispersion and hue in the polylactic acid. In the case of deterioration prevention, it is preferable to knead with an extruder or a kneader, that is, the polymer discharge port of the reactor may be connected to a single-shaft or multi-axis extruder, and it may be exemplified to add various kinds of agents. After the polymerization, the granulated polylactic acid or the polylactic acid powder after the solid phase polymerization, and the method of mixing - 21 - 201002907 by an extruder or a kneader. At this time, various additives may be directly metered into the extruder or the kneader in a molten liquid, an aqueous solution or an organic solvent solution or dispersion, or may be slowly added to the polylactic acid by a side feeder. It is also preferred to carry out the mixing with the polylactic acid in the main batch of granules or fine powder by an extruder or a kneader. <Polylactic acid fiber> The polylactic acid fiber can be obtained by spinning and stretching the above polylactic acid according to a conventional method. In this case, the extension may be a plurality of extensions of one or more stages, and the stretching ratio is preferably 3 times or more, more preferably 4 times or more, and more preferably 4 to 10 times from the viewpoint of producing high-strength fibers. . The extension preheating may be a flat or needle contact heating in addition to the temperature rise of the rolls. The stretching temperature is preferably from 7 Torr to 140 ° C, more preferably from 80 to 130 ° C. Further, the heat treatment after stretching is preferably from 170 to 200 ° C, more preferably from 180 to 200 ° C under tension. The heat treatment can be carried out by a heating roll, a contact heater, a non-contact heating plate or the like. The fiber composed of the polylactic acid thus obtained is measured by a differential scanning calorimeter (DSC), and it is extremely important that the melting peak temperature (melting point) is 195 5 or more. When the melting point is lower than 1 95 °C, the strength of the fiber is lowered due to thermal history during dyeing, which is not preferable because it shrinks and hardens. Further, the higher the melting point, the better, but 240 ° C or less is sufficient. Further, the filament strength of the polylactic acid fiber is preferably 2.5 cN/dt ex or more, preferably about 3.0 cN/dtex. The higher the upper limit, the better, but it is actually around 10 cN/dtex. Further, from the viewpoint of the texture of the fiber structure, the monofilament fineness of the polylactic acid-22-201002907 acid fiber is preferably from 0.01 to 20 dtex', more preferably from 0.1 to 7 dtex. The total fineness is 30 to 500 dtex, and the number of fibers is preferably in the range of 20 to 200. <Fiber structure> The fiber structure can be obtained by weaving the above polylactic acid fiber. At this time, the fiber may be subjected to twisting or air processing, false twist crimping, or the like. In particular, the application of the twisted yarn of about 100 to 600 T/m to the fiber not only improves the abrasion resistance of the fiber structure, but also improves the workability in the production of the woven fiber structure. Further, it is preferred to use only a woven fiber structure made of polylactic acid fiber, but it may contain other fibers. The content of the other fibers is preferably 5.0% by weight or less based on the weight of the fiber structure. As other fibers, polyethylene terephthalate fibers and the like are exemplified. Further, the structure of the fiber structure is not particularly limited, but is preferably a woven or knitted fabric woven by a general loom or knitting mechanism. In any case, it is preferably a fibrous structure composed of a non-woven fabric or a matrix fiber and a heat-bonding fiber. For example, the weaving structure of the fabric is exemplified by the three original tissues of plain weave, twill weave, and forged weave, and the plain weave, double weave, double weave, etc. The type of knitting can be a circular weft (weft weaving) or a warp. The structure of the circular weave (weft weaving) is preferably woven as a warp knitting, rib knitting, double weaving, double reverse weaving, hanging stitch weaving, floating weaving, semi-twisting weaving, yarn weaving, weaving, etc. It is exemplified by a single comb, a flat weave, a single comb, a satin knit, a double combed orange, a -23-201002907 flat weave, a pile warp, a jacquard weave, and the like. The number of layers can be more than one layer. Further, it may be a bristles and a bottom tissue fiber structure composed of cut velvet (1 ο 〇 ppi 1 e). <Staining> Before dyeing, it may be at a temperature of 50 to 100 °. C is subjected to a reduction treatment under alkali conditions at a weak basicity of 80 to 100 ° C. Further, after dyeing, a dry heat treatment is preferably carried out at a temperature of 140 to 180 ° C. The fiber structure can be dyed by the following methods. Although a good azo-based disperse dye is preferably exemplified as the dye, it is not particularly limited to a disperse dye diester-based disperse dye or an azo-based disperse dye which is decomposed by a solution in a cleaning treatment liquid to be described later. The thiophene type. Further, the dyeing temperature of the fluorenone-dispersed ketone-type disperse dye and the disperse dye having an alkylamine group is preferably 110 to 140 ° C, more preferably 120. The dyeing time is good. When the fiber structure contains polyethylene terephthalate polyester fiber as the other fiber, it is preferably used in an aqueous dye solution containing a leveling agent, a pH adjuster, or the like. Better 120~135 °C or more At the temperature, the fiber structure which is subjected to 20~ 〇 dyeing treatment is preferably subjected to reduction, the single layer may be 2 piles, and/or the bristles are formed by scouring or before the temperature dyeing and/or the color is dispersed. For washing fastness this. In particular, it is exemplified by a dyeing treatment which is preferably a disperse dye having a temperature of a thiazole type material, a benzofuranone to a temperature of 1 to 3 ° C, and a temperature of preferably 120 ° C for 40 minutes. . In the case of -24-201002907, the reduction washing treatment is preferably carried out in a reduction bath of pH 8 to 2. In an alkaline region larger than p Η 8, polylactic acid fibers are decomposed to lower the fiber strength. Examples of the reducing agent include a tin-based reducing agent, a white powder C, a white powder, a vaporized tin, a sulfinic acid-based reducing agent, and a hydrogen sulfate. The concentration of the reducing agent is preferably from 1 to 10 g/liter, and the concentration is preferably selected depending on the type of dye used, the dyeing concentration, and the temperature of the reduction bath. The treatment temperature of the reduction bath is not particularly limited, but is preferably in the range of 60 to 98 ° C, and the treatment time is preferably from 10 to 40 minutes. Therefore, the 'reduction washing treatment is preferably carried out in a reduction bath of pH 8 to 2 at a temperature of 60 to 98 °C. Further, as the fiber swelling agent, a commonly used dyeing agent such as a chlorobenzene-based dyeing agent, a methylnaphthalene-based dyeing agent, or an o-phenylphenol-based system may be used as the fiber swelling agent. A dye-inducing agent, an aromatic ether-based dyeing agent, an aromatic ester-based dyeing agent, and the like. The fiber swells may, for example, be polyoxyethylene alkyl aryl ethers, polyoxyethylene alkylamines, polyoxyethylene alkyl phenol ethers, polyoxyethylene alkyl ethers, polyoxyethylenes which are considered to have affinity for fibers. The alkylamine ether, the polyoxyethylene alkylalkylbenzylammonium chloride, the alkyl chloride methyl chloride key, etc. are not limited thereto. When the reduction washing treatment is carried out in a weakly alkaline to acidic region at a pH of 8 or less, the polylactic acid fiber is not hydrolyzed at the time of the reduction washing treatment, and the dye of the surface portion of the remaining fiber can be reduced and decomposed. Further, it is preferable to impart an enamel resin, a polyethylene resin or a polyethylene terephthalate resin to the fiber structure after the "dyeing". The resin can be imparted to the fiber structure by pad dyeing or the like. It is preferable to impart a resin to the fiber structure to improve the abrasion resistance of the high fiber structure of -25 to 201002907. At this time, the amount of the resin adhered is preferably in the range of 0.5 to 5.0% by weight based on the weight of the fiber structure. Furthermore, before and/or after the dyeing step, water absorption processing, water repellent processing, raising processing, flame retardant, ultraviolet shielding or antistatic agent, antibacterial agent, deodorant, insect repellent, light storage agent, Retroreflectors, negative ion generators, and the like impart various functions to the processing. <Fiber Structure Characteristics> The present invention includes the fiber structure obtained by the above method. In the obtained fiber structure, the fiber density of the polylactic acid fiber contained in the fiber structure is preferably 2.3 cN/dtex or more. In particular, it is preferred to maintain 90% or more of the silk strength of the polylactic acid fiber before dyeing. Further, the basis weight of the fiber structure is preferably in the range of 30 to 1, 000 g/m2. Further, when the fiber structure is a woven fabric, the covering factor (CF) calculated from the following formula is 500 to 4,000 ° CF = (DWp/li) 1/2 x MWp + in terms of abrasion resistance and texture of the fiber structure. (DWf/1.1) 1/2xMWf where 'DW p is the warp total denier (dte χ ), m W p is the warp density (root / 2.54cm ) ' DWf is the weft total denier (dtex ), MWf is the weft Silk weave density (root / 2.54 cm). χ ' 13⁄4 I隹 structure is a fabric, the abrasion resistance of the fiber structure -26- 201002907 and texture, preferably 30 to 100 course number / course / 2.54 cm, 20~60 The number of needles (wale) / 2.54 cm. Such a fiber structure is dyed by using a fiber structure containing a high-melting polylactic acid fiber having a melting point of 1, 95 ° C or higher as measured by DSC, so that the fiber structure is not caused by the heat history at the time of dyeing. The fibers contained in the fibers are excessively damaged and thus exhibit excellent wear resistance. As the abrasion resistance, the planar wear resistance measured according to JIS L 1 096.8.1 7.3 C method is preferably 3 or more. Further, since the fiber structure is not hardened by heat history at the time of dyeing, the soft texture is not impaired. Of course, it is also biodegradable. The dyed fiber structure is a fiber structure which is excellent in dye fastness and has a small decrease in fiber strength in a moist heat environment. After the dyed fiber structure is treated in an environment of a temperature of 7 ° C and a humidity of 90% RH for one week, the fiber strength of the polylactic acid fiber contained in the fiber structure is preferably 0.5 cN/dtex or more, more preferably 3~10gr/dtex. In the present invention, "TENSIRON" (trade name) manufactured by ORI TEC TEC Co., Ltd. is used, and 10 target filaments (filaments) are randomly extracted from the fiber structure of the measurement object, and the length of the wire sample is 50 mm (length between the jigs). After the elongation rate is 500 mm/min, the skew-stress curve is measured under the conditions of an ambient temperature of 20 ° C and a relative humidity of 6 5 %, and the strength (cN/root) is obtained from the stress and the elongation at the time of the fracture. The intensity is divided by the fineness as the fiber strength (cN/dtex). Further, the sample was treated at 70 ° C x 90% RH for one week using a constant temperature and humidity device LHU-11 2M manufactured by tabAI ESPEC (manufacturing), and the sample was placed in an environment of the machine set in the factory set at -27-201002907 for one week. deal with. Further, the dyed fiber structure preferably has a brightness index (L値) of 80 or less. Further, the dyed fibrous structure has a washing fastness of 3 or more, which is preferably determined by the AATCC method. Further, the dyed fiber structure of the present invention may be additionally subjected to water repellent processing, raising processing, ultraviolet shielding or antibacterial agent, deodorant, insect repellent, light storing agent, retroreflective agent, negative ion generating agent, etc., using a general method. Gives a variety of processing to the function. <Fiber product> The dyed fiber structure of the present invention can be used for various fiber products. Examples of the fiber product include clothing materials, clothing materials, automobile interior materials, household goods, industrial materials, and small articles. As the clothing, for example, a shirt, a jacket, a pair of shorts, a coat, and the like are exemplified. Examples of clothing materials are overlock materials, liners, and the like. Examples of automotive interior materials include seat skins, flooring, and ceiling materials. Examples of household items are curtains, carpets, mats, cookware, and the like. Examples of industrial materials are belts, nets, ropes, heavy cloths, bags, hair consumption, and instruments. Examples of small items are clothing items, slings, glasses wiping, food wiping, tooth pads, sling toys, toy linings, hats, handbags, whiteboard cleaning cloths, notebook sheets, and the like. Since these fiber products use the dyed fiber structure of the present invention, they are not only biodegradable, but also exhibit excellent abrasion resistance and soft texture. -28- 201002907 EXAMPLES Examples and comparative examples of the present invention are described in detail below, but the present invention is not limited thereto. Further, each measurement item in the examples was measured by the following method. (1) Weight average molecular weight (Mw) The weight average molecular weight of the polymer was determined by comparison with a polystyrene standard sample by GPC (column temperature 40 ° C, chloroform). (2) Glass transfer point, melting point, and stereoscopic degree The TA-2920 differential scanning calorimeter DSC manufactured by TA Instruments was used. The measurement was carried out by heating the l〇mg sample from room temperature to 260 °C at a temperature of 1 ° C /min under a nitrogen atmosphere. The average crystal melting temperature, the glass transition temperature, and the stereoscopic compound crystal melting temperature were determined by the first scanning. The degree of stereochemistry is calculated by the following formula. S(%) = [(AHms/AHmsO)/(AHmhMHmhO + AHms/AHmsO)] X 1 00 (where ^110^0 = 203.41/^, AHmhO= 142J/g > △Hms: steric complex melting point Melting 焓, △Hmhi crystallization melting 焓) (3) Strong elongation of fiber -29- 201002907 Based on HS-L-1013, and using the constant elongation tensile test of TENSIR〇N manufactured by 〇IUENTEC The machine was measured at a clamp interval of 2 cm and a tensile speed of 20 cm/min. (4) Amount The basis weight (g/m2) was determined by JIS L 1 096. 8_5.1. (5) Abrasion resistance of fiber structure The plane wear was judged by JIS L 1 09 6. 8. 1 7_ 3 C method. Level 5 is the highest and Level 1 is the lowest. (6) Texture of the fiber structure The sensory evaluation was performed by three subjects, and it was evaluated as (grade 3) soft, and (grade 2) ordinary '(level 1) hard three grade. (7) Three-dimensional rate (Sc rate)

使用理化學電器公司製造之ROTA FLEX RU200B型X 射線繞射裝置’以透過法在下列條件下將X射線繞射圖形 記錄在顯像板上。求得所得X射線繞射圖型中之赤道方向 之繞射強度輪廓。依據下式,由其中20=12.0。、20.7。、 24.0。附近出現之源自立體錯合物結晶之各繞射峰之積分強 度總合Σ ISC1及2 0 =16_5。附近出現之源自均結晶之繞射峰 之積分強度Ihm求得立體化率(Sc化率)。又,Σ 1$£;1及 Ihm係如圖1所示,係藉由赤道方向之繞射強度輪廓中背景 -30- 201002907 或非晶之散射散亂之差異估算。 X射線源.Cu-Κα線(共焦鏡) 輸出:45kVx70mA 狹長模嘴:ΙιηηιΦ〜0.8ιηηιφ 照相機長度:120mm 累I十時間:10分鐘 樣品:長3公分,35毫克 Sc化率=Σ Isci/(S Isci + lHM)xl〇〇 其中 Σ Isci = lsci+Isc2 + Isc3 15以(丨=1~3)係分別爲20=12.〇。、2〇.7。、24.〇。附近 之各繞射峰之積分強度 (8 )洗滌堅牢度 以下列之AATCCII-A法測定。The X-ray diffraction pattern was recorded on a developing panel by a transmission method using a ROTA FLEX RU200B type X-ray diffraction device manufactured by Ricoh Electric Co., Ltd. under the following conditions. The diffraction intensity profile in the equatorial direction in the resulting X-ray diffraction pattern is obtained. According to the following formula, 20 = 12.0. 20.7. 24.0. The integral strength sums of the respective diffraction peaks originating from the steric complex crystals appearing near ISC1 and 2 0 = 16_5. The stereoscopic rate (Sc rate) is obtained by the integrated intensity Ihm of the diffraction peak derived from the uniform crystal which appears nearby. Also, Σ 1$£;1 and Ihm are as shown in Fig. 1, estimated by the difference between the background -30-201002907 or the scattered scattering of the diffracted intensity profile in the equator direction. X-ray source. Cu-Κα line (confocal lens) Output: 45kVx70mA Long and narrow nozzle: ΙιηηιΦ~0.8ιηηιφ Camera length: 120mm Tired I ten time: 10 minutes Sample: Length 3 cm, 35 mg Sc rate = Σ Isci/ (S Isci + lHM)xl〇〇 where Isci = lsci+Isc2 + Isc3 15 is (==1~3) is 20=12.〇. 2〇.7. 24. Integral intensity of each of the nearby diffraction peaks (8) Wash fastness was measured by the following AATCC II-A method.

1) 試驗法:AATCC6 1 - 1 980IIA 2) 裝置及材料 1.洗滌試驗機:40〜44rpm 2·試驗瓶(不鏽鋼製):45 0~550毫升 3. 不鏽鋼球:直徑0.4mm,每一瓶中50個 4. 肥皂:固態洗滌皂(JIS K3 3 02)無添加劑(1種^ 5. 偏矽酸鈉(Na2Si03. 5H20) 6. 冰醋酸 7. 電熨斗 8. 離心脫水機或絞乾機 -31 - 201002907 3 )附加白布 AATCC多纖維編號1 緯絲:乙酸酯、棉、尼龍、絲、嫘縈、羊毛 經絲:聚酯(短纖維紗) 4 )試驗片之調製 取出一片縱lkmx橫氕爪之試驗片,使—片5cmx5cm之 附加白布(多纖維編號1 )以與試驗片中央處接觸之方式 以白木棉絲縫合4邊。編物之情況下使用與試驗片相同大 小之密度8 0 (條/ 2 · 5 4 c m ) X 8 0 (條/ 2 _ 5 4 c m )之漂白薄呢( muslin),亦缝合4邊之試驗片以防止端部在試驗中捲入 〇 5 )試驗之操作 於試驗瓶中放入1 5 0毫升之0.2 %肥皂、0.2 %偏矽酸鈉 之溶液,放入50個不鏽鋼硬球。溫度預熱至49。(:後,加入 複合試驗片,安裝在密閉之旋轉機軸上且在溫度49 T:下旋 轉操作45分鐘。接著未冷卻立刻自試驗瓶取出複合試驗片 ’以100毫升溫水(40 °C )洗淨1分鐘兩次後,再以1〇〇毫 升水(27 °C )洗淨1分鐘。隨後,以離心脫水機或絞乾機 脫水,同時取出試驗片及附加白布,且以溫度1 3 5 T:〜1 5 〇 °C之電熨斗壓著乾燥。 6 )判定 多纖維編號1之污染判定,於尼龍部分污染予以灰色 分級係依循:Π S L 0 8 0 1進行。 -32- 201002907 (5 ) L値 染色後針織物之L値係以分光側光器(Gretag MacBeth Color-Eye 7000A)測定布料質感之表面。L値表 示亮度,其數値愈大表示亮度愈高,愈接近100則爲淡色 越接近白色,愈接近0則顯示濃色。 (6)纖維強度(g/dtex) 本發明中之強度係使用ORIENTEC公司製造之「 TENSIRON」 (商品名),自測定對象隨意拉取1〇條對 象單絲(纖絲),在絲試料長50mm (夾具間長度)、伸 長速度500mm/分鐘之條件下於環境氣體溫度20°C、相對濕 度65%之條件下測定歪斜-應力曲線,求得破裂點之應力及 伸張強度(克/條)後,以該強度除以纖度作爲纖維強度 (g/dtex )。另外,各値係使用10次之測定値之平均値。 製造例1 (聚L-乳酸之製造) 相對於1 0 0重量份之L乳交酯(武藏業化學硏究所(股 )製造,光學純度1〇〇°/。)添加0.005重量份之辛酸錫,且 在氮氣氛圍氣體下,置於裝置攪拌翼之反應機中,在180 °C下反應2小時’添加相對於辛酸錫1 · 2倍當量之磷酸後, 於1 3.3 kP a下去除殘留之乳交酯,經顆粒化,獲得聚L -乳 酸。所得之聚L -乳酸之重量平均分子量爲1 5萬,玻璃轉移 點(Tg)爲63°C,熔點爲。 -33- 201002907 製造例2 (聚D-乳酸之製造) 相對於1 〇 〇重量份之D乳交酯(武藏業化學硏究所(股 )製造’光學純度1 〇 0 % )添加0 · 0 0 5重量份之辛酸錫,且 在氮氣氛圍氣體下,置於裝置攪拌翼之反應機中,在180 °C下反應2小時,添加相對於辛酸錫1 .2倍當量之磷酸後, 於1 3 _ 3 kP a下去除殘留之乳交酯,經顆粒化,獲得聚D_乳 酸。所得之聚D-乳酸之重量平均分子量爲15萬,玻璃轉移 點(Tg)爲63°C,溶點爲180°C。 製造例3(立體錯合聚乳酸樹脂之製造) 使製造例1中獲得之聚L -乳酸及製造例2中獲得之聚D -乳酸各50重量份與〇_1重量份之磷酸酯金屬鹽(磷酸2,2 -亞 甲基雙(4,6 -二-第三丁基苯酣)鈉鹽,平均粒徑5ym, ADEKA (股)(原:旭電化工業(股))製造之 ADEKASTAPU N A - 1 1 )於2 3 0 t:下熔融混練,自第—供給 口供給相對於聚L-乳酸及聚D-乳酸之合計100重量份爲〇.7 重量份之作爲碳二醯亞胺之日清紡(股)製造之 CARBOZILITE LA-1,且在圓筒溫度230°C下混練押出,於 水槽中取出線股’且於切粒機中顆粒化,獲得立體錯合聚 乳酸樹脂。所得立體錯合聚乳酸樹脂之Mw爲1 3 · 5萬,熔點 (Tm )爲2 1 7°C,立體化率爲1 00%。 製造例4 (立體錯合聚乳酸樹脂之製造) 使製造例1中獲得之聚L-乳酸及製造例2中獲得之聚D_ -34- 201002907 乳酸各50重量份及〇·5重量份之磷酸酯金屬鹽(AD ΕΚ A ( 股)(原:旭電化工業(股))製造之ADEKASTAPU ΝΑ-ΐ 1 ) 於 230°C 下熔 融混練 ,自第 一 供給口 供給相 對於聚 L-乳酸及聚D-乳酸之合計100重量份爲0.7重量份之作爲碳二 醯亞胺之日清紡(股)製造之CARBOZILITE LA-1,且在 圓筒溫度23 0 °C下混練押出,於水槽中取出線股,且於切 粒機中顆粒化,獲得立體錯合聚乳酸樹脂。所得立體錯合 聚乳酸樹脂之Mw爲13.5萬,熔點(Tm)爲224 °C,立體化 率爲1 0 0 %。 實施例1 使上述製造例3中所得之立體錯合聚乳酸樹脂於11 (TC 下乾燥2小時,在l5〇°C下乾燥5小時,使樹脂之水份率成 爲8 0 p p m時,使用具有3 6孔直徑〇 · 2 7 m m之吐出孔之紡絲模 嘴,在25 5 °C之紡絲溫度下以8.3 5克/分鐘之吐出量紡絲後 ,於500m/分鐘之速度下捲取未延伸絲。使捲取之未延伸 絲在延伸機上預熱80 °C下延伸4.9倍捲取延伸絲後,於180 °C下進行熱處理。紡絲步驟、延伸步驟中之步驟通過性良 好,捲取之延伸絲爲纖度167dTex/36fil之多纖維,強度 3.6 cN/dTex,伸長度 35% ’ 溶點213°C。 將2條所得立體錯合聚乳酸纖維合絲,且進行1 60Τ/ΙΠ 之撚絲後,配置成經絲及緯絲,製織斜紋織物組織之織物 後,使該織物在1 50 °C之溫度下乾熱定型2分鐘後,使用液 流染色機,在溫度120 °C下進行20分鐘染色。此時,使用 -35- 201002907 分散染料。接著,經由含浸絞液機對該纖維構造體賦予相 對於纖維構造體重量爲1 ·5重量%之矽樹脂’在溫度13 0 °c 下乾燥1〇分鐘後在溫度160 下進行乾熱定型2分鐘。 所得織物爲經絲密度4〗條/公分,緯絲密度1 8條/公分 ,覆蓋因子2 6 9 0,平面磨耗性3級,質感3級’且呈現耐磨 耗性及柔軟質感者。 接著,使用該織物縫製車用座椅之表皮材(汽車內裝 材)。該車用座椅表皮材爲呈現耐磨耗性及柔軟質感者。 實施例2 僅使用由實施例1獲得之立體錯合聚乳酸纖維構成之 撚絲絲條(1 6 0 T/m ) ’使用2 0機號圓編織機,製編1段網 目組織之圓編物。 接著,使該編物在150 °C之溫度下乾熱定型2分鐘後, 使用液流染色機’在1 2 0 °C之溫度下進行2 0分鐘染色。此 時使用分散染料。而且,藉由含浸絞液機對該纖維構造體 賦予相對於纖維構造體重量爲1 · 5重量%之矽樹脂,且在溫 度130°C下乾燥10分鐘後’在溫度16〇。(::下施加乾熱定型2 分鐘。 所得織物爲經絲密度3 5橫列針數/ 2 · 5 4公分,緯絲密度 24條/2.54公分,平面磨耗性3級,質感3級,且呈現耐磨耗 性及柔軟質感者。 接著’使用該織物縫製車用座椅之表皮材(汽車內裝 材)。該車用座椅表皮材爲呈現耐磨耗性及柔軟質感者。 -36- 201002907 比較例1 實施例1中,除使用立體錯合聚乳酸取代製造例1獲得 之聚L-乳酸以外’餘與實施例1相同。 聚乳酸纖維之熔點爲1 80 °C。所得織物因染色時之熱 經歷而收縮變硬(質感1級)。又’爲平面磨耗性1級與耐 磨耗性差者。 參考例1 除使用0.5重量份之鋁雙(2,2’_亞甲基雙(4,6 -二-第 三丁基苯基)磷酸酯)氫氧化物(ADEKA (股)(原:旭 電化工業(股))製造之ADEKASTAPU NA-21 )作爲磷酸 酯金屬鹽以外,餘與實施例1般進行操作,紡絲時發生劇 烈昇華物,難以紡絲。 實施例3 使製造例4中所得之立體錯合聚乳酸樹脂於1 1 0 °C下乾 燥2小時,在1 5 〇 °C下乾燥5小時,使樹脂之水份率成爲 80ppm時,使用具有36孔直徑〇.27mm之吐出孔之紡絲模嘴 ,在2 5 5 °C之紡絲溫度下以8.3 5克/分鐘之吐出量紡絲後, 於500m/分鐘之速度捲取未延伸絲。使捲取之未延伸絲在 延伸機上預熱8 0 °C下延伸4 · 9倍捲取延伸絲後,於1 8 0 °C下 進行熱處理。紡絲步驟、延伸步驟中之步驟通過性良好, 捲取之延伸絲爲纖度167dTex/36fil之多纖絲,強度3.6 -37- 201002907 cN/dTex,伸長度35%,經DSC測定具有單一熔解峰,該溶 解峰溫度(熔點)爲224 °C ’立體化率爲100%。 將2條所得立體錯合聚乳酸纖維合絲,實施1 6 0 T/m之 撚絲後,配置成經絲及緯絲’製織斜紋織物組織之織物後 ,使該織物在1 5 0 °C之溫度下乾熱定型2分鐘後’使用液流 染色機,在溫度l2〇°C下進行30分鐘之染色。此時使用以 下分散染料染色,且實施還原洗淨處理。 (分散染料名) C . I. Disperse Blue 79 1 % owf 將所得染色物在下述還原浴中(PH5.5 )洗淨: 浴比;1 : 2 0 溫度X時間;12(TC X30分鐘 還原浴組成及洗淨條件: 二氧化硫尿素lg/L 浴比;1 : 2 0 溫度X時間;70°C xl 5分鐘 接著,在溫度130 °C下乾燥10分鐘後,於溫度160°C下 實施乾燥定型2分鐘。如此般處理後,經染色之纖維構造 体中,L値爲3 8,洗滌堅牢度爲4級,該編織材中所含立體 錯合乳酸纖維在70 °C X 90%RH下處理1週後之纖維強度爲 1 ·8 cN/dtex ( 3 00克/條)。接著,使用該編織材獲得制服 衣料,洗滌堅牢度優異且耐久性亦良好。 -38- 201002907 實施例4 實施例3中,除將磷酸酯金屬鹽之含量變成重量份 以外,餘與實施例3相同。所得之經染色纖維構造體之l値 爲3 8,洗滌堅牢度爲4級,該編織材中所含立體錯合乳酸 纖維在70°C x90%RH下處理1週後之纖維強度爲1.8 cN/dtex (3 00克/條)。接著,使用該編織材獲得制服衣料,洗· 堅牢度優異且耐久性亦良好。 實施例5 實施例3中,除將磷酸酯金屬鹽之含量變成重量份 以外,餘與實施例3相同。所得之經染色纖維構造體之L値 爲3 8,洗滌堅牢度爲4級,該編織材中所含立體錯合乳酸 纖維在70 °C x90%RH下處理1週後之纖維強度爲1.8 cN/dtex (3 00克/條)。接著,使用該編織材獲得制服衣料,洗滌 堅牢度優異且耐久性亦良好。 比較例2 實施例3中,除使用立體錯合聚乳酸取代製造例1獲得 之聚L -乳酸以外,餘與實施例3相同。延伸絲經D S C測定具 有單一熔解峰,該熔解峰溫度(熔點)爲1 8 0 °C。所得織 物在70 °C x9 0%RH下處理1週後之纖維強度爲0.05 cN/dtex (8克/條),難以維持織物之構造。 發明之效果 -39- 201002907 依據本發明,可獲得不僅具有生物分解彳生’ 軟質感、耐磨耗性及洗滌堅牢度均優異之經染色 IMtl 體0 產業上利用之可能性 本發明之經染色纖維構造體可用作衣料、为& , — 狀料資材、 汽車內裝材、家居用品、產業資材等纖維製品之原料。 【圖式簡單說明】 圖1爲用以求得立體化率(Sc化率)之赤道方向之繞 射強度輪廓。 -40-1) Test method: AATCC6 1 - 1 980IIA 2) Apparatus and materials 1. Washing test machine: 40~44rpm 2·Test bottle (made of stainless steel): 45 0~550ml 3. Stainless steel ball: 0.4mm in diameter, each bottle 50 in 4. 4. Soap: solid detergent soap (JIS K3 3 02) without additives (1 kind ^ 5. sodium metasilicate (Na2Si03. 5H20) 6. glacial acetic acid 7. electric iron 8. centrifugal dehydrator or wringer -31 - 201002907 3 )Additional white cloth AATCC multi-fiber No. 1 Weft: acetate, cotton, nylon, silk, crepe, wool warp: polyester (short fiber yarn) 4) Preparation of test piece Take out a vertical lkmx The test piece of the cross-claw was sutured with 4 pieces of white cloth (multi-fiber number 1) of 5 cm x 5 cm in a manner of being in contact with the center of the test piece. In the case of braiding, a density of 80 (bar / 2 · 5 4 cm ) X 8 0 (bar / 2 _ 5 4 cm) of the same size as the test piece was used, and the test piece of 4 sides was also sewn. In order to prevent the end portion from being involved in the test, the test was carried out by placing 150 ml of 0.2% soap and 0.2% sodium metasilicate solution into the test bottle and placing 50 stainless steel hard balls. The temperature is preheated to 49. (: After that, the composite test piece was added, mounted on a closed rotating shaft and rotated for 45 minutes at a temperature of 49 T: Then, the composite test piece was taken out from the test bottle immediately after cooling without cooling to 100 ml of warm water (40 ° C) After washing for 1 minute twice, it was washed with 1 ml of water (27 ° C) for 1 minute. Then, it was dehydrated by a centrifugal dehydrator or a wringer, and the test piece and the additional white cloth were taken out at a temperature of 1 3 . 5 T: ~1 5 〇 °C electric iron pressed dry. 6) Judging the multi-fiber number 1 pollution determination, the gray part of the nylon contamination is followed by: Π SL 0 8 0 1. -32- 201002907 (5) L値 The L値 of the dyed fabric was measured for the texture of the fabric with a spectrophotometer (Gretag MacBeth Color-Eye 7000A). L値 indicates the brightness. The higher the number, the higher the brightness. The closer to 100, the lighter the color is. The closer to 0, the darker the color. (6) Fiber strength (g/dtex) In the strength of the present invention, "TENSIRON" (trade name) manufactured by ORIENTEC Co., Ltd. is used, and one single object filament (filament) is randomly drawn from the object to be measured, and the length of the wire sample is long. The skew-stress curve was measured under the conditions of an ambient gas temperature of 20 ° C and a relative humidity of 65% under conditions of 50 mm (length between clamps) and elongation speed of 500 mm/min, and the stress at the fracture point and the tensile strength (g/bar) were determined. Thereafter, the intensity is divided by the fineness as the fiber strength (g/dtex). In addition, the average enthalpy of the measurement was measured 10 times for each tether. Production Example 1 (Production of Poly L-Lactic Acid) 0.005 parts by weight of tin octylate was added to 100 parts by weight of L-lactide (manufactured by Musashi Chemical Research Institute, optical purity: 1 〇〇 ° /.) And in a reactor under a nitrogen atmosphere, placed in a reactor stirring wing, reacted at 180 ° C for 2 hours. After adding 1. 2 times equivalent of phosphoric acid relative to tin octoate, the residue was removed at 13.3 kP a. Lactide, granulated, to obtain poly-L-lactic acid. The obtained poly L-lactic acid had a weight average molecular weight of 15,000 and a glass transition point (Tg) of 63 ° C and a melting point of . -33- 201002907 Production Example 2 (Manufacturing of Poly D-Lactic Acid) Adding 0 · 0 0 to 1 part by weight of D-lactide (made by Musashi Chemical Research Institute (optical purity 1 〇 0 %) 5 parts by weight of tin octylate, and placed in a reactor equipped with stirring wings under a nitrogen atmosphere, reacted at 180 ° C for 2 hours, added with 1.2 times equivalent of phosphoric acid with tin octoate, at 1 3 _ 3 kP a to remove residual lactide, granulated to obtain poly D_lactic acid. The obtained poly D-lactic acid had a weight average molecular weight of 150,000, a glass transition point (Tg) of 63 ° C, and a melting point of 180 °C. Production Example 3 (Production of a steric miscible polylactic acid resin) 50 parts by weight of each of the poly-L-lactic acid obtained in Production Example 1 and the poly-D-lactic acid obtained in Production Example 2 and 〇_1 parts by weight of a phosphate metal salt (2,2-Methylenebis(4,6-di-tert-butylphenylhydrazine) phosphate, average particle size 5ym, ADEKASTAPU NA manufactured by ADEKA (formerly: Asahi Denki Kogyo Co., Ltd.) - 1 1 ) melt-kneading at 203t: from the first supply port, 100 parts by weight of the total of the poly-L-lactic acid and the poly-D-lactic acid is 〇.7 parts by weight as the carbodiimide CARBOZILITE LA-1 manufactured by Nisshinbo Co., Ltd., and kneaded at a cylinder temperature of 230 ° C, and the strands were taken out in a water tank and pelletized in a pelletizer to obtain a stereo-aligned polylactic acid resin. The obtained stereo-aligned polylactic acid resin had a Mw of 135,000, a melting point (Tm) of 2 17 ° C, and a stereochemistry of 100%. Production Example 4 (Production of steric miscible polylactic acid resin) The poly L-lactic acid obtained in Production Example 1 and the poly D_-34-201002907 lactic acid obtained in Production Example 2 were each 50 parts by weight and 5% by weight of phosphoric acid. The ester metal salt (ADEKASTAPU ΝΑ-ΐ 1 ) manufactured by AD ΕΚ A (share) (formerly: Asahi Denki Kogyo Co., Ltd.) is melt-kneaded at 230 ° C, and is supplied from the first supply port with respect to poly-L-lactic acid and poly 100 parts by weight of D-lactic acid is 0.7 parts by weight of CARBOZILITE LA-1 manufactured by Nisshinbo Co., Ltd. as a carbon diimide, and is kneaded at a cylinder temperature of 23 0 ° C, and the strands are taken out in a water tank. And granulated in a pelletizer to obtain a stereo-aligned polylactic acid resin. The obtained stereo-aligned polylactic acid resin had a Mw of 135,000, a melting point (Tm) of 224 ° C, and a stereoscopic ratio of 100%. Example 1 The sterically miscible polylactic acid resin obtained in the above Production Example 3 was dried at 11 (TC for 2 hours, dried at 15 ° C for 5 hours, and the water content of the resin was 80 ppm). 3 Spinning nozzle of 6 hole diameter 〇· 2 7 mm discharge hole, after spinning at a spinning temperature of 25 5 °C at a spinning rate of 8.3 5 g/min, coiling at a speed of 500 m/min The wire is not stretched. The unstretched wire taken up is extended by 490 times on the stretcher at 80 ° C, and the stretched wire is taken up, and then heat-treated at 180 ° C. The steps in the spinning step and the stretching step are good. The stretched wire is a multi-fiber with a fineness of 167dTex/36fil, the strength is 3.6 cN/dTex, the elongation is 35%, and the melting point is 213 ° C. The two obtained stereoscopically misaligned polylactic acid fibers are combined and subjected to 1 60 Τ/ After 捻 捻 , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , Dyeing was carried out for 20 minutes at C. At this time, the dye was dispersed using -35-201002907. Then, via the impregnation winch The fiber structure was subjected to drying at a temperature of 130 ° C for 1 minute and then dried at a temperature of 160 ° C for 2 minutes. The resulting fabric was warp. Density 4 * strip / cm, weft density 1 8 / cm, coverage factor 2 6 9 0, flat wear level 3, texture level 3 'and wear resistance and soft texture. Next, use the fabric sewing The surface material of the vehicle seat (automobile interior material). The vehicle seat surface material is a wear-resistant and soft texture. Embodiment 2 Only the stereo-aligned polylactic acid fiber obtained in Example 1 is used.捻 丝 ( (1 60 T/m ) 'Use a 20 knitting machine to make a circular braid of 1 mesh mesh. Then, let the braid dry and heat for 2 minutes at 150 °C. Thereafter, the liquid dyeing machine was used to perform dyeing at a temperature of 120 ° C for 20 minutes. At this time, a disperse dye was used. Moreover, the fiber structure was given a weight relative to the fiber structure by an impregnation winch machine. 1 · 5 wt% of bismuth resin, and dried at a temperature of 130 ° C for 10 minutes After 'at a temperature of 16 〇. (:: apply dry heat setting for 2 minutes. The resulting fabric is a warp density of 3 5 rows of needles / 2 · 5 4 cm, weft density of 24 / 2.54 cm, plane wearability 3 Grade, texture level 3, and exhibits wear resistance and soft texture. Then 'Use this fabric to sew the skin material of the car seat (automobile interior material). The car seat skin material shows wear resistance. -36-201002907 Comparative Example 1 In Example 1, except that the poly-L-lactic acid obtained in Production Example 1 was used instead of the sterically miscible polylactic acid, the remainder was the same as in Example 1. The polylactic acid fiber has a melting point of 1 80 °C. The resulting fabric shrinks and hardens due to the heat experienced during dyeing (texture level 1). In addition, it is a flat wear level and a poor wear resistance. Reference Example 1 In addition to 0.5 parts by weight of aluminum bis(2,2'-methylenebis(4,6-di-t-butylphenyl)phosphate) hydroxide (ADEKA (share) (original: Asahi) ADEKASTAPU NA-21 manufactured by Electrochemical Industry Co., Ltd.) As the phosphate metal salt, the operation was carried out in the same manner as in Example 1, and a sharp sublimate was generated during spinning, which was difficult to spin. Example 3 The sterically miscible polylactic acid resin obtained in Production Example 4 was dried at 110 ° C for 2 hours, and dried at 15 ° C for 5 hours to have a water content of the resin of 80 ppm. A spinning nozzle of a 36-hole diameter 27.27 mm spout hole is spun at a spinning temperature of 2 5 5 ° C at a spinning rate of 8.3 5 g/min, and the undrawn yarn is taken up at a speed of 500 m/min. . The unstretched filaments which were taken up were preheated at 80 ° C on a stretching machine for 4 · 9 times to take up the stretched yarn, and then heat-treated at 180 ° C. The spinning step and the step in the stretching step have good passability, and the drawn filament is a multifilament of 167dTex/36fil, the strength is 3.6 -37-201002907 cN/dTex, the elongation is 35%, and the single melting peak is determined by DSC. The dissolution peak temperature (melting point) was 224 ° C. The stereochemistry rate was 100%. Two pieces of the obtained three-dimensionally misaligned polylactic acid fiber were twisted, and after twisting of 160 K/m, and then arranged into a warp and weft yarn to fabricate a twill weave fabric, the fabric was made at 150 °C. After 2 minutes of dry heat setting at the temperature, the dyeing was carried out for 30 minutes at a temperature of 12 ° C using a liquid flow dyeing machine. At this time, the following disperse dye was used for dyeing, and a reduction washing treatment was carried out. (Disperse dye name) C. I. Disperse Blue 79 1 % owf Wash the obtained dye in the following reduction bath (pH 5.5): bath ratio; 1: 2 0 temperature X time; 12 (TC X 30 minute reduction bath Composition and washing conditions: sulfur dioxide urea lg/L bath ratio; 1: 2 0 temperature X time; 70 ° C x l 5 minutes, then drying at a temperature of 130 ° C for 10 minutes, drying at a temperature of 160 ° C 2 minutes. After the treatment, in the dyed fiber structure, the L値 is 38, the washing fastness is 4, and the sterically miscible lactic acid fiber contained in the woven material is treated at 70 °C X 90% RH. The fiber strength after the week was 1·8 cN/dtex (300 g/bar). Then, the woven material was used to obtain a uniform clothing, which was excellent in fastness to washing and good in durability. -38 - 201002907 Example 4 Example 3 In the above, except that the content of the phosphate metal salt was changed to a part by weight, the remainder was the same as in Example 3. The obtained dyed fiber structure was 3, and the washing fastness was 4, and the woven material contained three-dimensional. The fiber strength of the mismatched lactic acid fiber after treatment at 70 ° C x 90% RH for 1 week was 1.8 cN / dtex (300 g / strip Then, the woven material was used to obtain a uniform fabric, which was excellent in washing fastness and durability. Example 5 In Example 3, except that the content of the phosphate metal salt was changed to parts by weight, the remainder was the same as in Example 3. The obtained dyed fiber structure has an L値 of 38, and the washing fastness is 4, and the fiber density of the sterically miscible lactic acid fiber contained in the woven material is treated at 70 ° C x 90% RH for 1 week. cN/dtex (3 00 g/bar). Then, the woven material was used to obtain a uniform clothing, which was excellent in washing fastness and good in durability. Comparative Example 2 In Example 3, except that sterically miscible polylactic acid was used instead of Production Example 1 The obtained poly L-lactic acid was the same as in Example 3. The stretched yarn had a single melting peak as determined by DSC, and the melting peak temperature (melting point) was 180 ° C. The obtained fabric was 70 ° C x 9 0% RH. After 1 week of treatment, the fiber strength was 0.05 cN/dtex (8 g/strand), and it was difficult to maintain the structure of the fabric. Effect of the invention-39-201002907 According to the present invention, it is possible to obtain not only a biodegradable twin, but also a soft texture and wear resistance. Excellent in both consumption and washing fastness Dyeing IMtl Body 0 Industrial Applicability The dyed fiber structure of the present invention can be used as a raw material for fabrics, textile materials, automobile interior materials, household products, industrial materials, and the like. Brief Description of the Formula] Figure 1 shows the diffraction intensity profile of the equatorial direction for obtaining the stereoscopic rate (Sc rate).

Claims (1)

201002907 十、申請專利範圍 1. 一種經染色之纖維構造體的製造方法,其特徵爲將 包含熔點爲1 95 °c以上之聚乳酸纖維之纖維構造體染色。 2 ·如申請專利範圍第1項之製造方法’其中該聚乳酸 纖維含有(i)重量平均分子量5萬至30萬之聚L-乳酸(A 成分)、(Π)重量平均分子量5萬至30萬之聚D-乳酸(B 成分)及(iii )每a成分與B成分之合計1〇〇重量份,含有 0.05-5重量份之以下述式(1)或(2)表示之磷酸酯金屬 鹽:201002907 X. Patent application scope 1. A method for producing a dyed fiber structure, characterized in that a fiber structure comprising a polylactic acid fiber having a melting point of 1 95 ° C or more is dyed. 2. The manufacturing method according to claim 1, wherein the polylactic acid fiber contains (i) a poly-L-lactic acid (component A) having a weight average molecular weight of 50,000 to 300,000, and a weight average molecular weight of 50,000 to 30. D-lactic acid (B component) and (iii) 1 part by weight of each a component and B component, and 0.05 to 5 parts by weight of a phosphate metal represented by the following formula (1) or (2) salt: (1) 式(1)中,R!表示氫原子或碳數1〜4之院基’ R2、r3各獨 立表示氫原子或碳數1〜12之烷基,Μ!表示鹼金屬原子或鹼 土類金屬原子,Ρ表示1或2, 201002907(1) In the formula (1), R! represents a hydrogen atom or a group of carbon atoms 1 to 4', and R3 each independently represents a hydrogen atom or an alkyl group having 1 to 12 carbon atoms, and Μ! represents an alkali metal atom or an alkaline earth. Metal-like atom, Ρ means 1 or 2, 201002907 (2) 式(2)中,R4、R5及R6各獨立表示氫原子或碳數1〜丨2之 烷基,M2表示鹼金屬原子或鹼土類金屬原子,P表示1或2 〇 3 .如申請專利範圍第1項之製造方法,其中聚乳酸纖 維以每聚L-乳酸成分與聚D-乳酸成分之合計1〇〇重量份’ 含有0.1〜5重量份之碳二醯亞胺化合物,且在130°C之高溫 水中處理30分鐘後之分子量維持率爲85%以上。 4 ·如申請專利範圍第1項之製造方法,其中聚乳酸纖 維之單絲纖度在0.0 1〜2 0 dtex之範圍內。 5 .如申請專利範圍第1項之製造方法,其中聚% _ Μ 維之絲強度爲2.5 cN/dtex以上。 6 ·如申請專利範圍第1項之製造方法,其中纖維構造 體中含有其他纖維。 7 ·如申請專利範圍第6項之製造方法’其中其他纖維 爲聚對苯二甲酸乙二醇酯纖維。 8 .如申請專利範圍第i項之製造方法,其中纖維構造 體爲織物或編物。 9.如申請專利範圍第丨項之製造方法,其中染色溫度 在110〜140 °C之範圍內。 -42 - 201002907 10.如申請專利範圍第1項之製造方法,其中經染色處 理後實施還原洗淨處理。 1 1 如申請專利範圍第1 0項之製造方法,其中還原洗 淨處理係在pH8〜2之還原浴中,於溫度60〜98。(:之範圍內進 行。 1 2.如申請專利範圍第1項之製造方法,其中經染色後 ’於纖維構造體上賦予矽樹脂、聚乙烯樹脂或聚對苯二甲 酸乙二醇酯樹脂。 13. —種經染色之纖維構造體,其係藉由申請專利範 圍第1~12項中任一項之製造方法所製造。 1 4 ·如申請專利範圍第1 3項之纖維構造體,其中纖維 構造體中所含之聚乳酸纖維之纖維強度爲2.3 cN/dteX以上 〇 1 5 _如申請專利範圍第1 3項之纖維構造體,其中在溫 度70°C、濕度90%rh之環境下處理一週後,纖維構造體中 所含之聚乳酸纖維之纖維強度爲0.5 cN/dtex以上。 1 6 .如申請專利範圍第1 3項之纖維構造體,其係基量 在30~l,000g/m2之範圍內之布帛。 1 7 ·如申請專利範圍第丨3項之纖維構造體,其平面磨 耗性爲3級以上之布帛。 1 8 如申請專利範圍第丨3項之纖維構造體,其亮度指 數(L値)爲80以下。 1 9.如申請專利範圍第丨3項之纖維構造體,其係藉由 AATCC IIA法測定之洗滌堅牢度爲3級以上。 -43- 201002907 2 0,一種纖維製品,其係選自由使用申請專利範圍第 1 3〜1 9項中之任一項之經染色纖維構造體所構成之衣料、 衣料資材、汽車內裝材、家居用品、產業資材及小物品類 組成之群組。 -44-(2) In the formula (2), R4, R5 and R6 each independently represent a hydrogen atom or an alkyl group having 1 to 2 carbon atoms, M2 represents an alkali metal atom or an alkaline earth metal atom, and P represents 1 or 2 〇3. The manufacturing method of the first aspect of the invention, wherein the polylactic acid fiber contains 0.1 to 5 parts by weight of a carbodiimide compound per 1 part by weight of the total of the poly-L-lactic acid component and the poly-D-lactic acid component, and The molecular weight retention after treatment in high temperature water at 130 ° C for 30 minutes was 85% or more. 4. The manufacturing method according to claim 1, wherein the polyfilament fiber has a single filament fineness in the range of 0.01 to 20 dtex. 5. The manufacturing method of claim 1, wherein the poly% _ Μ silk has a strength of 2.5 cN/dtex or more. 6. The manufacturing method of claim 1, wherein the fiber structure contains other fibers. 7. The manufacturing method as claimed in claim 6 wherein the other fibers are polyethylene terephthalate fibers. 8. The manufacturing method of claim i, wherein the fibrous structure is a fabric or a knitted fabric. 9. The method of manufacturing the invention of claim 2, wherein the dyeing temperature is in the range of 110 to 140 °C. The manufacturing method of claim 1, wherein the reduction washing treatment is carried out after the dyeing treatment. 1 1 The manufacturing method of claim 10, wherein the reduction washing treatment is carried out in a reduction bath having a pH of 8 to 2 at a temperature of 60 to 98. (2) The method according to the first aspect of the invention, wherein after the dyeing, a resin, a polyethylene resin or a polyethylene terephthalate resin is imparted to the fiber structure. 13. A dyed fibrous structure produced by the manufacturing method of any one of claims 1 to 12. 1 4 - a fibrous structure according to claim 13 of the patent application, wherein The fiber strength of the polylactic acid fiber contained in the fiber structure is 2.3 cN/dteX or more 〇1 5 _ as in the fiber structure of the third aspect of the patent application, wherein the temperature is 70 ° C and the humidity is 90% rh After one week of treatment, the fiber strength of the polylactic acid fiber contained in the fiber structure is 0.5 cN/dtex or more. 16. The fiber structure of the third aspect of the patent application has a basis weight of 30 to 1,000 g. Fabrics in the range of /m2. 1 7 · If the fiber structure of the third paragraph of the patent application is applied, the plane wearability is a fabric of grade 3 or higher. 1 8 If the fiber structure of the third paragraph of the patent application is applied, Its brightness index (L値) is below 80. The fiber structure of the third aspect of the patent, which has a washing fastness of 3 or more by the AATCC IIA method. -43- 201002907 2 0, a fibrous product selected from the scope of application patents. Group of clothing materials, clothing materials, automotive interior materials, household products, industrial materials and small items consisting of dyed fiber structures of any of the items.
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