TW201134992A - Flame retardant fiber assembly, method for producing same, and fiber product - Google Patents

Flame retardant fiber assembly, method for producing same, and fiber product Download PDF

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Publication number
TW201134992A
TW201134992A TW100101836A TW100101836A TW201134992A TW 201134992 A TW201134992 A TW 201134992A TW 100101836 A TW100101836 A TW 100101836A TW 100101836 A TW100101836 A TW 100101836A TW 201134992 A TW201134992 A TW 201134992A
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Taiwan
Prior art keywords
fiber
flame
retardant
mass
metal compound
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TW100101836A
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Chinese (zh)
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TWI530597B (en
Inventor
Takeshi Tanaka
Toshiaki Ebisu
Hiroyasu Hagi
Masaaki Miyoshi
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Kaneka Corp
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Publication of TWI530597B publication Critical patent/TWI530597B/en

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    • 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
    • D01F1/07Addition of substances to the spinning solution or to the melt for making fire- or flame-proof filaments

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  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Textile Engineering (AREA)
  • Artificial Filaments (AREA)

Abstract

Disclosed are: a flame retardant fiber assembly which has satisfactorily high flame retardancy and satisfactorily high flame shielding performance; a method for producing the flame retardant fiber assembly; and a fiber product. Specifically disclosed is a flame retardant fiber assembly, which contains 3-30% by mass of halogen-containing fibers, 20-50% by mass of polyester fibers and 30-77% by mass of flame retardant fibers other than the halogen-containing fibers. The halogen-containing fibers contain a polymer (1) that contains 30-70% by mass of acrylonitrile, 70-30% by mass of a halogen-containing vinylidene monomer and/or a halogen-containing vinyl monomer, and 0-10% by mass of a vinyl monomer that is copolymerizable with the aforementioned compounds, and at least one metal compound (2) that promotes a dehalogenation reaction of the polymer (1) during combustion or a carbonization reaction of the polymer (1) during combustion. The halogen-containing fibers have a shrinkage variation of not more than 65% when the temperature thereof is raised from 50 DEG C to 300 DEG C under a load of 0.0054 mN/dtex.

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201134992 六、發明說明: 【發明所屬之技術領域】 本發明係關於一種具有高度難燃性之難燃纖維集合體及 其等之製造方法、與纖維製品,該難燃纖維集合體藉由在 ' 燃燒時表現出極高度之碳化性、形態保持性、自媳性,而 可適宜用於寢具或傢俱等所使用之必需高度之難燃性的纖 維製品。 【先前技術】 近年來,確保衣食住之安全性之要求提高,就防火之觀 點考慮,難燃原料之必要性正在提高。其中,特別是為了 防止發生時人的受害較大之就寢中之火災’對寢具或傢俱 等所使用之原料賦予難燃性之必要性正在提高。 於該等寢具或傢倶等布藝製品中,為實現使用時之舒適 性或設計性,多將棉或聚酯、胺基甲酸酯發泡體等易燃性 原料用於其内部或表面。為確保其等之難燃性,重要的是 藉由將適當之難燃原料用於該等製品中,而使其具有長時 間防止該易燃性原料著火之高度難燃性。X,該難燃原料 亦必需保持該等寝具或傢倶等製品之舒適性或設計性。 . 4乍為使用該冑燃原料之一之纖維的難燃纖維原料,過去 . 肖各種難燃性纖維及防火劑進行了研究,但仍未出現—種 使該高度之難燃性與對寢具或傢倶等製品所要求之舒適性 或設計性等必要條件充分保持均衡者。 例如有對棉布塗布防火劑之所謂後加卫防火之方法但 存在防火劑附著之均句化、由附著引起之布之硬化、由^ 152753.doc 201134992 滌引起之脫離、安全性等問題。 二作為廉價原料之㈣系纖維於燃燒時溶融 維製成布㈣,會產生孔洞,無法維持結構,而 火,具f傢俱等所使用之棉或胺基甲酸㈣泡體著 .·、性能而言並不充分。亦存在含㈣原子等之難辦 纖維,但燃燒時之行為與上述同樣,最終溶融,作 為性此而言並不充分。 又1三氧化錄或五氧㈣、氧域#添加至纺絲原液 中而獲得高難燃改良丙烯酸纖維(modacrylic fiber)之方法 雖可賦予難燃性,但存在對火或熱之遮斷性未達到令人滿 意之程度的問題。作為該等性能中,即料難燃性且滿足 對火或熱之遮斷性者,存在添加有含有甲基丙烯酸縮水甘 油酯之聚合物的交聯高難燃丙烯酸系纖維(專利文獻”,但 田曝露於如燃燒器火之強力火焰下時,存在纖維本身分解 而最終著火之情形。 又,存在添加有水玻璃或氧化鋅等所代表之固相難燃劑 之高難燃火焰阻隔性改良丙烯酸纖維(專利文獻2),但存在 以下情形:該等纖維雖然滅火性能或火焰阻隔性能優異, 但燃燒時形成之碳化膜較硬,根據傢俱或寢具之種類或燃 燒部位之形狀,有時纖維之收縮變動大,故對燃燒時之碳 化膜施加應力’而於碳化膜上產生龜裂,或者因少許之荷 重而於碳化膜上產生開孔。作為解決該問題之方法,提出 有藉由添加氧化辞及縮合磷酸鹽系化合物,控制收縮時之 碳化速度,而使龜裂難以產生之改良丙烯酸纖維(專利文 152753.doc 201134992 獻3),但於使用該等纖維時,存 非複數種且限定種類 之纖維,以及限定之纖維混率’ 的問題。 彳‘“、法獲得面度之難燃性 又,亦提出有藉由實施濕熱緊張埶虚 熟處理,而獲得耐熱收 縮性良好之丙烯酸系合成纖維之製造 方法(專利文獻4)。然 而存在以下問題,由於在緊張狀態 〜r取予熱處理,故無法 充分去除殘留收縮應力,雖可抑制 』抑制16〇C之相對低溫下之 收縮,但於如火焰之2Gn:以上之高溫下明顯收縮,结果 難燃性差。又,由於作為實用纖維製品而必需之與其他纖 維之混用亦完全未考慮’故無法耐受作為實用之難燃原料 之使用。 已分別提出將添加有大量難燃劑之高度難燃化之含㈣ 纖維與非難燃纖維加以組合而成的難燃纖維集合體(專利 文獻5)、以及由本質上為難燃性之纖維與含函素纖維等所 構成之具有蓬鬆感之難燃性不織布(專利文獻6)。 然而,該等方法存在以下等問題:燃燒時無法保持布第 或織物等燃燒前之形態,無法確保所需之難燃性、特別是 火焰阻隔性;通常耐熱性纖維或本質上為難燃性之纖維: 容易獲得所需之_性,但纖維本身大多硬且脆,原材料 製造加工時之操作極其困難,而且成本較高。 [先前技術文獻] [專利文獻] [專利文獻1]曰本專利特開2005] 79876號公報 [專利文獻2]日本專利特開2〇〇6_2258〇5號公報 152753.doc 201134992 [專利文獻3]曰本專利特開2007-2915 70號公報 [專利文獻4]曰本專利特開昭58-156014號公報 [專利文獻5]曰本專利特開昭61-89339號公報 [專利文獻6]美國專利7259117號 【發明内容】 [發明所欲解決之問題] 本發明為解決上述先前之問題,而提供一種滿足較高之 難燃性、尚度之火焰阻隔性的難燃纖維集合體及其製造方 法、與纖維製品。 [解決問題之技術手段] 本發明之難燃纖維集合體含有含齒素纖維、聚酿系纖 維、及含齒素纖維以外之難燃性纖維。當將上述難燃纖維 集合體之總量設為100質量%時,上述含鹵素纖維之含量 為3〜30質量%,上述聚酯系纖維之含量為2〇〜5〇質量。,且 上述含鹵素纖維以外之難燃性纖維之含量為3〇〜77質量 %。上述含齒素纖維之特徵在於,含有包含丙烯腈3〇〜7〇 質量/〇 3鹵素亞乙烯基單體及/或含鹵素乙烯基單體 7〇〜30質量%、及可與該等共聚合之乙烯基系單體〇〜1〇質 量%的總量100質量%之聚合物⑴,與促進上述聚合物⑴ 之燃燒時之脫齒反應及燃燒時之碳化反應的至少丨種金屬 化口物(2),且於0.0054 mN/dtex之荷重下將溫度自贼提 高至300t時之收縮變動為65%以下。 本發明之難燃纖維集合體之製造方法的特徵在於:上述 難燃纖維集合體係含有含南素纖維、聚醋系纖維、及含齒 152753.doc 201134992 素纖維以外之難燃性纖維者;上述製造方法包括如了步 驟:當將上述難燃纖維集合體之總量設為100質量。/。時, 將3〜30質量%之上述含齒素纖維、20〜50質量%之上述聚醋 系纖維、及30〜77質量%之上述含鹵素纖維以外之難燃性 纖維加以混合;上述含鹵素纖維於0.0054 mN/dtex之荷重 - 下將溫度自50°c提高至3〇〇°C時之收縮變動為65%以下; 該含鹵素纖維係藉由使含有包含丙稀腈3〇〜70質量%、含 函素亞乙烯基單體及/或含鹵素乙烯基單體7〇〜3〇質量0/〇、 及可與該等共聚合之乙烯基系單體〇〜1〇質量%的總量1〇〇 質量%之聚合物(1) ’與促進上述聚合物(1)之燃燒時之脫鹵 反應及燃燒時之碳化反應的至少丨種金屬化合物(2)之組合 物進行紡絲後’實施熱處理而獲得。 本發明之纖維製品之特徵在於包含上述難燃纖維集合 體。 [發明之效果] 根據本發明,可獲得具有較高之難燃性、高度之火焰阻 隔性的纖維製品。 【實施方式】 本發明者等人為解決上述問題而反覆銳意研究,結果發 ' 現’以預定含量含有含_素纖維、聚S旨系纖維、及含齒素 纖、准以外之難燃性纖維之難燃纖維集合體發揮高度之難燃 上述3鹵素纖維含有包含丙烯腈30〜70質量。/〇、含鹵 二乙烯基單體及/或含函素乙烯基單體7。〜30質量。/。、及 β ”。亥等共聚合之乙烯基系單體〇〜1〇質量%的總量ι〇〇質 152753.doc 201134992 量%之聚合物(1),與促進上述聚合物(1)之燃燒時之脫函反 應及燃燒時之碳化反應的至少丨種金屬化合物(2),且於 0.0054 mN/dtex之荷重下將溫度自5〇t提高至3〇〇t時之收 縮變動為65%以下’從而完成本發明。 (含鹵素纖維) 於本發明中,含鹵素纖維包含聚合物(1)、與促進上述 聚合物(1)之燃燒時之脫齒反應及燃燒時之碳化反應的至少 1種金屬化合物(2)。上述聚合物〇)包含丙烯腈3〇〜7〇質量 4、含鹵素亞乙烯基單體及/或含鹵素乙烯基單體〜3〇質 量/。及可與6亥等共聚合之乙烯基系單體〇〜丨〇質量%,總 量為100質量%。又’上述聚合物⑴較佳為包含丙烯腈 4〇〜65質量。/。、含齒素亞乙烯基單體及/或含齒素乙烯基單 體60〜35質量%、A可與該等共聚合之乙烯基系單體〇〜ι〇 質量。/。。於上述聚合物⑴中’若丙稀腈含量為4g〜65質量 % ’則容易獲得纖維化時所必需之耐熱性,且亦可實現難 燃化。更佳之丙稀腈含量為5G〜㈣量%,若為該範圍, 則纖維之著色變得更少。 作為上述聚合物⑴,例如可列舉:丙稀猜_偏二氣〔 烯、丙烯腈-偏二氣乙烯·偏二敗乙稀等含南素亞乙稀基另 單體之1種以上與丙稀腈之共聚物;偏二氣乙烯、偏1 乙烯、偏二氟乙烯等含齒素亞乙烯基系單體之!種以上、 與丙稀腈以及可與該等共聚合之乙稀基系單體之共聚彩 專’但並不限^於該等。又,亦可將—種以上之上述共聚 物適當混合使用 152753.doc 201134992 作為上述可與該等共聚合之乙稀基系單體,例如可列 舉:丙烯酸及其酯、甲基丙烯酸及其酯、丙烯醯胺、甲美 丙稀酿胺、乙酸乙稀6旨、乙烯基㈣及其鹽、甲基缔丙i 績酸及其鹽、苯乙烯料及其鹽、2•㈣醯胺_2_甲基續酸 及其鹽等,可使用該等以種或2種以上。又,於其中至少 1種為含較基乙烯基系單體之情形時,$色性提高,故 較佳。 上述共聚物⑴可利用已知之聚合方法而獲得。例如, 作為聚合方式,可列舉塊狀聚合、m合、乳化聚合、 >谷液聚合等,作為聚合形態,可列舉連續式、批次式、半 批次式等,但並不限定於該等。其中,就工業觀點而言, 作為聚合方式,較佳為乳化聚合與溶液聚合,作為聚合形 態’較佳為連續式與半批次式。 作為促進上述聚合物(1)之燃燒時之脫函反應及燃燒時 之碳化反應的至少1種金屬化合物(2),可使用促進脫鹵反 應及碳化反應之兩反應的選自氧化辞、碳酸鋅、硫化鋅、 硼酸鋅、錫酸鋅、偏錫酸、氧化鎢、氧化锆、氧化錫、氧 化銅、磷酸銅、三氧化銦、鈦酸鋇、對甲苯磺酸鋅中之金 屬化合物(2-i) ’或將上述金屬化合物(2-1)與促進脫鹵反應 之選自銻化合物、氧化鐵、磷酸鐵、草酸鐵、硫化鐵、氧 化翻、三氧化鉍、氧氣化鉍、碘化銅中之金屬化合物(2-2) 組合使用。 本發明者等人認為,上述金屬化合物(2-1)促進聚合物 (1)之燃燒時之脫齒反應,促進成為燃燒時之碳化反應之前 152753.doc 201134992 驅物的多烯之生成,進而,藉由脫齒而生成之金属函化物 對多稀結構發揮觸媒作用而促進碳化。作為上述金屬化合 物(2 1) ’就促進其後之碳化之方面而言,較佳為使脫齒反 應於200 C以下產生之化合物。尤佳為選自氧化辞、錫酸 鋅、碳酸鋅、及氧化錫中之至少一種。 上述金屬化合物(2-1)除了可單獨使用以外,亦可組合使 用種以上又’亦可將上述金屬化合物(2_ j)與選自録化 合物' 氧化鐵、磷酸鐵、草酸鐵、硫化鐵、氧化鉬、三氧 化祕、氧氣化Μ、魏鋼中之促進聚合物⑴之燃燒時之脫 鹵反應的金屬化合物(2_2)組合使用。促進聚合物之脫 鹵反應之金屬化合物(2_2)藉由促進聚合物(1)之脫鹵反 應,而促進成為碳化反應之前驅物的多烯之生成,但另一 方面由於未兼具促進來自所生成之多烯結構之碳化的能 力,故金屬化合物(2-2)之單獨使用並不有效。 作為上述金屬化合物(2_2),尤佳為銻化合物。銻化合物 不僅促進聚合物⑴之燃燒時之脫纽應,而且藉由脫齒而 生成之銻齒化物於燃燒時之較廣溫度區域形成氣體,該氣 體發揮捕捉自由基而抑制燃燒之作用,即滅火性能。 作為上述銻化合物,可列舉:三氧化銻、四氧化銻、五 氧化銻等氧化銻化合物,銻酸或其鹽類,氧氣化銻等無機 銻化合物等,但並不限定於該等。又,亦可將該等組合使 用。其中,就性能及工業獲得性之觀點而言,較佳為三氧 化錄及五氧化録。 相對於上述聚合物(1) 100質量份,金屬化合物(2)之添 152753.doc -10- 201134992 加量較佳為0.05〜50質量份。關於下限值,更佳為〇」質量 :’進而更佳為1質量份。又’關於上限值,更佳為40質 里伤,進而更佳為30質量份。若金屬化合物⑺之使用量為 ㈣5〜50質量份’則具有燃燒時使聚合物碳化之效果(碳化 效果),可獲得為了獲得所需之高度難燃性能而必需的碳 化效果,且獲得所需之收縮率。若為較佳之範圍,則上述 作用效果變得更高。 相對於上述聚合物(1) 1〇〇質量份,金屬化合物之添 加量較佳為G.G5〜5G質量份。關於下限值,更佳為〇1質量 伤’進而更佳為1質量份。又,關於上限值,更佳為質 量伤’進而更佳為3〇質量份。若金屬化合物(2_ i)之使用量 為0.05 50貝量份,則具有燃燒時使聚合物碳化之效果(碳 化效果),可獲得為了獲得所需之高度難燃性能而必需的 石厌化效果,且獲得所需之收縮率。若為較佳之範圍,則上 述作用效果變得更高。 相對於上述聚合物(丨)100質量份,金屬化合物之添 加量為0〜50質量份,較佳為3〜4〇質量份,更佳為5〜3〇質量 份。亦存在即便為〇質量份亦可達成所需難燃性能之情 形,但自熄效果較小,故於用於要求更高之自熄效果之用 途時’較佳為添加3質量份以上、40質量份以下。 作為上述金屬化合物(2)之平均粒徑,較佳為3 μιη以 下,更佳為2 μπι以下。若金屬化合物(2)之平均粒徑為3 μιη以下’則就於含_素聚合物中添加金屬化合物成分而 成之纖維之製造步驟中的噴嘴堵塞等故障避免、纖維之強 152753.doc •11- 201134992 度提高、纖維中之金屬化合物成分粒子之 =:金:化合物⑺之平均粒徑之下限並無特而: :性二方面而言’較佳為—上,更佳 1上香進而’上述金屬化合物⑺可為改善結塊性而對粒子 實施化學修飾’亦可於分散於水中或有機溶劑中之狀 態下使用。此處’所謂平均㈣,係指中絲徑。作為中 值粒徑之測定方法,可使用光散射法。 上述含陳纖維較佳為相對於上述聚合物⑴100質量 份,而進-步含有含環氧基化合物01〜20質量份。藉由含 有含環氧基化合物,而利用纖維製造步驟中之乾燥或熱: 理進行交聯,於纖維中形成高分子交聯結構,從而可進一 步抑制纖維之收縮。 作為上述含環氧基化合物,可列舉含有環氧基之聚合 物’例如可為縮水甘㈣型、縮水甘油胺型、縮水甘油酉旨 型、環狀脂肪族型、或含有該等之共聚物。若考慮到於纺 絲〉合中之溶出、每單位重量之反應基(環氧基)之數量,則 作為縮水甘油酯類,例如較佳為使用聚甲基丙烯酸縮水甘 油醋(重量平均分子量為3000〜100000)。 於上述含齒素纖維中,視需要亦可含有抗靜電劑、熱著 色防止劑、耐光性提昇劑、白度提昇劑、失透性防止劑、 著色劑、難燃劑等其他添加劑。 上述含鹵素纖維之於0.0054 mN/dtex之荷重下將溫度自 50 C提向至300°C時之收縮變動為65°/。以下。 上述中’所謂將溫度自50°C提高至30〇t時之收縮變 152753.doc 12· 201134992 動,係指於5(TC至300°C之溫度範圍内,收縮率之最高點 與最低點之差量。該差量必需為〇以上之數值。若以本案 圖式中之表記而言,則例如相當於圖9〜丨5中之箭頭所示之 le·圍。若具體說明’則如下所述: 1·例如,如圖9或圖11所示,於隨著溫度上升而單調收縮 之情形時,收縮變動成為匕點^乂^⑽^^之收縮率。 2.如圖12〜15所示,於收縮後一度伸長,並再次收縮之情 形時,根據一度伸長時之伸長情況,於圖12中,收縮變動 成為c點之收縮率,於圖13中,收縮變動成為1點之收縮 率,於圖14、15中,收縮變動成為1)點之收縮率與b,點之收 縮率之差。 3, 如圖10所示,於收縮後單調伸長、或者伸長並於中途十 斷之情形時,收縮變動成為箭頭所示之收縮率(伸長並中 斷之情形時,收縮變動為〇〇)。 4. 圖中之a點為軟化開始點。於3點〜b點之間,產生由應力 緩和引起之收縮、由脫齒引起之收縮及由軟化引起之「伸 長」’收縮勝過伸長。以後,成為由脫南引起之收縮、 由碳化引起之收縮(形狀維持)、由軟化引起之「伸長」的 競爭,形成如下圖案: ⑴於碳化能力優異之情形時,收縮(或形狀維持)勝過伸 長’形成如圖9或圖11之收縮圖案; 於b點附近伸長處於優 ,於某點(圖中b'點)再 (2)於石反化能力猶差之情形時, 勢’隨著溫度上升而碳化處於優勢 次開始收縮(圖12、13、14、15); 152753.doc 201134992 (3)於無碳化能力之情形_,b點以後,伸長處於優勢, 形成圖10之收縮圖案。 5.上述含鹵素纖維之收縮圖案有4種(圖9、圖12、圖13、圖 14)。上述含鹵素纖維之收縮圖案中最佳為圖9,其次為圖 12,再其次為圖13、圖14。可為如圖9所示由應力緩和引 起之收縮與由脫函引起之收縮小,且碳化能力$,單調收 縮最佳之收縮圖案,亦可為如圖12、13、14所示碳化能力 梢差,即便碳化前藉由軟化而伸長,亦會於某溫度以上再 •人產生碳化而收縮(形狀維持)之收縮圖案。其中,更佳為 圖中b,點之收縮率為G%以h又,上述含㈣纖維於 0.0054 mN/dtex之荷重下將溫度自5〇β(:提高至3〇η:時進 行碳化,未切斷而殘存。於本發明中,所謂上述含函素纖 維於0.0054 mN/dtex之荷重下將溫度自5〇〇c提高至3〇〇β(:時 進行碳化,未切斷而殘存,係指一面於〇〇〇54 mN/dtex之 荷重下將溫度自5(TC提高至30(rc,一面利用下述纖維收 縮率之測定方法測定纖維收縮率之情形時,上述含齒素纖 維並未切斷而殘存。 6.與此相對’圖1 〇、圖! i、圖j 5表示收縮變動超出“%之 情形之收縮變動。圖10中,若提高溫度,則會失去彈性或 切斷。圖11中’碳化能力優異,㈣溫度上升而單調收 縮,但由應力緩和引起之收縮(圖中a〜b點)過大,結果將溫 度自50 C提尚至300°C時之收縮變動超出65%。圖15係與 圖12、13相同之收縮圖案,但碳化能力弱,伸長處於優 勢,收縮變動(b點之收縮率與b’點之收縮率之差)超出 152753.doc •14· 201134992 65% 〇 上述含鹵素纖維較佳為單纖維強度為〇 5〜16 cN/dtex, 更佳為0.5M.1 cN/dtex。上述含齒素纖維中,於〇 〇〇54 二N/dtex之荷重τ將溫度自贼提高至曹c時之收縮變動 容易成為65%以下,獲得較高之難燃性。於本發明中,將 單纖維強度係依據JIS L 1 015而測定者。 上述含i素纖維可為短纖維,亦可為長纖維,可於使用 方法中適當選擇。纖度係根據難燃纖維集合體及纖維製品 之用途而適當選擇,較佳W〜5〇如,更佳為15〜3〇 dtex’進而更佳為L7〜15 dtexe切割長度可根據難燃纖維 集合體及纖維製品之用途而適當選擇。例如可列舉:短切 纖維(纖維長0.1〜5 mm)或短纖維(纖維長“〜丨“爪⑷、或 完全未切割之長纖維(長絲)。其中,較佳為纖維長3㈣ 麵左右之短纖維…可與組合使用之其他纖維之纖度 相同,亦可更細或更寬。 對上述含鹵素纖維之難燃機制進行說明。 (1)關於金屬化合物(2-1) 作為金屬化合物(2-1) ’例如列舉氧化鋅一般認為氧化 鋅具有促進含齒素纖維之脫齒反應之作用。又,本發明者 等人認為,藉由脫_、⑽齒化氫而生成之齒化鋅(於氣之 情形時為氣化辞(ZnCl2))不僅對多稀結構發揮觸媒作用而 促進碳化(燃燒時之殘渣成為形態保持成分),而且亦有助 於丙烯腈之三畊環形成反應(纖維藉由環化而收縮卜上述 效果不僅可利用氧化鋅而發揮,而且亦可利用其他辞化: 152753.doc 15 201134992 物、胺曱酸鋅或辛酸鋅等有機鋅化合物、或者氧化錫或氧 化銅等一部分金屬氧化物而發揮。又,作為由金屬化合物 (2·1)引起之碳化、環化促進作用之結果而產生之碳化物牢 固,可使殘渣、特別是保持纖維形態之殘渣之存在成為可 能。於使火接觸於使用殘存有上述加熱時之殘渣、特別是 保持纖維形態之殘渣之纖維的布第、不織布等複合體上 時,可藉由該殘渣而阻隔火焰。 (2)關於使於0.0054 mN/dtex之荷重下將溫度自5〇t提高 至300°C時之收縮變動為65%以下 通常,含鹵素纖維於加熱(燃燒)時暫時收縮,其後表現 出擴展之行為。作為加熱(燃燒)時之收縮要因,考慮到以 下兩個要因:a.由碳化引起之收縮、b.由紡絲殘留應力引 起之收縮。其t,a.由碳化引起之收縮起因於自共聚物之 脫南反應、丙烯腈之三畊環形成。其係源自共聚物組成之 化學反應,難以抑制由該反應引起之收縮。另一方面,汰 由紡絲殘留收縮應力引起之收縮起因於纖維製造過程中之 凝固或延伸操作時賦予纖維之殘留應變’可藉由適當選擇 纖維之製造條件、特別是纖維製造過程中之熱處理條件而 抑制。作為熱處理方法,可列舉鬆弛熱處理、濕熱15〇它 以上之緊張熱處理、乾熱180。〇以上之緊張熱處理。其 中作為充分抑制紡絲殘留應力之熱處理方法,較佳為鬆 他熱處理。藉由實施該等熱處理’可抑制紡絲殘留收縮應 力,可將加熱(燃燒)時之收縮變動,即於0.0054 mN/dtex 之荷重下將溫度自50 C提高至300°C時之收縮變動設為 152753.doc -16· 201134992 下將溫度自50°C提 則表現出較高之難 65%以下。若於0.0054 mN/dtex之荷重 尚至3 00°C時之收縮變動為65%以下, 燃性 '高度之火焰阻隔性。例如,於美國之床之燃燒試驗 16CFR1633中’由於並無以下於試驗中不合格之情形而較 佳.燃燒時,纖維收縮得到抑制,於曝露於火焰中之部分 產生孔洞,或者因應變而產生龜裂,火焰自該處進入,而 使内部易燃性結構物著火。就表現出更高之難燃性 '更高 之火焰阻隔性之方面而言 上述於0.0054 mN/dtex之荷重 下將溫度自50°C提高至30(TC時之I缩變動較佳為6〇%以 下,更佳為50%以下,尤佳為45%以下。再者,上述於 0.0054 mN/dtex之荷重下將溫度自5(rc提高至3〇〇r時之收 縮變動較佳為儘可能小,越接近於〇%越佳。又,較佳為 於0.0054 mN/dtex之荷重下將溫度自5(rc提高至3〇(Γ(:時, 進行碳化,並未切斷而殘存。於本發明中,上述含函素纖 維之軟化溫度與脫鹵起始溫度(分解點)接近,故若提高熱 處理溫度,則存在由於產生脫_反應而使纖維著色,或者 難以賦予充分之熱處理之情形。作為該解決對策,有降低 上述含齒素纖維之丙烯腈含量而降低軟化點之方法,藉此 可將熱處理溫度設定為分解溫度以下。此外,若為加壓濕 熱條件下,則於軟化點溫度以下亦可進行充分之熱處理。 (3)關於含有環氧基之聚合物(作為一例之聚甲基丙烯酸 縮水甘油酯(pGMA))之收縮抑制機制 使pGMA於紡絲製程中反應,而於纖維中導入高分子交 聯結構,藉此抑制收縮。本發明者等人認為,pGMA係利 152753.doc •17· 201134992 用乾燥或熱處理之熱而進行交聯,只要存在酸觸媒,則可 進一步進行交聯。本發明者等人認為,上述含齒素纖維中 所含之金屬氧化物(三氧化銻(Sb2〇3)、氧化鋅(Zn〇))奪取 纖維中所含之聚合物中之i素而形成自化物(於氣之情形 時,形成SbClrZnCl2),該等作為酸觸媒而促進{)(}1^八之 交聯。 上述含函素纖維可藉由使含有包含丙烯腈3〇〜7〇質量 %、含ώ素亞乙烯基單體及/或含齒素乙烯基單體7〇〜3〇質 量%、及可與該等共聚合之乙稀基系單體〇〜1〇質量%的聚 合物(1) ’與促進燃燒時之脫_反應及燃燒時之碳化反應的 至少i種金屬化合物(2)之組合物進行紡絲後,實施熱處理 而製造。具體而言,可利用濕式紡絲法、乾式纺絲法、半 乾半濕式法等公知之方法進行。例如,於濕式纺絲法中, 藉由使上述聚合物溶解於队沭二甲基甲醯胺、n,n_二甲基 乙醯胺、丙輞、硫氰酸鹽水溶液、二甲基亞硬、’石肖酸水溶 液等溶劑中後,使其通過喷嘴擠出至凝固浴中而使其凝 固,繼而進行延伸、水洗、乾燥、熱處理,視需要賦予捲 縮進仃切斷,由此獲得製品。上述溶劑較佳為二甲 基甲醯胺、N,N-二甲基乙酿胺、丙酮’進而,n,n_二甲基 甲醯胺、丙酮由於可於工業上操作,故而較佳。 土 再者’若於0·0054 mN/dtex之荷重τ將溫度自抓提高 至3〇〇C時之收縮變動為65%以下之範圍,則亦可於纺出 後、熱處理前進行延伸。即’上述含南素纖維之製造亦可 藉由將含有上述組合物之纺絲液擠出(纺出),進行一次延 152753.doc 201134992 2水洗,其後加以乾燥,進行二次延伸,並實施执處理 订。於本發明中,所謂—次延伸,係指於纺出後、直 至乾燥之前之纖維製造步驟(纺絲步驟)中進行延伸 作,所謂二次延伸,係指自乾 ,、 :進打延伸之操作。再者,一次延伸只要在乾燥步驟: 前,則可於任一步驟中進行’例如可於水洗前進行、一面 =一面進行、水純進行、或者自水洗巾連續進行 洗後。 於上述含函素纖維之製造中,延伸倍率乘以緩和倍率所 得之總延伸倍率决伸倍率x緩和倍率)較佳為5倍以下,更 佳為4.8倍以下,尤佳為3 7倍以下。藉此,可進—步抑制 紡絲殘留收縮應力’可獲得更高之難燃性。又,上述總延 伸倍率較佳為(M倍以±,更佳為! 〇倍以1。 、 於本發明中’所謂延伸倍率’係指於熱處理前之纖維製 造步驟(紡絲步驟)中纖維長所延伸之比例。上述熱處理前 之纺絲步驟例如包括凝固步驟(紡絲液之擠出)、水洗步驟 (々亦包括-面水洗一面延伸之情形)、乾燥步驟、延伸步驟 等處理。若假定為纖維長不變之處理,例如絲線(纖維束) 於2個親間移動時之處理,則於人側輥速度與出側輕速度 相同之情形時,延伸倍率為1()倍,若假^為纖維長成為3 倍之處理,例如絲線(纖維束)於2個輥間移動時之處理,則 於出側輥速度為入側輥速度之3倍之情形時,延伸倍率成 為3·〇倍。上述延伸倍率並無特別限定,就纖維之生產性 及纖維強度之表現、以及使於0.0054 mN/dtex之荷重下將 152753.doc •19· 201134992 溫度自5〇C提高至3〇〇。广d* 回至3〇〇C時之收縮變動設為⑽以下 面而言,較佳為1.〇〜10 〇倍〇 ^ 又作為上述延伸俾座夕π 限值,更佳為2.0倍… 逆评借羊之下 |尤佳為3·〇倍’作為上限值,更佳Α 9.0倍,尤佳為8.0倍。 為 中Μ、早、f料a 於”,、處理前之複數個紡絲步驟 2賦予複數:人延伸之情形時,本發明之延伸倍率為各延伸 2予步财之延伸倍率相乘所得者。例如,如上所述,於 仇本、 仃— 人延伸及二次延伸之情形時,延伸 倍率為一次延伸倍率乘 _ ^ ^一 -人延伸倍率所得者。於該情形201134992 VI. Description of the Invention: [Technical Field] The present invention relates to a flame-retardant fiber assembly having high flame retardancy and a method of manufacturing the same, and a fiber product by which the flame-retardant fiber assembly is It exhibits extremely high carbonization, form retention, and self-tanning properties when burned, and can be suitably used for a highly resistant flame retardant fiber product used for bedding or furniture. [Prior Art] In recent years, the demand for ensuring the safety of clothing, food, and shelter has increased, and the necessity of flame retardant materials is increasing in view of fire prevention. Among them, in particular, in order to prevent the fire in the bed when the person is injured, the necessity of imparting flame retardancy to the raw materials used for bedding or furniture is increasing. In the fabrics such as beddings or furniture, in order to achieve comfort or design during use, flammable materials such as cotton or polyester or urethane foams are often used for the interior or surface thereof. . In order to ensure their flame retardancy, it is important to have a high level of flame retardancy against ignition of the flammable material by using suitable flame retardant materials in such products. X, the flame retardant material must also maintain the comfort or design of the products such as bedding or furniture. 4乍 is a flame-retardant fiber raw material using the fiber of one of the smoldering materials. In the past, various flame-retardant fibers and fire-retardant agents have been studied, but they have not yet appeared to make the height of the flame retardant and sleepy. The necessary conditions such as comfort or design required for products such as furniture or furniture are adequately balanced. For example, there is a so-called post-fire protection method for applying a fireproofing agent to a cotton cloth, but there is a problem of uniformity of the adhesion of the fireproofing agent, hardening of the cloth caused by the adhesion, detachment caused by the cleaning of the 152753.doc 201134992, and safety. (2) As a cheap raw material, (4) the fiber is melted into a cloth (4) when it is burned, which will create holes and cannot maintain the structure, but the fire, the furniture used in f furniture, etc., or the urethane (4) bubble body. The words are not sufficient. There are also difficult-to-do fibers containing (iv) atoms, but the behavior at the time of burning is the same as above, and eventually it is not sufficient. The method of obtaining a high flame-retardant modacrylic fiber by adding a trioxide or pentaoxane (tetra) or oxygen domain # to a spinning dope can impart flame retardancy, but has a barrier property against fire or heat. A problem that did not reach a satisfactory level. Among these properties, there is a crosslinked high flame retardant acrylic fiber to which a polymer containing glycidyl methacrylate is added, which is difficult to ignite and satisfies the barrier property against fire or heat (Patent Document). However, when the field is exposed to a strong flame such as a burner fire, there is a case where the fiber itself decomposes and eventually ignites. Further, there is a high flame retardant flame barrier property to which a solid phase flame retardant represented by water glass or zinc oxide is added. Improved acrylic fiber (Patent Document 2), but there are cases where the fibers have excellent fire-extinguishing properties or flame barrier properties, but the carbonized film formed during burning is hard, depending on the type of furniture or bedding or the shape of the burning portion. When the shrinkage of the fiber is large, stress is applied to the carbonized film during combustion to cause cracks in the carbonized film, or pores are formed in the carbonized film due to a small load. As a method for solving this problem, it is proposed to borrow An improved acrylic fiber which is difficult to produce cracks by controlling the carbonization rate at the time of shrinkage by adding an oxidized word and a condensed phosphate compound (Patent Document 152753.doc) 201134992 3), but when using these fibers, there are problems with non-complex and limited types of fibers, and limited fiber mixing. '彳', the law is not difficult to burn, but also borrowed A method for producing an acrylic synthetic fiber having excellent heat shrinkage resistance is obtained by performing a moist heat stress treatment (Patent Document 4). However, there is a problem in that the heat shrinkage is prevented in a state of tension, so that the residual shrinkage cannot be sufficiently removed. Although the stress can suppress the shrinkage at a relatively low temperature of 16 〇C, it shrinks remarkably at a high temperature such as 2Gn of the flame, resulting in poor flame retardancy. Moreover, it is necessary for other fibers as a practical fiber product. Mixing is also completely unconsidered. Therefore, it cannot be tolerated as a practical and difficult-to-burn material. It has been proposed to combine the highly flame-retardant (4) fiber and non-flammable fiber with a large amount of flame retardant added. Aggregate (Patent Document 5), and a flame-retardant non-woven fabric composed of a fiber which is inherently flame-retardant and a material-containing fiber Patent Document 6). However, these methods have problems in that the shape before burning such as cloth or fabric cannot be maintained during combustion, and the required flame retardancy, particularly flame barrier properties cannot be ensured; usually heat-resistant fibers or essence Fiber which is incombustible: It is easy to obtain the desired properties, but the fiber itself is mostly hard and brittle, and the operation of the raw material is extremely difficult to operate and manufacture, and the cost is high. [Prior Art Document] [Patent Literature] [Patent Document 1 Japanese Patent Laid-Open Publication No. Hei. No. Hei. No. Hei. No. Hei. No. Hei. No. Hei. No. Hei. [Patent Document 5] Japanese Patent Laid-Open Publication No. SHO-58-156014 [Patent Document 5] Japanese Patent Laid-Open Publication No. SHO 61-89339 [Patent Document 6] US Patent No. 7,259,117 [Invention] [Problems to be Solved by the Invention] In order to solve the above problems, the present invention provides a flame-retardant fiber assembly which satisfies a high flame retardancy and a flame barrier property, a method for producing the same, and a fiber product. [Technical means for solving the problem] The flame-retardant fiber assembly of the present invention contains a dentate-containing fiber, a poly-branded fiber, and a flame-retardant fiber other than the dentate-containing fiber. When the total amount of the above flame-retardant fiber aggregate is 100% by mass, the content of the halogen-containing fiber is 3 to 30% by mass, and the content of the polyester-based fiber is 2 Å to 5 Å by mass. Further, the content of the flame retardant fiber other than the halogen-containing fiber is from 3 to 77% by mass. The dentate-containing fiber is characterized in that it contains acrylonitrile 3〇~7〇 mass/〇3 halogen vinylidene monomer and/or halogen-containing vinyl monomer 7〇30% by mass, and can be co-operated with The polymer (1) having a total amount of 100% by mass of the polymerized vinyl monomer 〇1 to 1% by mass, and at least one metallization port for promoting the decoking reaction at the time of combustion of the polymer (1) and the carbonization reaction at the time of combustion The object (2), and under a load of 0.0054 mN/dtex, the shrinkage change when the temperature is increased from the thief to 300 t is 65% or less. The method for producing a flame-retardant fiber assembly according to the present invention is characterized in that the flame-retardant fiber assembly system comprises a non-flammable fiber containing a sulphide fiber, a polyester fiber, and a 152753.doc 201134992 fiber; The manufacturing method includes the step of setting the total amount of the above-mentioned flame retardant fiber aggregate to 100 mass. /. In the case of 3 to 30% by mass of the above-mentioned dentate-containing fibers, 20 to 50% by mass of the above-mentioned polyester fibers, and 30 to 77% by mass of the flame-retardant fibers other than the halogen-containing fibers; The fiber has a shrinkage variation of 55% or less at a load of 0.0054 mN/dtex from 3 ° C to 3 ° C; the halogen-containing fiber is made to contain a mass of 3 〇 to 70 of acrylonitrile. %, the content of the halogenated vinyl monomer and/or the halogen-containing vinyl monomer 7〇~3〇0/〇, and the copolymerizable vinyl monomer 〇~1〇% by mass Polymer of 1% by mass of polymer (1) 'after spinning with a composition of at least a metal compound (2) which promotes a dehalogenation reaction during combustion of the above polymer (1) and a carbonization reaction during combustion 'Achieved by heat treatment. The fibrous product of the present invention is characterized by comprising the above-mentioned flame retardant fiber assembly. [Effect of the Invention] According to the present invention, a fiber product having high flame retardancy and high flame barrier property can be obtained. [Embodiment] The inventors of the present invention have made intensive studies to solve the above problems, and as a result, they have been prepared to contain γ-containing fibers, poly-S-fibers, and dentate-containing fibers, and non-flammable fibers. The flame-retardant fiber assembly exhibits a high degree of flame retardance. The above-mentioned 3 halogen fibers contain 30 to 70 masses of acrylonitrile. /〇, halogen-containing divinyl monomer and/or hydroxyl-containing vinyl monomer 7. ~30 quality. /. And the total amount of the copolymerized vinyl monomer 〇~1〇 mass% ι 152 152753.doc 201134992 % by weight of the polymer (1), and promote the above polymer (1) At least the metal compound (2) in the decoupling reaction during combustion and the carbonization reaction during combustion, and the shrinkage change when the temperature is increased from 5〇t to 3〇〇t under a load of 0.0054 mN/dtex is 65% The present invention is completed as follows ((halogen-containing fiber). In the present invention, the halogen-containing fiber contains the polymer (1), at least a denture reaction for promoting combustion of the polymer (1), and at least carbonization reaction upon combustion. 1 metal compound (2). The above polymer 〇) comprises acrylonitrile 3〇~7〇 mass 4, halogen-containing vinylidene monomer and/or halogen-containing vinyl monomer 〜3〇 mass/. The copolymerized vinyl monomer 〇 丨〇 丨〇 丨〇 mass %, the total amount is 100% by mass. Further, the above polymer (1) preferably contains acrylonitrile 4 〇 to 65 mass%. 60% to 35% by mass of the base monomer and/or the dentate-containing vinyl monomer, and A may be copolymerized with the vinyl group In the above polymer (1), if the acrylonitrile content is 4 g to 65% by mass, the heat resistance necessary for the fiberization can be easily obtained, and the flame retardation can be achieved. More preferably, the acrylonitrile content is 5 G to (4)% by weight, and if it is in this range, the color of the fiber becomes less. As the above polymer (1), for example, acrylonitrile-diene gas (ene, acrylonitrile) is exemplified. a copolymer of one or more kinds of monomers containing succinylethylene and other monomers, such as a second gas, a second ethylene, or a acetonitrile; a dentate containing ethylene, a vinylidene fluoride or a vinylidene fluoride a copolymer of a vinylidene monomer, a acrylonitrile, and a copolymerizable ethylene monomer, but not limited to these. The above copolymer is appropriately mixed and used as 152753.doc 201134992 as the above-mentioned ethylene-based monomer copolymerizable with the above, and examples thereof include acrylic acid and its ester, methacrylic acid and its ester, acrylamide, and methamine. Acrylic amine, ethyl acetate 6, vinyl (tetra) and its salts, methyl propyl i acid and its salts, styrene And a salt thereof, 2, (tetra) decylamine 2 - methyl phthalic acid, a salt thereof, etc., may be used in the above-mentioned species or in a mixture of two or more. In addition, at least one of them is a compound containing a vinyl group-containing monomer. The copolymer (1) can be obtained by a known polymerization method. For example, examples of the polymerization method include bulk polymerization, m-type polymerization, emulsion polymerization, > Examples of the polymerization form include a continuous form, a batch type, and a half batch type, but are not limited thereto. Among them, from the industrial viewpoint, as a polymerization method, emulsion polymerization and solution polymerization are preferred, and the polymerization form is used. 'Let's preferably a continuous type and a half batch type. As the at least one metal compound (2) which promotes the decoupling reaction at the time of combustion of the polymer (1) and the carbonization reaction at the time of combustion, a dehalogenation reaction can be used. The two reactions of the carbonization reaction are selected from the group consisting of oxidation, zinc carbonate, zinc sulfide, zinc borate, zinc stannate, metastannic acid, tungsten oxide, zirconium oxide, tin oxide, copper oxide, copper phosphate, indium trioxide, barium titanate. a metal compound in zinc p-toluenesulfonate ( 2-i) 'or the above metal compound (2-1) is selected from the group consisting of ruthenium compound, iron oxide, iron phosphate, iron oxalate, iron sulfide, oxidized ruthenium, antimony trioxide, osmium oxide, iodine The metal compound (2-2) in copper is used in combination. The present inventors believe that the above-mentioned metal compound (2-1) promotes the de-tonation reaction at the time of combustion of the polymer (1), and promotes the formation of polyene which is a precursor of 152753.doc 201134992 before the carbonization reaction at the time of combustion, and further The metal complex formed by the de-toothing promotes carbonization by exerting a catalytic action on the multi-dilute structure. As the metal compound (2 1)', in order to promote subsequent carbonization, it is preferred to react the degumming reaction to a compound which is produced at 200 C or less. More preferably, it is at least one selected from the group consisting of oxidized words, zinc stannate, zinc carbonate, and tin oxide. The above-mentioned metal compound (2-1) may be used alone or in combination of two or more kinds, and the above metal compound (2_j) may be selected from the group consisting of iron oxide, iron phosphate, iron oxalate, iron sulfide, The metal compound (2_2) which is used for the dehalogenation reaction in the combustion of the polymer (1) in the molybdenum oxide, the trioxide secret, the osmium oxide, and the Wei steel is used in combination. The metal compound (2_2) which promotes the dehalogenation reaction of the polymer promotes the formation of a polyene which is a precursor of the carbonization reaction by promoting the dehalogenation reaction of the polymer (1), but on the other hand, since it does not have both promotion The ability to carbonize the resulting polyene structure is not effective for the individual use of the metal compound (2-2). As the metal compound (2-2), a ruthenium compound is particularly preferable. The ruthenium compound not only promotes the de-energization of the combustion of the polymer (1), but also the dentate formed by the de-tooth formation forms a gas in a wide temperature region at the time of combustion, and the gas functions to capture the radicals and suppress the combustion, that is, Fire extinguishing performance. Examples of the ruthenium compound include ruthenium oxide compounds such as antimony trioxide, osmium tetroxide, and antimony pentoxide; ruthenium acid or a salt thereof; and an inorganic ruthenium compound such as ruthenium oxide, but are not limited thereto. Also, these combinations can be used. Among them, in terms of performance and industrial availability, it is preferred to be a trioxide recording and a pentoxide recording. The amount of the metal compound (2) is preferably 152753.doc -10- 201134992, and is preferably 0.05 to 50 parts by mass based on 100 parts by mass of the above polymer (1). The lower limit value is more preferably "quality": and further preferably 1 part by mass. Further, regarding the upper limit value, it is more preferably 40 mass damage, and more preferably 30 mass parts. When the amount of the metal compound (7) used is (4) 5 to 50 parts by mass 'the effect of carbonizing the polymer upon combustion (carbonization effect), the carbonization effect necessary for obtaining the desired high flame retardancy can be obtained, and the desired The shrinkage rate. If it is a preferred range, the above effect becomes higher. The amount of the metal compound added is preferably G.G5 to 5G parts by mass based on 1 part by mass of the polymer (1). The lower limit value is more preferably 〇1 mass damage and further preferably 1 part by mass. Further, the upper limit value is more preferably a mass damage' and more preferably 3 parts by mass. When the amount of the metal compound (2_i) used is 0.05 50 parts by weight, the effect of carbonizing the polymer at the time of combustion (carbonization effect) can be obtained, and the stone anaging effect necessary for obtaining the desired high flame retardancy can be obtained. And obtain the desired shrinkage. If it is a preferable range, the above effect becomes higher. The amount of the metal compound added is 0 to 50 parts by mass, preferably 3 to 4 parts by mass, more preferably 5 to 3 parts by mass, based on 100 parts by mass of the above polymer (丨). There is also a case where the required flame retardancy can be achieved even for the mass fraction, but the self-extinguishing effect is small, so when used for applications requiring a higher self-extinguishing effect, it is preferable to add 3 parts by mass or more. Below the mass. The average particle diameter of the metal compound (2) is preferably 3 μm or less, more preferably 2 μm or less. When the average particle diameter of the metal compound (2) is 3 μm or less, the failure of the nozzle, such as nozzle clogging, in the manufacturing step of the fiber in which the metal compound component is added to the _-containing polymer is 152753.doc • 11- 201134992 degree increase, metal compound component particles in fiber =: gold: the lower limit of the average particle size of compound (7) is not special: : in terms of sex 2, 'preferably-upper, better 1 incense The above metal compound (7) may be chemically modified to improve the agglomeration property, and may be used in a state of being dispersed in water or an organic solvent. Here, the so-called average (four) refers to the middle diameter. As a method of measuring the median diameter, a light scattering method can be used. The above-mentioned fiber-containing fiber is preferably contained in an amount of from 0.1 to 20 parts by mass based on 100 parts by mass of the polymer (1). The crosslinking of the fibers can be further suppressed by forming a polymer crosslinked structure in the fibers by using the epoxy group-containing compound and crosslinking by heat or heat in the fiber production step. The epoxy group-containing compound may be, for example, a glycidyl (tetra) type, a glycidylamine type, a glycidyl group, a cyclic aliphatic type, or a copolymer containing the epoxy group-containing compound. . When considering the amount of the reaction group (epoxy group) per unit weight of the dissolution in the spinning, the glycidyl ester is preferably used, for example, polyglycidyl methacrylate (the weight average molecular weight is 3000~100000). Further, the above-mentioned dentate-containing fibers may contain other additives such as an antistatic agent, a thermal coloring inhibitor, a light resistance improving agent, a whiteness improving agent, a devitrification preventing agent, a coloring agent, and a flame retardant. The above-mentioned halogen-containing fiber has a shrinkage variation of 65 °/ when the temperature is raised from 50 C to 300 ° C under a load of 0.0054 mN/dtex. the following. In the above, the so-called shrinkage change from 50 ° C to 30 ° t 152753.doc 12 · 201134992 movement, refers to the highest and lowest point of shrinkage in the temperature range of 5 (TC to 300 ° C) The difference is necessary to be a value above 〇. If it is expressed in the diagram of the present invention, for example, it corresponds to the circle shown in the arrows in Figs. 9 to 丨5. The following: For example, as shown in FIG. 9 or FIG. 11, when the temperature is monotonously contracted as the temperature rises, the contraction fluctuation becomes the contraction rate of the point 乂^(10)^^. As shown in the figure, when it is stretched once after shrinking and contracted again, according to the elongation at the time of one-degree elongation, in Fig. 12, the contraction fluctuation becomes the contraction rate of point c, and in Fig. 13, the contraction fluctuation becomes a contraction of 1 point. In FIGS. 14 and 15, the shrinkage fluctuation is the difference between the shrinkage ratio of the point 1) and the shrinkage ratio of b and the point. 3. As shown in Fig. 10, when it is monotonously stretched or stretched after shrinking and is broken midway, the shrinkage fluctuation becomes the shrinkage ratio indicated by the arrow (when the elongation is interrupted, the shrinkage fluctuation is 〇〇). 4. Point a in the figure is the softening start point. Between 3 o'clock and b o'clock, shrinkage caused by stress relaxation, shrinkage caused by decogging, and "stretching" caused by softening are superior to elongation. In the future, the shrinkage caused by the de-salt, the shrinkage due to carbonization (shape retention), and the "elongation" caused by softening form the following pattern: (1) When the carbonization ability is excellent, the shrinkage (or shape retention) is won. Over-extension 'forms a shrink pattern as shown in Figure 9 or Figure 11; elongation is superior at point b, at a certain point (b' point in the figure) and (2) when the stone reversal ability is still poor, the potential 'follows The temperature rises and the carbonization is in the dominance and begins to shrink (Fig. 12, 13, 14, 15); 152753.doc 201134992 (3) In the case of no carbonization ability _, after b point, the elongation is in an advantage, forming the shrink pattern of Fig. 10. . 5. There are four types of shrinkage patterns of the above halogen-containing fibers (Fig. 9, Fig. 12, Fig. 13, Fig. 14). The shrinkage pattern of the above halogen-containing fiber is preferably as shown in Fig. 9, followed by Fig. 12, and then Fig. 13 and Fig. 14. It can be a shrinkage caused by stress relaxation as shown in FIG. 9 and a shrinkage caused by the decoupling, and the carbonization ability is $, and the shrinkage pattern of the monotonic shrinkage is optimal, and the carbonization ability can be as shown in FIGS. 12, 13, and 14. Poor, even if it is stretched by softening before carbonization, it will shrink and shrink (shape maintain) at a certain temperature. More preferably, in the figure, b, the shrinkage ratio of the dots is G%, and the above-mentioned (four) fibers are carbonized at a load of 0.0054 mN/dtex from a temperature of 5 〇 β (: 3 〇 η: In the present invention, the above-mentioned element-containing fiber is increased in temperature from 5 〇〇 c to 3 〇〇 β under a load of 0.0054 mN/dtex (when it is carbonized, and remains without being cut, The above-mentioned dentate-containing fiber is used when the temperature is reduced from 5 (TC to 30 (rc) under the load of 〇〇〇54 mN/dtex, and the fiber shrinkage ratio is measured by the following method for measuring the fiber shrinkage ratio. 6. It is not cut off. 6. In contrast, 'Fig. 1 〇, Fig. ! i, Fig. j 5 shows the contraction fluctuation when the contraction fluctuation exceeds the %. In Fig. 10, if the temperature is increased, the elasticity is lost or cut off. In Fig. 11, 'the carbonization ability is excellent, (4) the temperature rises and monotonously shrinks, but the shrinkage caused by the stress relaxation (a to b points in the figure) is too large, and the shrinkage fluctuation of the temperature from 50 C to 300 ° C is exceeded. 65%. Figure 15 is the same shrinking pattern as Figures 12 and 13, but the carbonization ability is weak and the elongation is excellent. , shrinkage variation (difference between shrinkage rate at point b and shrinkage at b' point) exceeds 152753.doc •14·201134992 65% 〇The above halogen-containing fiber preferably has a single fiber strength of 〇5 to 16 cN/dtex, Preferably, it is 0.5M.1 cN/dtex. Among the above-mentioned dentate fibers, the load τ of 二54 2 N/dtex increases the temperature from thief to Cao c, and the shrinkage change easily becomes 65% or less, which is higher. In the present invention, the strength of the single fiber is measured in accordance with JIS L 1 015. The above-mentioned i-containing fiber may be a short fiber or a long fiber, and may be appropriately selected in a method of use. Suitablely selected according to the use of the flame-retardant fiber assembly and the fiber product, preferably W~5, for example, more preferably 15~3〇dtex', and even more preferably L7~15 dtexe cutting length can be based on the flame-retardant fiber assembly and The use of the fibrous product is appropriately selected, for example, a chopped fiber (fiber length of 0.1 to 5 mm) or a short fiber (fiber length "~丨" claw (4), or a completely uncut long fiber (filament). It is preferably a short fiber of about 3 (four) sides of the fiber length ... which can be used in combination with The fiber has the same fineness and may be finer or wider. The flame retardant mechanism of the above halogen-containing fiber will be described. (1) Regarding the metal compound (2-1) as the metal compound (2-1) 'For example, zinc oxide is generally used. It is considered that zinc oxide has an effect of promoting the de-toothing reaction of the dentate-containing fibers. Further, the inventors of the present invention believe that the zinc hydride formed by dehydrogenation and (10) hydrogenation of hydrogen (in the case of gas, gasification) (ZnCl2)) not only promotes carbonization by exerting a catalytic action on a multi-thin structure (the residue at the time of combustion becomes a form-retaining component), but also contributes to the formation of a three-till ring of acrylonitrile (the fiber shrinks by cyclization) The effect can be exhibited not only by zinc oxide, but also by other organic chemicals such as zinc, zinc octylate or zinc octoate, or a part of metal oxides such as tin oxide or copper oxide. Further, the carbide generated as a result of the carbonization and cyclization promoting action by the metal compound (2·1) is strong, and the residue, particularly the residue which retains the fiber form, can be present. When the fire is brought into contact with a composite such as cloth or non-woven fabric in which the residue at the time of heating, particularly the fiber remaining in the form of fibers, remains, the flame can be blocked by the residue. (2) The shrinkage fluctuation when the temperature is increased from 5 〇t to 300 °C under a load of 0.0054 mN/dtex is 65% or less. Normally, the halogen-containing fiber temporarily shrinks upon heating (combustion), and thereafter exhibits Extended behavior. As a factor of shrinkage during heating (combustion), two factors are considered: a. shrinkage caused by carbonization, b. shrinkage caused by residual residual stress. Its t, a. shrinkage caused by carbonization is caused by the decoupling reaction from the copolymer and the formation of the three-pill ring of acrylonitrile. It is derived from a chemical reaction of a copolymer composition, and it is difficult to suppress shrinkage caused by the reaction. On the other hand, the shrinkage caused by the residual shrinkage stress of the spinning is caused by the residual strain imparted to the fiber during the solidification or stretching operation in the fiber manufacturing process', by appropriately selecting the manufacturing conditions of the fiber, particularly the heat treatment in the fiber manufacturing process. Conditional inhibition. Examples of the heat treatment method include a relaxation heat treatment, a moist heat of 15 Torr or more, and a dry heat 180.紧张 The above heat treatment. Among them, as a heat treatment method for sufficiently suppressing the spinning residual stress, it is preferred to heat-treat. By performing these heat treatments, the spinning residual shrinkage stress can be suppressed, and the shrinkage during heating (combustion) can be varied, that is, the shrinkage fluctuation when the temperature is raised from 50 C to 300 ° C under a load of 0.0054 mN/dtex. For 152753.doc -16· 201134992, the temperature from 50 °C is higher than 65%. If the load is at 0.0054 mN/dtex and the shrinkage variation is less than 35% at 300 °C, the flame retardance of the flammability 'height. For example, in the United States bed burning test 16CFR1633 'because there is no such failure in the test, the fiber shrinkage is suppressed, the hole is exposed in the flame exposed portion, or the strain is generated. Cracked, the flame enters from there, and the internal flammable structure catches fire. In terms of exhibiting higher flame retardancy, the higher the flame barrier property, the temperature is increased from 50 ° C to 30 under the load of 0.0054 mN / dtex (the change in I at TC is preferably 6 〇). % or less, more preferably 50% or less, and particularly preferably 45% or less. Further, the above-mentioned shrinkage fluctuation from 5 (rc to 3〇〇r) is preferably as much as possible under a load of 0.0054 mN/dtex. Smaller, the closer to 〇%, the better. Further, it is preferable to increase the temperature from 5 (rc to 3 〇 under a load of 0.0054 mN/dtex (Γ: when carbonized, it remains without being cut off. In the present invention, the softening temperature of the above-mentioned element-containing fiber is close to the dehalogenation starting temperature (decomposition point). Therefore, if the heat treatment temperature is increased, the fiber is colored due to the occurrence of the de-reaction, or it is difficult to impart sufficient heat treatment. As a countermeasure against this, there is a method of lowering the softening point by lowering the acrylonitrile content of the dentate-containing fibers, whereby the heat treatment temperature can be set to be lower than the decomposition temperature, and at the softening point under the conditions of pressurized hot and humid heat. A sufficient heat treatment can be performed below the temperature. (3) About The shrinkage inhibition mechanism of the epoxy group-containing polymer (for example, polyglycidyl methacrylate (pGMA)) causes pGMA to react in the spinning process, and introduces a polymer crosslinked structure into the fiber, thereby suppressing shrinkage. The present inventors believe that the pGMA system 152753.doc •17·201134992 is crosslinked by heat of drying or heat treatment, and further crosslinking can be carried out as long as an acid catalyst is present. The inventors believe that the above The metal oxide (sb2〇3, zinc oxide (Zn〇)) contained in the dentate fiber captures the i element in the polymer contained in the fiber to form an autograft (in the case of gas) Forming SbClrZnCl2), which acts as an acid catalyst to promote cross-linking of {)(}1^8. The above-mentioned element-containing fiber can be obtained by containing acrylonitrile containing 3〇7〇% by mass of alizarin-containing vinylene. The base monomer and/or the dentate-containing vinyl monomer 7〇3 to 3% by mass, and the polymer (1) which can be copolymerized with the ethylene-based monomer 〇~1〇% by mass and promote At least one metal compound (2) of the carbonization reaction during the combustion and the carbonization reaction at the time of combustion The compound is produced by heat treatment after being spun, and specifically, it can be produced by a known method such as a wet spinning method, a dry spinning method, or a semi-dry semi-wet method. For example, in a wet spinning method. By dissolving the above polymer in a mixture of dimethyl dimethyl carbamide, n, n dimethyl acetamide, propyl hydrazine, aqueous thiocyanate, dimethyl sulfite, aqueous solution of succinic acid, etc. After the solvent is passed through a nozzle, it is extruded into a coagulation bath to be solidified, and then subjected to stretching, water washing, drying, heat treatment, and if necessary, a crimping and cutting is performed to obtain a product. The solvent is preferably two. Methylformamide, N,N-dimethyletheneamine, acetone', n,n-dimethylformamide, and acetone are preferred because they can be industrially handled. In addition, if the load τ at 0·0054 mN/dtex increases the temperature from scratch to a range of 65% or less at 3 〇〇C, it can be extended after spinning and before heat treatment. That is, the production of the above-mentioned N-containing fiber can be carried out by extruding (spun) a spinning solution containing the above composition, performing a 152753.doc 201134992 2 water washing, followed by drying, and performing secondary stretching, and Implementation of the implementation of the order. In the present invention, the term "secondary extension" means elongation in the fiber production step (spinning step) after spinning and until drying, and the so-called secondary stretching means self-drying, and: operating. Further, the primary stretching may be carried out in any step as long as it is before the drying step. For example, it may be carried out before water washing, one side = one side, water purely, or continuously washed from a water washing towel. In the production of the above-mentioned element-containing fiber, the stretching ratio multiplied by the relaxation ratio is determined to be 5 times or less, more preferably 4.8 times or less, and particularly preferably 3.7 times or less. Thereby, the spinning residual shrinkage stress can be further suppressed to obtain higher flame retardancy. Further, the total stretching ratio is preferably (M times ±, more preferably! 〇 times 1). In the present invention, the term "stretching magnification" means fibers in the fiber manufacturing step (spinning step) before heat treatment. The ratio of elongation is long. The spinning step before the above heat treatment includes, for example, a solidification step (extrusion of the spinning solution), a water washing step (including the case where the surface is extended while the surface is washed), a drying step, an extension step, and the like. For the treatment of the length of the fiber, for example, when the thread (fiber bundle) is moved between two parents, the stretching ratio is 1 () times if the speed of the human side roller is the same as the speed of the exit side. ^The treatment is performed when the length of the fiber is three times. For example, when the yarn (fiber bundle) is moved between the two rolls, the stretching ratio becomes 3 when the exit side roller speed is three times the speed of the inlet side roller. The above stretching ratio is not particularly limited, and the performance of the fiber and the fiber strength are exhibited, and the temperature of 152753.doc •19·201134992 is increased from 5〇C to 3〇〇 under a load of 0.0054 mN/dtex. Wide d* back to 3〇〇C The contraction variation is set to (10) in the following, preferably 1. 〇~10 〇 times 〇^ and as the above-mentioned extended 俾 夕 π π limit, more preferably 2.0 times... Under the evaluation of the sheep under the sheep | ·〇倍' as the upper limit value, more preferably 9.0 9.0 times, especially 8.0 times. For the middle Μ, early, f material a ”,, before the treatment, a plurality of spinning steps 2 are given plural: the situation of human extension When the stretching ratio of the present invention is multiplied by the stretching ratio of each extension 2, for example, as described above, in the case of Qiu Ben, 仃-person extension and secondary extension, the stretching ratio is the primary stretching ratio. Multiply _ ^ ^ one - the person who stretched the magnification. In this case

時,若延伸倍率相同,貞彳& # A 只J敉佳為相比二次延伸,一次延伸 之作用較大。作為進而舫社 & 退而杈佳之態樣,可列舉僅以一次延伸 進行延伸的態樣。並且,一 -人延伸倍率較佳為8倍以下, 更佳為6倍以下,尤佳A <;拉 :"、σ 下。又,二次延伸倍率較佳 為3倍以下’更佳為1.5倍以下。 又’於本發明中,所謂緩和倍率,係指於上述熱處理步 驟中纖維收縮之比例。具體而言,係指於纖維製造步驟 (纺絲步驟)中之熱處理步驟’例如包括凝固步驟(纺絲液之 擠出)、水洗步驟(亦包括一面水洗一面延伸之情形)、乾燥 步驟、延伸步料之處理㈣後料行的減理步驟中, 使纖維長收縮之比例。例如於賦予纖維長不變之熱處理之 情形時’緩和倍率為Κ0倍,於賦^纖維長成為·之熱處 理之情形時,緩和倍率為〇·5倍。作為上述緩和倍率,並 .”、特別限定,就使於〇.0〇54 mN/dtex之荷重下將溫度自 5〇°C提高至30(TC時之收縮變動為65%以下之方面而言, 較佳為G.3〜1.〇倍。並且’作為上述緩和倍率之下限值,更 152753.doc •20· 201134992 佳為0.4倍,尤佳為〇·5倍,作為上限值,更佳為〇 9倍尤 佳為0.8 5倍。 本發明之熱處理有鬆弛熱處理與緊張熱處理。本發明中 所明之鬆弛熱處理,係指以下狀態下之熱處理:例如若假 定當絲線(纖維束)於2個輥間移動時賦予熱處理,則於纖維 不收縮之溫度條件下將2個輥設為相同旋轉速度之情形時 於輥間移動時之絲線之狀態(定長狀態)、或者移動之絲線 相比於此更鬆弛之狀態(鬆弛狀態)。再者,於藉由熱處理 而使纖維於2個輥間收縮之情形時,只要施加於纖維之張 力與上述狀態為相同水準,則亦成為鬆弛熱處理。又本 發明中所謂之緊張熱處理,係指以下狀態下之熱處理:上 述鬆弛熱處理中之絲線之狀態以外之狀態,例如於纖維不 收縮之溫度條件下將2個輥設為相同旋轉速度之情形時, 超出在輥間移動時之絲線之狀態(定長狀態),而施加於纖 維之張力更大之狀態(緊張狀態)。再者,於藉由熱處理而 使纖維於2個輥間收縮之情形時,只要施加於纖維之張力 與上述狀態為相同水準,則亦成為緊張熱處理。並且,於 不使用輥之情形時,若為與鬆弛熱處理中之絲線之狀態同 等之張力狀態下之熱處理,則亦成為鬆弛熱處理,若為與 緊張熱處理中之絲線之狀態同等之張力狀態下之熱處理, 則成為緊張熱處理。 作為上述熱處理方法,可為作為—般之熱處理方法的乾 熱處理法、濕熱處理法中之任一方法。所謂本發明中之濕 熱處理,係定義為含有水蒸氣之環境(濕潤空氣)中的加熱 152753.doc -21· 201134992 狀態之處理。上述環境為相# 為相對濕度30%以上,較佳為相對 濕度㈣以上,進而較佳為相對濕度7〇%以上尤佳為相 對濕度麵(飽和水蒸氣條件)。相對濕度越高,收縮變動 率或纖維白度等越良好。進而作為濕熱處理法,可列舉加 熱水蒸氣處理法、滿熱加壓蒸氣處理法,但並不限定於 此。進而,於進行渴埶Λ厭 > 、 …加壓蒸軋處理法之情形時,作為賦 予漁熱之態樣’並益特別irp 6 …、将別限疋,例如可列舉於放入有絲線 之裝置内投入蒸氣之方法、於放入有絲線之裝置内投入蒸 氣而形成飽和水蒸氣條件之方法、於放入有絲線之裝置中 投入由=外設置之熱風製造機(加熱器)所產生之熱風並且 投入蒸礼,方法等。作為熱處理時之纖維。絲線)之張力狀 態可為鬆^、緊張中之任_狀態。再者,此處所謂㈣ 二處=疋長狀態。作為該等之組合’可列舉:乾熱緊 張熱處理法、乾熱鬆他轨虚 菘弛熱處理法、加熱水蒸氣緊張熱處理 法、加熱水蒸氣鬆他熱處理法、濕熱加壓蒸氣緊張熱處理 法、濕熱加壓蒸氣鬆他熱處理法,較佳為乾熱鬆他孰處理 法、加熱水蒸氣鬆他熱處理法、濕熱加厂堅蒸氣鬆他熱處理 =進而較佳為乾熱鬆弛熱處理法、濕熱加壓蒸氣鬆他熱 理法。又’亦可將該等方法或纖維之纖維(絲線)之張力 狀態組合複數種而形成熱處理步驟。 通常’於含齒素纖維之熱處理中,處理溫度越高,越可 降低訪絲殘留收縮應力,尤其於進行濕熱處理,進而於濕 熱加麼蒸氣中進行處理之情形時,即便熱處理所必需之熱 為含函素纖維之軟化溫度或分解溫度以下亦可傳遞至纖維 152753.doc -22· 201134992 内部,因此可於著色或強度不降低 處理。上述埶處理可充为之熱 處1了㈣續式或批次式處理進行。尤其於 使用丙埽腈超出5〇質量%; > p老 之八聚物之情形時,較佳為加埶 水蒸乳處理法、濕熱加遷蒸氣… ^ -i- 〇/ LV -r -V xx . 於便用丙烯腈為50 。 ,、聚物之情形時,較佳為乾熱處理法、渴埶 加壓蒸氣處理法。j:k因力 ........ 因在於,任一種纖維之著色均較 ^關於熱處理溫度,於進行鬆他熱處理之情 乾熱處理法,則為⑽〜較佳為⑽〜⑽。C’進而車t 佳為150〜170°C ,甚良、持私丄r- 右為濕熱加壓蒸氣處理法,則為 8〇〜⑽。c,較佳為90〜15〇t,進而較佳為_〜崎若 為加熱水蒸氣處理法,則為14〇〜23〇t ,較佳為 150〜2UTC,進而較佳為勝19代。於進行緊張熱處理之 情形時’若為乾熱處理法’則為18〇〜26〇。。,較佳為 180〜24()t:,若為濕熱加壓蒸氣處理法,則為150〜23(TC, 較佳為160〜210 C ,若為加熱水蒸氣處理法則為 160〜250 C,較佳為17〇〜22(rc。熱處理溫度之上限並無特 別限定,就上述含函素纖維之著色及工業之觀點而言,為 300 C,較佳為250°C,進而較佳為22〇°C。 作為上述熱處理,較佳為鬆弛熱處理、1 8CTC以上之乾 熱緊張熱處理或者15〇eC以上之濕熱緊張熱處理。可容易 獲得於0.0054 mN/dtex之荷重下將溫度自5〇〇c提高至3〇〇〇c 時之收I®變動為6 5 %以下的含鹵素纖維。又,作為熱處 理,更佳為鬆弛熱處理,尤佳為於9〇〜丨5〇艽之濕熱中進行 鬆弛熱處理❶再者,本發明中所謂之熱處理,係指於加熱 152753.doc •23· 201134992 下使纖維收縮,減輕、去除紡絲收縮應力。 (聚酯系纖維) 於本發明中,所謂聚酯系纖維,係指依據JIS L丨〇9丨Ε 法之氧指數法試驗所測定之氧指數(以下稱作L〇I值)為23 以下的聚酯纖維。例如亦包括:包含聚對苯二甲酸乙二 s曰、聚對笨二曱酸丁二酯、聚萘二甲酸乙二酯、聚萘二甲 酸丁二酯、聚對苯二曱酸丙二酯等之纖維;或藉由複合紡 絲法等,將該等聚酯成分與熔點不同之成分例如聚丙烯或 聚乙烯等加以混合,並纖維化成一根的低熔點黏合劑.聚酯 系纖維等》 (含鹵素纖維以外之難燃性纖維) 於本發明中,作為含豳素纖維以外之難燃性纖維,只要 為上述含齒素纖維以外之具有難燃性之纖維即可,例如可 使用芳族聚醯胺纖維、苯甲酸酯纖維、聚苯硫醚纖維、聚 醚醚酮纖維、聚醯亞胺纖維、聚醯胺醯亞胺纖維、難燃聚 酉曰纖維、三聚氰胺纖維、丙烯酸酯纖維、聚苯氧化物 (P〇lybenzoxide)纖維、聚氣乙烯纖維、聚偏二氣乙浠纖 維、聚氣乙烯醇纖維、聚四氟乙烯纖維、包括含有無機化 合物之再生纖維素纖維或含有磷系難燃劑之再生纖維素纖 維等的再生纖維素纖維、塗布有難燃劑之後加工難燃纖維 素纖維、氧化丙烯酸纖維、碳纖維、玻璃纖維、活性碳纖 ,,隹等。可適且使用LOI值為25以上之纖維。上述之争,上 述含有無機化合物之再生纖維素纖維中之無機化合物較佳 為矽成分。又’關於上述含有無機化合物之再生纖維素纖 I52753.doc -24· 201134992 ’准中之無機化合物的含量,當將總量設為刚質量 二值較佳紅5質量%,更佳為3質量%,進而更佳為4: 罝。尤佳為6質量%,上限值較佳為32質量%,更佳 27質量❶/。’進而更佳為22質量%,尤佳為“質量%。上述 之中:無機化合物之含量係以無機化合物之含有元素量 (質量%)所表示,於無機化合物為矽成分之情形時,係护 石夕元素之含量。又’關於含㈣成分之再生纖維素纖維中日 之石夕成分的含量㈣元素之含量,下限值較佳為丨$質量 %’更佳為3質量% ’進而更佳為以質量% ’尤佳^質量 %,上限值較佳為32質量%,更佳為27質量%,進而更佳 為22質量%’尤佳為16質量%。又’上述之中,所謂難燃 聚酯纖維,係指L0I值為26以上之聚酯纖維,亦包括含有 難燃劑之纖維或聚芳酯纖維等。 其中,就難燃性表現或隔熱性、成本、難燃纖維集合體 之質感等觀點而言,較佳為含有矽成分或磷系難燃劑等之 再生纖維素纖維、塗布有難燃劑之後加工難燃纖維素纖 維、三聚氰胺纖維、難燃聚酯纖維、丙烯酸酯纖維、芳族 聚醯胺纖維,更佳為含有矽成分或磷系難燃劑等之再生纖 維素纖維、塗布有難燃劑之後加工難燃纖維素纖維、芳族 聚醯胺纖維。 作為上述芳族聚醯胺纖維,例如可使用Dup〇nt&司製造 之商品名「Kevlar」、Dupont公司製造之商品名 「Nomex」、帝人公司製造之商品名rTechn〇ra」、帝人公 司製造之商品名「Twaron」、帝人公司製造之商品名 152753.doc • 25· 201134992When the stretching ratio is the same, 贞彳&# A only J is better than the second extension, and the effect of one extension is larger. As a further aspect of the company, it is preferable to extend the aspect only by one extension. Further, the one-person extension ratio is preferably 8 times or less, more preferably 6 times or less, and particularly preferably A <; pull: ", σ. Further, the secondary stretching ratio is preferably 3 times or less', more preferably 1.5 times or less. Further, in the present invention, the relaxation ratio refers to the ratio of fiber shrinkage in the above heat treatment step. Specifically, it means a heat treatment step in the fiber manufacturing step (spinning step), for example, including a solidification step (extrusion of the spinning solution), a water washing step (including a case where one side is washed with one side), a drying step, and an extension. In the treatment step of the step material (4), the ratio of the fiber length shrinkage in the step of reducing the material row. For example, in the case of heat treatment for imparting a fiber length, the relaxation ratio is Κ0 times, and when the fiber length is changed to a heat treatment, the relaxation ratio is 〇·5 times. The above-mentioned relaxation ratio is particularly limited, and the temperature is increased from 5 〇 ° C to 30 under the load of 〇 〇 m 54 mN/dtex (the shrinkage variation at TC is 65% or less). Preferably, it is G.3~1.〇 times, and 'as the lower limit of the above relaxation ratio, more 152753.doc •20·201134992 is preferably 0.4 times, especially preferably 〇·5 times, as the upper limit value, More preferably, it is 9 times and preferably 0.8 times. The heat treatment of the present invention has a relaxation heat treatment and a tension heat treatment. The relaxation heat treatment in the present invention refers to heat treatment in the following state: for example, if a yarn (fiber bundle) is assumed When heat treatment is applied between the two rolls, the state of the wire when moving between the rolls (fixed length state) or the moving wire phase when the two rolls are set to the same rotational speed under the temperature condition in which the fibers are not shrunk In a state where it is more slack than this (relaxed state). Further, when the fiber is shrunk between the two rolls by heat treatment, the tension applied to the fiber is the same level as the above state, and the heat treatment is also relaxed. Also known as the present invention The intense heat treatment refers to a heat treatment in a state other than the state of the yarn in the relaxation heat treatment, for example, when the two rolls are set to the same rotation speed under the temperature condition in which the fibers are not shrunk, the movement between the rolls is exceeded. The state of the wire (the fixed length state) is applied to the state in which the tension of the fiber is greater (tension state). Further, when the fiber is shrunk between the two rolls by heat treatment, it is applied to the fiber as long as it is applied to the fiber. When the tension is the same as the above-mentioned state, the heat treatment is also intense. Further, when the roll is not used, if the heat treatment is the same as the state of the yarn in the relaxation heat treatment, the heat treatment is also performed. The heat treatment in the tension state equivalent to the state of the thread in the heat treatment is a stress heat treatment. The heat treatment method may be any one of a dry heat treatment method and a wet heat treatment method as a general heat treatment method. The wet heat treatment in the present invention is defined as heating in an environment containing water vapor (wet air). 152753.doc -21· 201134992 State treatment. The above environment is phase # is relative humidity of 30% or more, preferably relative humidity (four) or more, and further preferably relative humidity of 7〇% or more, preferably relative humidity surface (saturated water) The vapor content is higher. The higher the relative humidity, the better the shrinkage rate, the fiber whiteness, etc. Further, the wet heat treatment method includes a heating steam treatment method and a full heat pressure steam treatment method, but is not limited thereto. In the case of the thirst irritated >, ...the pressure-steaming treatment method, as the aspect of imparting the heat of the fish, and the special irp 6 ..., it is not limited to, for example, it can be exemplified in the presence of a thread. A method of introducing steam into a device, a method of introducing steam into a device having a wire to form a saturated steam condition, and a device for inserting a wire into a device equipped with a wire to generate a hot air generator (heater) provided outside the wire Hot air and put steaming, methods, etc. As a fiber during heat treatment. The tension state of the thread can be loose or tight. Furthermore, here is the so-called (four) two places = long state. As such a combination, a dry heat stress heat treatment method, a dry heat relaxation rail heat relaxation heat treatment method, a heating water vapor tension heat treatment method, a heating water vapor relaxation heat treatment method, a wet heat pressure steam tension heat treatment method, and a damp heat may be mentioned. Pressurized steam relaxation heat treatment method, preferably dry heat pine treatment method, heating water vapor relaxation heat treatment method, damp heat plus factory steaming heat treatment = further preferably dry heat relaxation heat treatment method, wet heat pressure steam Songta heat method. Further, the method or the tension state of the fibers (filaments) of the fibers may be combined to form a heat treatment step. Generally, in the heat treatment of dentate-containing fibers, the higher the treatment temperature, the lower the residual shrinkage stress of the invisible wire, especially in the case of wet heat treatment, and then in the case of heat treatment plus steam, even if heat required for heat treatment It can also be transferred to the inside of the fiber 152753.doc -22· 201134992 for the softening temperature or decomposition temperature of the fiber containing the element, so that the coloring or strength can be reduced without treatment. The above-mentioned enthalpy treatment can be used as a heat (1) continuation or batch processing. Especially when using acrylonitrile exceeds 5 〇 mass%; > p old octamer, it is preferred to add hydrazine steam treatment, moist heat addition steam... ^ -i- 〇 / LV -r - V xx . Use acrylonitrile for 50. In the case of a polymer, a dry heat treatment method or a thirst pressure steam treatment method is preferred. j:k is due to the force........ Because the color of any of the fibers is higher than the heat treatment temperature, and the heat treatment method for the heat treatment is (10) to preferably (10) to (10). C' and then the car t is preferably 150 to 170 ° C, very good, private 丄 r- right is wet heat pressure steam treatment, then 8 〇 ~ (10). c, preferably 90 to 15 〇t, and more preferably _~ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ In the case of the intense heat treatment, 'if dry heat treatment method' is 18 〇 to 26 〇. . Preferably, it is 180 to 24 () t: if it is a wet heat pressurized steam treatment, it is 150 to 23 (TC, preferably 160 to 210 C, and 160 to 250 C for heating steam treatment, It is preferably 17 〇 22 22 ( rc. The upper limit of the heat treatment temperature is not particularly limited, and is 300 C, preferably 250 ° C, and more preferably 22 in terms of the color of the above-mentioned element-containing fiber and industrial viewpoint.作为 ° C. The heat treatment is preferably a relaxation heat treatment, a dry heat stress heat treatment of 18 CTC or more, or a damp heat stress heat treatment of 15 〇e C or more. It can be easily obtained at a load of 0.0054 mN/dtex and the temperature is from 5 〇〇 c. It is a halogen-containing fiber with a change of I® of 65% or less when it is increased to 3〇〇〇c. Further, as a heat treatment, it is preferably a relaxation heat treatment, and it is preferable to relax in a damp heat of 9〇~丨5〇艽. Heat treatment ❶ In addition, the heat treatment in the present invention means shrinking the fiber under heating 152753.doc •23·201134992 to reduce and remove the spinning shrinkage stress. (Polyester fiber) In the present invention, the so-called polyester Fiber, refers to the oxygen index test according to JIS L丨〇9丨Ε method The measured oxygen index (hereinafter referred to as L〇I value) is a polyester fiber of 23 or less. For example, it also includes: polyethylene terephthalate, polybutylene dibutylate, polynaphthalene a fiber such as ethylene formate, polybutylene naphthalate or propylene terephthalate; or a component different from a melting point such as polypropylene by a composite spinning method or the like; a low-melting adhesive which is mixed with polyethylene and the like and is fiberized into one. Polyester-based fiber or the like (a flame-retardant fiber other than a halogen fiber). In the present invention, it is a flame-retardant fiber other than a halogen-containing fiber. As long as it is a fiber having flame retardancy other than the above-mentioned dentate-containing fiber, for example, an aromatic polyamide fiber, a benzoate fiber, a polyphenylene sulfide fiber, a polyetheretherketone fiber, or a polyfluorene fiber can be used. Amine fiber, polyamidoximine fiber, flame retardant polybenzazole fiber, melamine fiber, acrylate fiber, polyphenylene oxide (P〇lybenzoxide) fiber, polystyrene fiber, poly(ethylene diacetate) fiber, poly Gas vinyl alcohol fiber, polytetrafluoroethylene fiber, including Regenerated cellulose fiber such as regenerated cellulose fiber of inorganic compound or regenerated cellulose fiber containing phosphorus-based flame retardant, processed with flame retardant agent, processed with flame retardant cellulose fiber, oxidized acrylic fiber, carbon fiber, glass fiber, activated carbon fiber , 隹, etc. A fiber having an LOI value of 25 or more may be suitably used. The above-mentioned inorganic compound in the regenerated cellulose fiber containing an inorganic compound is preferably a bismuth component. Plain fiber I52753.doc -24· 201134992 'The content of the inorganic compound in the quasi-quantity, when the total amount is set to be just the mass binary value, preferably red 5% by mass, more preferably 3% by mass, and even more preferably 4: 罝. More preferably, it is 6 mass%, and the upper limit is preferably 32 mass%, more preferably 27 mass%. Further, it is more preferably 22% by mass, and particularly preferably "% by mass. In the above, the content of the inorganic compound is represented by the content of the inorganic compound (% by mass), and when the inorganic compound is a bismuth component, The content of the element of the stone eve, and the content of the element (4) of the regenerated cellulose fiber containing the (four) component, the lower limit is preferably 丨$% by mass, more preferably 3% by mass. More preferably, the mass % is particularly good, and the upper limit is preferably 32% by mass, more preferably 27% by mass, and even more preferably 22% by mass, and particularly preferably 16% by mass. The term "flammable polyester fiber" refers to a polyester fiber having a L0I value of 26 or more, and also includes a fiber containing a flame retardant or a polyarylate fiber, etc. Among them, flame retardancy or heat insulation, cost, and difficulty From the viewpoint of the texture of the fuel fiber assembly, etc., it is preferably a regenerated cellulose fiber containing a bismuth component or a phosphorus-based flame retardant, a processable flame retardant cellulose fiber, a melamine fiber, and a flame-retardant polyester fiber. Acrylate fiber, aromatic poly The amine fiber is more preferably a regenerated cellulose fiber containing a bismuth component or a phosphorus-based flame retardant, or a flame retardant cellulose fiber or an aromatic polyamide fiber coated with a flame retardant. For example, the product name "Kevlar" manufactured by Dup〇nt & Division, the trade name "Nomex" manufactured by Dupont Co., Ltd., the product name "RTechn〇ra" manufactured by Teijin Co., Ltd., the product name "Twaron" manufactured by Teijin Co., Ltd., and the Teijin company can be used. Trade name 152753.doc • 25· 201134992

Conex」’作為上述聚苯硫醚纖維,例如可使用東洋紡公 司製造之商品丨;作為上述聚酿亞胺纖維,例 如可使用東洋纺公司製造之商品名「p84」;作為上述聚酿 胺醯亞胺纖維,例如可使用Kermel公司製造之商品名 「Kermel」;作為上述難燃聚酯纖維,例如可使用東洋紡 公司製造之商品名r Heim」、Trevira公司製造之商品名 「Trevira CS」;作為上述三聚氰胺纖維,例如可使用 Basofil Fiber公司製造之商品名「Bas〇fu」;作為上述丙烯 酸酯纖維,例如可使用東洋紡公司製造之商品名 「MoiSCarej;作為上述聚苯氧化物纖維,例如可使=東 洋紡公司製造之商品名「ZylGn」;作為上述聚偏二氣乙稀 纖維,例如可使用旭化成纖維公司製造之商品名 「Saran」;作為上述含有矽成分之再生纖維素纖維,例如 可使用Sated公司製造之商品名「㈣」、D—以卿 公司製造之商品名「FR Corona」、Omikenshi公司製造之 商品名「HOPE-FR」;作為上述含有磷系難燃劑之再生纖 維素纖維’例如可使用Lenzing公司製造之商品名 「Lenzing FR」、Omikenshi公司製造之商品名「ΝΕχτ· FR」、Daiwabo Rayon公司製造之商品名「dfg」等。 (難燃纖維集合體) 於本發明中,所謂難燃纖維集合體(c〇mp〇site),係指含 有上述含函素纖維者,係填充物等之棉、不織布、織物、 編織物、網眼針織物、編帶等。於本發明中,所謂難燃纖 維複合體(mixture),係上述難燃纖維集合體之一例,係指 152753.doc -26 - 201134992 :::述含齒素纖維與其他纖維而形成複合體者。本發明 唯及、纖維集合體包含上述含❹纖維、上述聚醋系纖 =了㈣維以外之難燃性纖維。當將上述難燃 ,、准集σ體之總1設為} 〇〇質量 負重/〇時,上述含齒素纖維之 3量為3〜30質量%,較佳 — W賢量。/。,更佳為5〜10質量 ^二為該範圍,則可獲得所需之_性,尤其於難燃纖 :集合體採用不織布或布帛之形態之情形時,獲得抑制接 焰之:面部之溫度上升’減輕對存在於背面之内部結構體 之熱知壞的效果,而且可接古 隹入 』徒阿難燃性。又,上述難燃纖維 :、口姐中之上述聚酯系纖維之含量為2〇〜質量%,較佳 為20〜40質量m該範圍,則可同時實現難燃纖維集 合體之難燃性與蓬鬆性或f感性。又,上述難燃纖維集合 體中之上述含i素纖維以外之難燃性纖維的含量為30〜77 質量%,較佳為35〜75重量%,進而較佳為4〇〜6〇質量%。 性能 若為該範圍内’則容易維持所需之滅火性,同時獲得難燃 又,只要不阻礙上述難燃纖維集合體之難燃性效果,則 亦可於難燃纖維集合體中含有上述纖維種類以外之纖維。 作為可含有之天然纖維,有棉(c〇tt〇n)纖維、木棉(kap〇k) 纖維、亞麻纖維、大麻纖維、苧麻(ramie)纖維、黃麻 (jute)纖維、馬尼拉麻(Manila hemp)纖維、洋麻 hemp)纖維、羊毛纖維、馬海毛(m〇hair)纖維、開司米山羊 毛(cashmere)纖維、駱駝纖維、阿爾帕卡毛(alpaca)纖維、 安哥拉(angora)纖維、絲纖維等。作為再生纖維有再生 152753.doc •27· 201134992 纖維素纖維(嫘縈、多元腦纖維(poiynosic)、旭化成公司製 造之商品名「Cupro」、Lenzing公司製造之商品名 「Tencel」、Lenzing公司製造之商品名「Lenzing Modal」)、再生膠原蛋白纖維、再生蛋白纖維、乙酸纖維 素纖維、普羅米克斯纖維(promix fibre)等。作為可含有之 合成纖維,有尼龍纖維、聚乳酸纖維、丙烯酸纖維、聚稀 烴纖維、聚乙烯醇纖維、聚乙烯纖維(東洋紡公司製造商 品名「Dyneema」)、聚胺基甲酸酯纖維、聚甲醛纖維等。 其於上述難燃纖維集合體中之比例係於〇〜3〇質量%之範圍 内選擇。只要以上述數值範圍含有上述含齒素纖維、上述 聚酯系纖維、及上述含齒素纖維以外之難燃性纖維,則可 於上述難燃纖維集合體中含有該等纖維。 於本發明中,上述難燃纖維集合體可藉由交織、 積層等將混棉、混紡、混纖、並人 、 加以處合而製造。又 態’有填充物等之棉 物、編帶等。 作為填充物等之棉 之棉等。 作為不織布,右.怎a 織布、熱黏合不織布切、製不織布、梳棉不織布、氣纺不 刺不織布、縫編不織匕學接著不織布、針刺不織布、水 工業上較為廉價。又,。熱黏合不織布、針刺不織布在 上包含均勻姓播 ,不織布可於厚度、寬度、長声士 ”。、明確之積層結構、不明確之積層 152753.doc 頌增心構中 戰 絲合絲、芯鞘等複合絲 作為上述難燃纖維集合體之具體形 不織布、織物、編織物、網眼針織 有開纖棉、棉球、網狀物、經成形 -28· 201134992 之任一者。 作為織物,有平紋織物、斜文織物、緞紋織物、變化平 紋織物、變化斜文織物、變化緞紋織物、花式織物、花紋 織物、單層織物、雙重組織、多重組織、縱起絨織物、橫 、成織物紗羅織物等。平紋織物、锻紋織物、花紋織物 的作為商品之質感及強度等優異。 作為編織物’包含圓編織物、緯編織物'經編織物、起 絨編織物等’有平針織物、平紋織物、重平織物、雙羅纹 織物(smooth stiteh)、羅紋織物、雙反面織物、經平組 織、經絨組織、經編锻紋組織、集圈抽花組織、夾概織物 等。平紋織物、重平織物的作為商品之質感優異。 所。月本發明之纖維製品(applicati〇n),係#包含上述 燃纖維集合體者,係射如以下矣-. 係對如以下表不一例之製品等之總稱。 (υ衣服及日用品材料 衣服(包括外衣、内衣、毛衣、背心、褲子等)、手套 機子、圍巾、帽子、寢具、枕、靠塾、布製玩偶等 U)特殊服裝 防護服、消防服、工作服、防寒服等 (3) 室内裝飾材料 椅套、窗簾、壁紙、地毯等 (4) 產業資材 過濾器、耐火填充物、襯裏材料等。 例如床 靠墊、 若使用本發明之纖維製品來製造寢具或傢俱 墊枕頭、棉被(comforter)、床罩戍 早床褥、被褥 152753.doc •29- 201134992 椅子等難燃性布藝製品,則可獲得具有難燃性,且具有質 感、觸感、色調、吸濕性等優異特性的布藝製品。作為床 墊,例如有内部使用金屬製彈簧之袋裝彈簧床墊(p〇cket coil mattress)、框架彈簧床墊(b〇x c〇il mamess),或者内 部使用使苯乙烯或胺基曱酸酯樹脂等發泡而成之絕緣體或 低斥力胺基曱酸g曰之床墊等。藉由本發明之難燃纖維集合 體之難燃性,可防止向上述床墊内部之結構體延燒,故於 任一結構之床墊中,均可獲得難燃性優異,同時質感及觸 感亦優異之床墊。作為椅子,可列舉屋内使用之凳子、長 椅、單椅、扶手椅、躺椅•沙發、座椅裝置(可組合式椅 子、可分離式椅子(separate chair))、搖椅、摺疊椅、堆疊 椅(packing chair)、旋轉椅、或於屋外用於車輛用座位等 之,車座位、船舶用座位、飛機用座位、列車用座位等, 該等之中,亦可獲得具有作為通常之傢俱所要求之外觀及 觸感’同時具有防止内部之延燒之功能的難燃性製品。 作為針對難燃性布㈣品的包含本發明之難燃纖維集人 體之原材料(以下稱作本發明之原材料)的使时法,可: 織物或編物之形態詩表面之布料,亦可以織物、編物、 不織布之形態夾人於表面之布料與内部結構物例如胺 ,泡體及填充棉之間。於用於表面之布料之情形:, 只要使用本發明之原材料替代先前之表面之布料即可。 又,於夾持於表面原材料與内部結構物之間之情形時,可 於2片表面原材料之間夾人本發明之原材料亦可以本 明之原材料覆蓋内部結構物。再者,於財發明之原㈣ 152753.doc 201134992 覆蓋内部結構物之情形時,較佳為至少與表面之布料接觸 的内部結構物之部分由本發明之原材料所覆蓋。 [實施例] 以下,藉由實施例對本發明進行更加詳細之說明,但本 發明並不限定於該實施例。再者,於下述實施例中, 「%」係指「質量%」。 (脫函反應促進之評價方法) 脫齒反應促進之評價方法係使用熱重/熱示差測定計 (Seiko Instrument股份有限公司製造,商品名 「TG/DTA220」)’以下述方式實施。 將包含丙烯腈51.5質量份、含鹵素亞乙烯基單體47 4質 量份及苯乙烯磺酸鈉Μ質量份之聚合物(1) 5 mg,於空氣 條件下(氣體流量:200 ml/min,升溫速度:2(rc/min)加 熱時,測疋重量開始減少之溫度。於本發明中,將該重量 開始減少之溫度定義為脫鹵起始溫度。所測定之脫鹵起始 溫度為2 4 3 °C。 繼而,相對於上述聚合物(1) 100質量份,添加下述表1 所示之金屬化合物10質量份,將充分混合之試料5 mg於空 氣條件下(氣體流量:200 ml/min,升溫速度:2(rc/min) 加熱。此時,將脫函起始溫度未達243^之情形判定為促 進脫鹵反應,S己作A。又’將脫鹵起始溫度為243。。以上之Conex"', as the polyphenylene sulfide fiber, for example, a commercially available product manufactured by Toyobo Co., Ltd.; and, for example, the product name "p84" manufactured by Toyobo Co., Ltd.; For the amine fiber, for example, the product name "Kermel" manufactured by Kermel Co., Ltd., and the trade name "R Heim" manufactured by Toyobo Co., Ltd., and the trade name "Trevira CS" manufactured by Trevira Co., Ltd. can be used as the above-mentioned flame retardant polyester fiber; For the melamine fiber, for example, the product name "Bas〇fu" manufactured by Basofil Fiber Co., Ltd. can be used. For the acrylate fiber, for example, the product name "MoiSCarej" manufactured by Toyobo Co., Ltd. can be used as the above polyphenylene oxide fiber, for example, The product name "ZylGn" manufactured by the company; for the above-mentioned polyvinylidene-containing ethylene fiber, for example, the product name "Saran" manufactured by Asahi Kasei Fiber Co., Ltd.; and the regenerated cellulose fiber containing the bismuth component, for example, can be manufactured by Sated Co., Ltd. The trade name "(4)", D - the trade name "fr Corona" made by the company The product name "HOPE-FR" manufactured by Omikenshi Co., Ltd.; and the regenerated cellulose fiber containing the phosphorus-based flame retardant, for example, the product name "Lenzing FR" manufactured by Lenzing Co., Ltd., and the trade name "ΝΕχτ·" manufactured by Omikenshi Co., Ltd. FR", the product name "dfg" manufactured by Daiwabo Rayon Co., Ltd., etc. (Flame-resistant fiber aggregate) In the present invention, the term "c〇mp〇site" means a cotton, a nonwoven fabric, a woven fabric, a woven fabric, or the like which contains the above-mentioned filler-containing fiber. Mesh knits, braids, etc. In the present invention, the "flammable fiber composite" is an example of the above-mentioned flame-retardant fiber assembly, and is referred to as 152753.doc -26 - 201134992 ::: a dentate fiber and other fibers form a composite body. . In the present invention, the fiber assembly includes the above-mentioned ruthenium-containing fiber and the above-mentioned polyester fiber-containing fiber. When the total of 1 of the above-mentioned flame retardant and quasi-collector σ bodies is set to 〇〇 mass load/〇, the amount of the dentate-containing fibers is 3 to 30% by mass, preferably - sm. /. More preferably, it is 5 to 10 masses. If the range is 2, the desired properties can be obtained, especially for the incombustible fiber. When the aggregate is in the form of a non-woven fabric or a cloth, the flame is suppressed: the temperature of the face Rising 'to alleviate the effect of the heat of the internal structure that exists on the back side, and it can be smothered. Further, in the above-mentioned flame-retardant fiber, the content of the polyester-based fiber in the mouth-in-law is 2% to 3% by mass, preferably 20 to 40% by mass, and the flame retardancy of the flame-retardant fiber assembly can be simultaneously achieved. With fluffiness or f sensitivity. Further, the content of the flame retardant fiber other than the i-containing fiber in the flame-retardant fiber assembly is 30 to 77% by mass, preferably 35 to 75% by weight, and more preferably 4 to 65% by mass. . If the performance is within the range, it is easy to maintain the required fire-extinguishing property, and at the same time, it is difficult to obtain the above-mentioned fiber in the flame-retardant fiber assembly as long as it does not hinder the flame retardancy effect of the above-mentioned flame-retardant fiber assembly. Fibers other than the species. As natural fibers that can be contained, there are cotton (c〇tt〇n) fibers, kapok (kap〇k) fibers, flax fibers, hemp fibers, ramie fibers, jute fibers, and Manila hemp. Fiber, kenaf hemp) fiber, wool fiber, mohair hair, cashmere fiber, camel fiber, alpaca fiber, angora fiber, silk fiber, and the like. Recycled as a recycled fiber 152753.doc •27· 201134992 Cellulose fiber (poiynosic), trade name "Cupro" manufactured by Asahi Kasei Corporation, trade name "Tencel" manufactured by Lenzing, manufactured by Lenzing Trade name "Lenzing Modal"), regenerated collagen fiber, regenerated protein fiber, cellulose acetate fiber, promix fiber, and the like. Examples of the synthetic fibers that may be contained include nylon fibers, polylactic acid fibers, acrylic fibers, polyolefin fibers, polyvinyl alcohol fibers, polyethylene fibers (trade name "Dyneema" manufactured by Toyobo Co., Ltd.), and polyurethane fibers. Polyoxymethylene fiber, etc. The ratio in the above-mentioned flame-retardant fiber assembly is selected within the range of 〇3 to 3% by mass. When the dentate-containing fibers, the polyester fibers, and the flame-retardant fibers other than the dentate-containing fibers are contained in the above numerical range, the fibers may be contained in the flame-retardant fiber assembly. In the present invention, the above-mentioned flame-retardant fiber assembly can be produced by blending, blending, blending, and blending by interlacing, laminating, or the like. Also, there is a cotton material such as a filler or a braid. Cotton or the like as a filler or the like. As a non-woven fabric, right. How to weave, heat-bonded non-woven fabric, non-woven fabric, carded non-woven fabric, air-woven non-woven fabric, non-woven fabric, non-woven fabric, needle-punched non-woven fabric, water industry is relatively cheap. also,. Heat-bonded non-woven fabric, needle-punched non-woven fabric contains uniform surname on the top, non-woven fabric can be used in thickness, width, and long-sounding.", clear laminated structure, unclear laminated layer 152753.doc 颂 心 构 构 中 、 、 、 A composite yarn such as a sheath is a non-woven fabric, a woven fabric, a woven fabric, or a mesh knitted fabric of the above-mentioned flame-retardant fiber assembly, and is knitted with any of an open-fiber cotton, a cotton ball, a mesh, and a formed -28·201134992. There are plain weave, slanted fabric, satin fabric, variegated fabric, slanted woven fabric, woven satin fabric, fancy fabric, woven fabric, single layer fabric, double tissue, multiple tissues, vertical pile fabric, horizontal, A woven fabric, a woven fabric, a woven fabric, and a woven fabric are excellent in texture and strength as a product. The woven fabric includes a circular woven fabric, a weft knitted fabric, a warp knitted fabric, a piled woven fabric, etc. Jersey, plain weave, heavy weave, smooth stiteh, rib fabric, double reverse fabric, warp-knitted tissue, warp-knitted fabric, warp-knitted weave, tuck A woven fabric, a woven fabric, etc. The plain woven fabric and the heavy woven fabric are excellent in texture as a product. The fiber product (applicati〇n) of the invention of the present invention, which contains the above-mentioned fuel fiber aggregate, is as follows矣-. A general name for products such as the following: (υ Clothes and daily necessities materials (including outerwear, underwear, sweaters, vests, pants, etc.), gloves, scarves, hats, bedding, pillows, Um, cloth dolls, etc. U) special clothing protective clothing, fire service, overalls, winter clothes, etc. (3) interior decoration materials, chair covers, curtains, wallpapers, carpets, etc. (4) Industrial materials filter, refractory filler, lining material For example, a bed cushion, if the fiber product of the present invention is used to manufacture a bedding or furniture cushion pillow, a comforter, a bed cover, an early bed mattress, a bedding 152753.doc • 29-201134992, and other non-flammable fabric products, It is possible to obtain a fabric product which is flame retardant and has excellent properties such as texture, touch, color tone, moisture absorption, etc. As a mattress, for example, a bag spring in which a metal spring is used internally P〇cket coil mattress, frame spring mattress (b〇xc〇il mamess), or internal insulation for foaming styrene or amino phthalate resin or low repellency amine ruthenium citrate The mattress or the like of the mattress of the present invention can prevent the structure of the inside of the mattress from being burnt by the flame retardancy of the flame-retardant fiber assembly of the present invention, so that the mattress of any structure can be excellent in flame retardancy. At the same time, the mattress with excellent texture and touch is also used as a chair, which can be used as a stool, bench, single chair, armchair, recliner, sofa, seat device (combinable chair, separable chair) )), rocking chair, folding chair, packing chair, swivel chair, or seat for vehicles, etc., seat for cars, seats for ships, seats for airplanes, seats for trains, etc. It is also possible to obtain a flame-retardant product having the function of preventing the appearance and feel of the usual furniture as well as preventing the internal burning. As a time-making method for a flame-retardant cloth (four) product comprising a flame-retardant fiber of the present invention (hereinafter referred to as a raw material of the present invention), it may be: a fabric of a fabric or a knitted fabric, or a fabric, The pattern of knitted fabrics and non-woven fabrics is sandwiched between the fabric of the surface and internal structures such as amines, foams and filled cotton. In the case of a fabric for a surface: it is sufficient to replace the cloth of the previous surface with the raw material of the present invention. Further, in the case of being sandwiched between the surface material and the internal structure, the raw material of the present invention can be sandwiched between the two surface materials, and the internal structure can be covered with the raw material of the present invention. Further, in the case of the original invention of the invention (4) 152753.doc 201134992, it is preferred that at least part of the internal structure in contact with the fabric of the surface is covered by the raw material of the present invention. [Examples] Hereinafter, the present invention will be described in more detail by way of examples, but the invention is not limited thereto. Furthermore, in the following embodiments, "%" means "% by mass". (Evaluation method for decoupling reaction promotion) The evaluation method for the promotion of the detoxification reaction was carried out in the following manner using a thermogravimetric/thermal differential measurement meter (manufactured by Seiko Instrument Co., Ltd., trade name "TG/DTA220"). 50.1 parts by mass of acrylonitrile, 47 parts by mass of halogen-containing vinylidene monomer, and 5 parts by mass of sodium styrene sulfonate (1) 5 mg, under air conditions (gas flow rate: 200 ml/min, Heating rate: 2 (rc/min) When heating, the temperature at which the weight starts to decrease is measured. In the present invention, the temperature at which the weight starts to decrease is defined as the dehalogenation starting temperature. The measured dehalogenation starting temperature is 2 4 3 ° C. Then, 10 parts by mass of the metal compound shown in the following Table 1 was added to 100 parts by mass of the above polymer (1), and 5 mg of the sample which was sufficiently mixed was placed under air (gas flow rate: 200 ml). /min, heating rate: 2 (rc/min) heating. At this time, the starting temperature of the decoupling is less than 243^, which is determined to promote the dehalogenation reaction, and S is used as A. 243. above

If形判為未促進脫函反應,記作B。將各金屬化合物之 §平Ί貝結果不於表1中。 (碳化反應促進之評價方法) 152753.doc •31- 201134992 碳化反應促進之評價方法係使用熱重/熱示差測定計 (Seiko Instrument股份有限公司製造,商品名「TG/ DTA220」),以如下方式實施。 將包含丙烯腈51.5質量份、含鹵素亞乙烯基單體47.4質 量份及苯乙烯磺酸鈉1.1質量份之聚合物(1) 5 mg,於空氣 條件下(氣體流量:200 ml/min,升溫速度:2〇t:/min)加 熱時’測定500°C下之殘餘重量率。其結果,殘餘重量率 為 52% 〇 繼而’相對於上述聚合物(1) 100質量份,添加下述表1 所示之金屬化合物1 〇質量份,將充分混合之試料5 mg於空 氣條件下(氣體流量:2〇〇 ml/min,升溫速度:2〇°C /min) 加熱。此時,將5〇〇°C下之殘餘重量率為47°/。以上之情形 判定為促進碳化反應,記作^^又,將5〇〇t>c下之殘餘重量 率未達47%之情形判定為未促進碳化反應,記作B ^將各 金屬化合物之評價結果示於下述表1中。 (無機化合物之含有元素量及矽元素之含量) °式料(難燃纖維集合體中之含函素纖維以外之難燃性纖 維等)中之無機化合物之含有元素量或試料(難燃纖維集合 體中之含齒素纖維以外之難燃性纖維等)中之矽元素之含 量均係使用螢光X射線分析裝置(sn Nan〇 Techn〇l〇gy公司 製造,商品名「SEA221GA」),利用針對測定對象之元素 而製成之用以算出含量之校準曲線來算出。 152753.doc -32· 201134992 [表l]If the shape is judged as not promoting the decoupling reaction, it is recorded as B. The results of the diced mussels of each metal compound are not shown in Table 1. (Evaluation method for carbonization reaction promotion) 152753.doc •31- 201134992 The evaluation method for carbonization reaction promotion is performed by using a thermogravimetric/thermal differential measurement meter (manufactured by Seiko Instrument Co., Ltd., trade name "TG/DTA220") in the following manner. Implementation. The polymer (1) 5 mg containing 51.5 parts by mass of acrylonitrile, 47.4 parts by mass of a halogen-containing vinylidene monomer, and 1.1 parts by mass of sodium styrene sulfonate is heated under air conditions (gas flow rate: 200 ml/min). Speed: 2 〇 t: / min) When heating, the residual weight ratio at 500 ° C was measured. As a result, the residual weight ratio was 52%, and then '100 parts by mass of the above polymer (1) was added, and 1 part by mass of the metal compound shown in the following Table 1 was added, and 5 mg of the sample which was sufficiently mixed was placed under air conditions. (Gas flow rate: 2 〇〇 ml/min, heating rate: 2 〇 ° C / min) Heating. At this time, the residual weight ratio at 5 ° C was 47 ° /. In the above case, it was judged that the carbonization reaction was promoted, and it was recorded that the residual weight ratio under 5〇〇t>c was less than 47%, and it was judged that the carbonization reaction was not promoted, and the evaluation of each metal compound was recorded as B^. The results are shown in Table 1 below. (the content of the inorganic compound and the content of the lanthanum element) The content of the inorganic compound or the sample (the flame retardant fiber in the flame retardant fiber other than the functional fiber in the flame retardant fiber aggregate) The content of the lanthanum element in the flame retardant fiber other than the dentate fiber in the aggregate is a fluorescent X-ray analyzer (sn., manufactured by Sn Nan〇Techn〇l〇gy, trade name "SEA221GA"). It is calculated by using a calibration curve for calculating the content of the element to be measured. 152753.doc -32· 201134992 [Table l]

金屬化合物 脫氯起始溫度(°c) (脫鹵反應促進 評價方法) 500°C殘餘重量(%) (碳化反應促進 評價方法) 脫氣反應 促進性能 碳化 促進性能 無 243 52 - _ 氧化鋅 181 62 A A 碳酸辞 187 57 A A 硫化鋅 238 56 A A 氧化鎢 241 54 A A 氧化結 238 54 A A 氧化錫 200 56 A A 氧化銅 222 62 A A 磷酸銅 235 53 A A 三氧化銦 236 56 A A 鈦酸鋇 242 56 A A 硼酸鋅 237 49 A A 錫酸鋅 196 47 A A 偏錫酸 234 51 A A 三氧化銻 220 42 A B 五氧化録 220 42 A B 銻酸鈉 220 42 A B 氧化鐵 233 11 A B 磷酸鐵 230 35 A B 草酸鐵 227 28 A B 硫化鐵 226 40 A B 氧化_ 241 46 A B 三氧化鉍 197 43 A B 氧氣化鉍 191 39 A B 蛾化銅 203 41 A B 氫氧化鋁 244 45. B B 對曱苯磺酸辞 230 53 A A (含_素纖維之製造例1) 使包含丙烯腈51%、偏二氯乙烯48%及對苯乙烯磺酸鈉 1 %之共聚物以樹脂濃度成為30%之方式溶解於丙酮中,相 對於所得樹脂溶液之樹脂100質量份,以下述表2所示之添 加量,添加作為金屬化合物(2-1)之氧化辞(氧化鋅JIS 3 種)、作為金屬化合物(2-2)之三氧化銻,製成紡絲原液。 152753.doc -33- 201134992 使用喷嘴孔徑為0·10 孔數為1〇〇〇孔之喷嘴,將該紡 絲原液播出至3 0%丙酮水溶液中,一面使其凝固,一面以 3.3倍之延伸倍率進行一次延伸,水洗後於12〇t>c下進行乾 燥,於140°C下以1.3倍之延伸倍率進行二次延伸後,於加 熱水蒸氣中(飽和水蒸氣)17〇°c下,以0.85倍之缓和倍率進 行20秒之緊張熱處理,進而進行切斷,藉此獲得含鹵素纖 維。所得之纖維係纖度為7.8 dtex,切割長為64 mm之短纖 維’收縮變動為58%。 (含南素纖維之製造例2) 使包含丙烯腈57%、偏二氣乙烯41%及烯丙基磺酸鈉2〇/〇 之共聚物以樹脂濃度成為25%之方式溶解於二甲基甲醢胺 中,相對於所得樹脂溶液之樹脂1〇〇質量份,以下述表2所 示之添加量,添加作為金屬化合物(2“)之對曱苯磺酸鋅、 作為金屬化合物(2-2)之五氧化綈,製成紡絲原液。使用喷 嘴孔徑為0.06 mm及孔數為1〇〇〇孔之喷嘴,將該紡絲原液 擠出至55%二曱基曱醯胺水溶液中,一面使其凝固,一面 以5.6倍之延伸倍率進行一次延伸,水洗後於12〇艺下進行 乾燥,進而於濕熱加壓蒸氣中(飽和水蒸氣)13〇c>Ct,於緩 和倍率成為Q.85倍之無緊張之狀態下進行5分鐘之鬆他處 理’進而進行切斷,藉此獲得含函素纖維。所得之纖維係 纖度為7.8 dtex,切割長為64 mm之短纖維收縮變動為 63% 〇 (含幽素纖維之製造例3 ) 使包含丙稀腈51。/。、偏二氣乙稀似及對笨乙稀項酸納 152753.doc -34* 201134992 1〇/〇之共聚物以樹脂濃度成為30%之方式溶解於丙酮中,相 對於所得樹脂溶液之樹脂i00質量份,以下述表2所示之添 加量添加作為金屬化合物(2-1)之氧化鋅(氧化鋅JIS 3 種)、作為金屬化合物(2_2)之三氧化銻,製成紡絲原液。 使用喷嘴孔徑為〇.1〇 mm及孔數為1〇〇〇孔之喷嘴將該紡 絲原液擠出至30〇/〇丙酮水溶液中,一面使其凝固,一面以 3.3倍之延伸倍率進行一次延伸,水洗後於12〇它下進行乾 燥,於140C下以1.3倍之延伸倍率進行二次延伸後,於加 熱水蒸氣(飽和水蒸氣)*17〇〇c下,以〇85倍之緩和倍率進 行20秒之緊張熱處理,進而進行切斷,藉此獲得含鹵素纖 維。所得之纖維係纖度為78 dtex,切割長為64 mm之短纖 維,收縮變動為61%。 (含齒素纖維之製造例4) 使包含丙烯腈51%、偏二氯乙烯48%及對苯乙烯磺酸鈉 1%之共聚物以樹脂濃度成為3〇%之方式溶解於丙酮中,相 對於所得樹脂溶液之樹脂1〇〇質量份,以下述表2所示之添 加量,添加作為金屬化合物之氧化錫、作為金屬化合 物(2_2)之三氧化銻,製成紡絲原液。使用喷嘴孔徑為0.10 mm及孔數為1〇〇〇孔之喷嘴,將該紡絲原液擠出至3〇%丙酮 水溶液中,一面使其凝固,一面以33倍之延伸倍率進行 一次延伸,水洗後於12〇它下進行乾燥,於i4〇t下以Μ 倍之延伸倍率進行二次延伸後,於加熱水蒸氣(飽和水蒸 氣)中170C下,以0.85倍之緩和倍率進行2〇秒之緊張熱處 理,進而進行切斷,藉此獲得含齒素纖維。所得之纖維係 152753.doc •35- 201134992 纖度為7.8 dtex’切割長為64 _之短纖維收縮變動為 60%。 (含函素纖維之製造例5) 使包含丙烯腈51%、偏二氣乙烯48%及對苯乙稀續酸納 1%之共聚物以樹脂濃度成為3〇%之方式溶解於丙酮中,相 對於所得樹脂溶液之樹脂1〇〇質量份’以下述表2所示之添 加罝,添加作為金屬化合物(2_丨)之碳酸鋅、作為金屬化合 物(2-2)之三氧㈣’製成紡絲原液。使用喷嘴孔徑為m mm及孔數為1000孔之喷嘴,將該紡絲原液擠出至。丙酮 水溶液中,一面使其凝固,一面以3.3倍之延伸倍率進行 一次延伸,水洗後於12(TC下進行乾燥,於14〇t下以1 3 倍之延伸倍率進行二次延伸後,於加熱水蒸氣(飽和水蒸 氣)中170C下,以0.85倍之緩和倍率進行2〇秒之緊張熱處 理進而進行切斷,藉此獲得含ii素纖維。所得之纖維係 纖度為7.8 dtex,切割長為64 mm之短纖維,收縮變動為 60%。 (含南素纖維之製造例6) 面使其凝固’ 一面以 使包含丙烯腈51%、偏二氣乙烯48%及對苯乙烯磺酸鈉 1%之共聚物以樹脂濃度成為3〇%之方式溶解於丙酮中,相 對於所得樹脂溶液之樹脂1〇〇質量份,以下述表2所示之添 加量’添加作為金屬化合物(2-1)之氧化鋅(氧化鋅jIS 3 種)、作為金屬化合物(2-2)之三氧化銻,製成紡絲原液。 使用喷嘴孔徑為〇.1〇 mm及孔數為1〇〇〇孔之喷嘴,將該紡 絲原液擠出至3〇〇/。丙酮水溶液中 152753.doc -36· 201134992 3·3倍之延伸倍率進行—:欠延伸,水洗後於12(TC下進行乾 燥,於l4〇°C下以!·3倍之延伸倍率進行二次延伸後於: 熱水蒸氣(飽和水蒸氣)中17〇艺下,以〇85倍之緩和倍率進 订20秒之緊張熱處理,進而進行切斷,藉此獲得含函素纖 維。所得之纖維係纖度為7·8 dtex,切割長為64mm之短纖 維,收縮變動為59%。 (含齒素纖維之製造例7) 使包含丙烯腈51%、偏二氣乙烯48%及對苯乙烯磺酸鈉 1%之共聚物以樹脂濃度成為3〇%之方式溶解於丙酮中,相 對於所得樹脂溶液之樹脂1〇〇質量份,以下述表2所示之添 加量,添加作為金屬化合物(2_丨)之氡化鋅(氧化鋅jis 3 種)、作為金屬化合物(2·2)之三氧化銻,製成紡絲原液。 使用喷嘴孔徑為〇.1〇 孔數為1〇〇〇孔之喷嘴,將該紡 絲原液擠出至30%丙酮水溶液中,一面使其凝固,一面以 3.3倍之延伸倍率進行一次延伸’水洗後於12〇它下進行乾 燥,於140 C下以1.3倍之延伸倍率進行二次延伸後,於加 熱水蒸氣(飽和水蒸氣)$170〇CT,以〇85倍之緩和倍率進 行2分鐘之緊張熱處理,進而進行切斷,藉此獲得含鹵素 纖維。所得之纖維係纖度為7.8 dtex,切割長為64 mm之短 纖維’收縮變動為52%。 (含鹵素纖維之製造例8) 使包含丙烯腈5 1%、偏二氣乙烯48%及對苯乙烯磺酸鈉 1 %之共聚物以樹脂濃度成為30%之方式溶解於丙酮中,相 對於所得樹脂溶液之樹脂10〇質量份,以下述表2所示之添 152753.doc •37· 201134992 %、加作為金屬化合物(2_!)之氧化辞(氧化鋅JIS $ 種)、作為金屬化合物(2_2)之五氧化録,製成纺絲原液。 使用喷嘴孔輕為〇 1〇 mm及孔數為i刚孔之喷嘴將該纺 絲原液擠出至3〇%丙酮水減巾,—面使其凝固,一面以 3β·3倍之延伸倍率進行—次延伸,水洗後於12(TC下進行乾 燥,於HOt下以1>3倍之延伸倍率進行二次延伸後,於加 熱水蒸氣(飽和水蒸氣)中17(rc下,以〇.85倍之緩和倍率進 灯20私之緊張熱處理’進而進行切斷,藉此獲得含齒素纖 、准所侍之纖維係纖度為7.8 dtex,切割長為64 mm之短纖 維’收縮變動為60%。 (含齒素纖維之製造例9) 使包含丙烯腈51%、偏二氣乙烯48%及對苯乙烯磺酸鈉 1%之共聚物以樹脂漠度成為30%之方式溶解於丙綱中,相 對於所得樹脂溶液之樹脂100質量份,以下述表2所示之添 加量,添加作為金屬化合物(21)之氧化鋅(氧化鋅3 種),製成紡絲原液。使用喷嘴孔徑為〇 1〇 及孔數為 1000孔之喷嘴,將該紡絲原液擠出至3〇%丙酮水溶液中, 一面使其凝固,一面以33倍之延伸倍率進行一次延伸, 水洗後於12〇t下進行乾燥,於140°c下以〗3倍之延伸倍 率進行一次延伸後,於加熱水蒸氣(飽和水蒸氣)中! 7〇亡 下,以0.85倍之緩和倍率進行2分鐘之緊張熱處理,進而 進行切斷,藉此獲得含函素纖維。所得之纖維係纖度為 7.8 dtex,切割長為64 mm之短纖維,收縮變動為55〇/〇。 (含鹵素纖維之製造例10) 152753.doc -38- 201134992 使包含丙浠腈51 %、偏二氯乙稀48%及對苯乙烯續酸鈉 1%之共聚物以樹脂濃度成為30%之方式溶解於丙酮中,相 對於所得樹脂溶液之樹脂100質量份,以下述表2所示之添 加量’添加作為金屬化合物(2-1)之氧化鋅(氧化鋅JIS 3 種)、作為金屬化合物(2-2)之三氧化銻,製成紡絲原液。 使用嗅嘴孔徑為〇 mm及孔數為1〇〇〇孔之喷嘴,將該纺 絲原液擠出至3〇〇/0丙酮水溶液中,一面使其凝固,一面以 3_3倍之延伸倍率進行一次延伸’水洗後於1t下進行乾 燥’於140。(:下以1.3倍之延伸倍率進行二次延伸後,於 182C下’以〇.85倍之緩和倍率進行2分鐘之乾熱緊張熱處 理’進而進行切斷,藉此獲得含函素纖維。所得之纖維係 纖度為7.8 dtex,切割長為64 mm之短纖維,收縮變動為 47%。 (含齒素纖維之製造例η) 使包含丙烯腈51%、偏二氯乙烯48%及對笨乙烯磺酸鈉 1 /ό之共聚物以樹脂濃度成為3〇%之方式溶解於丙嗣中,相 對於所得樹脂溶液之樹脂1〇〇質量份,以下述表2所示之添 加量,添加作為金屬化合物(2-1)之氧化鋅(氧化鋅jis ^ 種)、作為金屬化合物(2_2)之三氧化錄,製成紡絲原液。 使用喷嘴孔徑為〇.1〇 mm及孔數為1〇〇〇孔之喷嘴,將該紡 絲原液擠出至30%丙_水溶液中,一面使其凝固,一面以 3.75倍之延伸倍率進行一次延伸,水洗後於下進行 乾燥,然後於185°C下以〇.8倍之緩和倍率進行2分鐘之乾 熱緊張熱處理’進而進行切斷,藉此獲得含函素纖維。所 152753.doc •39- 201134992 得之纖維係纖度為7.8 dtex,切割長為64 mm之短纖維,收 縮變動為41°/。。 (含鹵素纖維之製造例12) 使包含丙烯腈5 1 %、偏二氣乙烯48%及對苯乙烯磺酸鈉 1 %之共聚物以樹脂濃度成為30%之方式溶解於丙酮中,相 對於所得樹脂溶液之樹脂1 〇〇質量份,以下述表2所示之添 加量,添加作為金屬化合物(2-1)之氧化鋅(氧化鋅jis 3 種)、作為金屬化合物(2-2)之三氧化銻,製成紡絲原液。 分別使用喷嘴孔徑為〇.〇6 mm及孔數為1〇〇〇孔之噴嘴,將 該纺絲原液擠出至30%丙酮水溶液中,一面使其凝固,一 面以3 ·3倍之延伸倍率進行一次延伸,水洗後於12〇°c下進 行乾燥’於140°C下以1.3倍之延伸倍率進行二次延伸後, 於加熱水蒸氣(飽和水蒸氣)中17〇°C下,以0.85倍之緩和倍 率進行20秒之緊張熱處理,進而進行切斷,藉此獲得含鹵 素纖維。所得之纖維係纖度為丨·7 dtex,切割長為64 mm之 短纖維’收縮變動為59%。 (含函素纖維之製造例13) 使包含丙烯腈51%、偏二氣乙烯48%及對苯乙烯磺酸鈉 之共聚物以樹脂濃度成為30%之方式溶解於丙酮中,相 對於所得樹脂溶液之樹脂1〇〇質量份,以下述表2所示之添 加量’添加作為金屬化合物(2-1)之氧化鋅(氧化鋅JIS 3 種)、作為金屬化合物(2·2)之三氧化銻,製成紡絲原液。 分別使用喷嘴孔徑為0.14 mm及孔數為1〇〇〇孔之喷嘴,將 該紡絲原液擠出至3 0 %丙酮水溶液中,一面使其凝固,一 152753.doc • 40- 201134992 面以3.3倍之延伸倍率進行一次延伸,水洗後於i 2〇艽下進 行乾燥,於140°C下以1.3倍之延伸倍率進行二次延伸後, 於加熱水蒸氣(飽和水蒸氣)中17〇乞下,以0.85倍之緩和倍 率進行20秒之緊張熱處理,進而進行切斷,藉此獲得含齒 素纖維。所得之纖維係纖度為17 dte}i,切割長為64爪瓜之 短纖維,收縮變動為58%。 (含齒素纖維之製造例14) 使包含丙烯腈51%、偏二氯乙烯48%及對苯乙烯磺酸鈉 1。/〇之共聚物以樹脂濃度成為3〇%之方式溶解於丙酮中,相 對於所得樹脂溶液之樹脂100質量份,以下述表2所示之添 加量’添加作為金屬化合物(2-2)之三氧化銻,製成紡絲原 液。使用喷嘴孔徑為〇.1〇 mm及孔數為1000孔之喷嘴,將 該紡絲原液播出至3 0〇/〇丙酮水溶液中,一面使其凝固,一 面以3.3倍之延伸倍率進行一次延伸,水洗後於12(TC下進 行乾燥,於140°C下以1.3倍之延伸倍率進行二次延伸後, 於加熱水蒸氣(飽和水蒸氣)中17〇°C下,以0.8倍之緩和倍 率進行20秒之緊張熱處理,進而進行切斷,藉此獲得含鹵 素纖維。所得之纖維係纖度為7 8 dtex,切割長為64 mm之 短纖維。關於所得纖維之收縮變動,由於測定時已切斷, 故無法計測。 (含函素纖維之製造例15) 使包含丙烯腈51%、偏二氯乙烯48%及對苯乙烯磺酸鈉 1 %之共聚物以樹脂濃度成為30%之方式溶解於丙酮中,相 對於所得樹脂溶液之樹脂1 〇〇質量份,以下述表2所示之添 152753.doc -41- 201134992 加量,添加作為金屬化合物(2_1}之氧化鋅(氧化鋅jis ^ 種)、作為金屬化合物(2-2)之三氧化銻,製成紡絲原液。 使用喷嘴孔徑為010 mm及孔數為1〇〇〇孔之噴嘴將該紡 絲原液擠出至3〇〇/0丙酮水溶液中,一面使其凝固,一面以 5·9倍之延伸倍率進行一次延伸,水洗後於120°C下進行乾 燥,然後於170eC下以0.85倍之緩和倍率進行2分鐘之乾熱 緊張熱處理,進而進行切斷,藉此獲得含函素纖維。所得 之纖維係纖度為7.8 dtex,切割長為64 mm之短纖維,收縮 變動為67%。 (含齒素纖維之製造例16) . 使包含丙烯腈57%、偏二氣乙烯4〇%及烯丙基磺酸鈉3% 之共聚物以樹脂濃度成為24 5%之方式溶解於二甲基曱醢 胺中,相對於所得樹脂溶液之樹脂1〇〇質量份,以下述表2 所不之添加量,添加作為金屬化合物(2_2)之三氧化銻,製 成紡絲原液。使用喷嘴孔徑為0.06 mm及孔數為100000孔 之噴嘴,將該紡絲原液擠出至55%二曱基曱醯胺水溶液 中,一面使其凝固,一面以56倍之延伸倍率進行一次延 伸,水洗後於13〇°C下進行乾燥,進而於濕熱加壓蒸氣中 (飽和水蒸氣)115°c下,以0 85倍之緩和倍率進行15分鐘之 緊張熱處理,進而進行切斷,藉此獲得含_素纖維。所得 之纖維係纖度為1.9 dtex,切割長為38 mm之短纖維,收縮 變動為68%。 (含鹵素纖維之製造例j 7) 使包含丙稀腈57%、偏二氣乙烯41%及烯丙基磺酸鈉2〇/〇 152753.doc •42· 201134992 之/、聚物以树脂濃度成為25 %之方式溶解於二曱基甲酿胺 中,相對於所得樹脂溶液之樹脂100質量份,以下述表2所 示之添加1 ’添加作為金屬化合物(2·丨)之對甲苯續酸鋅、 作為金屬化合物(2_2)之五氧化銻,製成紡絲原液。使用喷 嘴孔徑為0.06 mm及孔數為1〇〇〇〇〇孔之喷嘴,將該紡絲原 液擠出至55%二甲基曱醯胺水溶液中,一面使其凝固,— 面以5.6倍之延伸倍率進行一次延伸,水洗後於12(TC下進 行乾燥’進而於濕熱加壓蒸氣中(飽和水蒸氣)125<)(:下,於 緩和倍率成為0.85倍之無緊張之狀態下進行2分鐘之鬆弛 處理’進而進行切斷,獲得含鹵素纖維。所得之纖維係纖 度為丨.7 dtex ’切割長為64 mm之短纖維,收縮變動為 85%。 (含鹵素纖維之製造例18) 使包含丙烯腈50%、氣乙烯49 5%及苯乙烯磺酸鈉〇 5〇/〇 之共聚物以樹脂濃度成為30%之方式溶解於丙酮中,相對 於所得樹脂溶液之樹脂100質量份,以下述表2所示之添加 堇’添加作為金屬化合物(2-1)之羥基錫酸鋅、作為含環氧 基化合物之聚甲基丙烯酸縮水甘油酯(重量平均分子量為 40000) ’製成紡絲原液。又,於上述紡絲原液中添加〇 5質 量伤之Ciba Specialty Chemicals股份有限公司製造之 「TINUVIN1577FF」(2-(4,6-二苯基-1,3,5-三味-2-基))。使 用喷嘴孔徑為〇.1〇 孔數為12〇〇〇〇孔之噴嘴,將該紡 絲原液擠出至25%丙酮水溶液中,一面使其凝固,一面以 2.18倍之延伸倍率進行一次延伸,水洗後,於U5<>c下進 152753.doc •43· 201134992 行乾燥,其後於145°C下,以2.75倍之延伸倍率進行二次 延伸’進而於170。(:下,以0.92倍之緩和倍率進行3分鐘之 乾熱緊張熱處理,進而進行切斷,藉此獲得含!|素纖維。 所得之纖維係纖度為2.2 dtex,切割長為51 mm之短纖維, 收縮變動為160% » (含鹵素纖維之製造例19) 使包含丙烯腈52°/。、偏二氣乙烯46.8%及苯乙烯續酸鈉 1.2%之共聚物以樹脂濃度成為30%之方式溶解於丙_中, 相對於所得樹脂溶液之樹脂100質量份,以下述表2所示之 添加量,添加作為金屬化合物(2-1)之羥基錫酸鋅、作為金 屬化合物(2-2)之三氧化銻,製成紡絲原液。使用噴嘴孔徑 為〇.〇8 mm及孔數為15000孔之喷嘴,將該紡絲原液擠出至 38%丙酮水溶液中,一面使其凝固,一面以22ι倍之延伸 倍率進行一次延伸,水洗後於12〇t下進行乾燥,其後於 15〇°C下,以3.0倍之延伸倍率進行二次延伸,進而於 17〇°C下,以0.80倍之緩和倍率進行3〇秒之乾熱緊張熱處 理,進而進行切斷,藉此獲得含_素纖維。所得之纖維係 纖度為3 dtex,切割長為38 mm之短纖維,收縮變動為 73%。 (含鹵素纖維之製造例2〇) 使包含丙烯腈52%、偏二氣乙烯47%及甲基稀丙基續酸 納1%之共聚物以樹脂濃度成為25%之方式溶解於二甲基甲 醯胺中,相對於所得樹脂溶液之樹脂丨〇〇質量份,以下述 表2所示之添加量’添加作為金屬化合物(η)之氧化錯、 152753.doc 201134992 作為金屬化合物(2-2)之五氧化銻,製成紡絲原液》使用喷 嘴孔徑為0.07 mm及孔數為30000孔之噴嘴’將該紡絲原液 擠出至50%二甲基甲醯胺水溶液中,一面使其凝固,一面 以8.0倍之延伸倍率進行一次延伸,水洗後於i3(rc下進行 乾燥’進而於濕熱加壓蒸氣中(飽和水蒸氣)120〇C下,於緩 和倍率成為0.8倍之無緊張之狀態下進行15分鐘之鬆弛處 理’進而進行切斷,藉此獲得含_素纖維。所得之纖維係 纖度為7.8 dtex,切割長為64 mm之短纖維,收縮變動為 72%。 (含鹵素纖維之製造例21) 使包含丙烯腈5〇。/0、氣乙烯48%及曱基烯丙基磺酸鈉2% 之共聚物以樹脂濃度成為30%之方式溶解於丙酮中,製成 纺、·糸原液。使用喷嘴孔徑為〇 min及孔數為30000孔之噴 嘴,將該紡絲原液擠出至30%丙酮水溶液中,一面使其凝 固 面以3.3倍之延伸倍率進行一次延伸,水洗後於 135°C下進行乾燥,其後於145<>(:下,以2 49倍之延伸倍率 進行二次延伸,進而於濕熱加壓蒸氣中(飽和水蒸氣)U5t 下,於緩和倍率成為〇·7倍之無緊張之狀態下進行i5分鐘 之鬆弛處理,鬆弛處理後,於丨丨5它下進行1 〇分鐘之乾 燥…;、後進行延伸直至消除捲縮為止,進而進行切斷,藉 此獲得含_素纖維。所得之纖維係纖度為7 8 I,切^ 長為64爪以之短纖維。關於所得纖維之收縮變動,由於測 定時已切斷’故無法計測。 (含_素纖維之製造例22) 152753.doc •45- 201134992 使包含丙烯腈51%、偏二氣乙烯48%及對苯乙烯磺酸鈉 1 %之共聚物以樹脂濃度成為3〇%之方式溶解於丙酮中,相 對於所得樹脂溶液之樹脂100質量份,以下述表2所示之添 加量,添加作為金屬化合物(2d)之氧化鋅(氧化鋅Jls 3 種)、作為金屬化合物(2-2)之三氧化銻,製成紡絲原液。 使用喷嘴孔徑為〇·1〇 mm及孔數為1〇〇〇孔之喷嘴,將該紡 絲原液擠出至3 0〇/〇丙酮水溶液中,一面使其凝固,一面以 3.3倍之延伸倍率進行一次延伸,水洗後於進行乾 燥’於140。(:下以1.3倍之延伸倍率進行二次延伸後,於 170C下,以0.85倍之緩和倍率進行2分鐘之乾熱緊張熱處 理,進而進行切斷’藉此獲得含齒素纖維。所得之纖維係 纖度為7.8 dtex,切割長為64 mm之短纖維,收縮變動為 70%。 再者’含函素纖維之收縮變動係以如下方式測定者。 (纖維收縮率之測定方法) 使依據上述製造例而製作之含鹵素纖維成為3333 dtex(分德士)後’採用約5 mm,利用tma(熱應力應變測定 裝置[Seiko Instrument股份有限公司製造,商品名 ^ TMA/SS150C」],使用氣體:氮氣,氣體流量:3〇 L/min ’升溫速度:2〇eC/min ’荷重18 mN)進行測定。若 將初始樣品長設為X ’且將任意溫度下之樣品長設為γ, 則纖維收縮率係由下式所表示。所謂本發明之含函素纖維 於0.0054 mN/dtex之荷重下將溫度自50〇c提高至3〇〇°c時並 未切斷而殘存,係指一面於〇 〇〇54 mN/dtex之荷重下將溫 152753.doc -46· 201134992 度自50°C提高至300°C ’ 一面利用上述測定方法測定纖維 收縮率(於本說明書中,亦僅稱作收縮率)之情形時,本發 明之含齒素纖維並未切斷而殘存: 纖維收縮率(°/。)=1 00-[(100χΥ)/Χ]。 (收縮變動之算出方法) 所謂將溫度自50°c提高至300。(:時之收縮變動,係指於 上述纖維收縮率之測定中,於5(rc至3〇〇〇c之溫度範圍内 上述纖維收縮率之最高點(α%)與最低點(p%)之差量。於纖 隹收縮率之測定中,當纖維切斷時收縮變動設為無限 大。 將製造例1〜22中之一-女it #位、东 , 。 T之_人延伸倍率、二次延伸倍率、熱處 中.之緩和倍率及總延伸倍率等紡絲條件亦示於下述表2 伸倍延伸倍料H次延伸倍率Χ二次延 .,、、處理時之緩和倍率而獲得之值。 152753.doc -47. 201134992Dechlorination onset temperature of metal compound (°c) (Evaluation method for dehalogenation reaction) 500°C residual weight (%) (Carbonation reaction evaluation method) Degassing reaction promotion performance Carbonization promotion performance No 243 52 - _ Zinc oxide 181 62 AA Carbonate 187 57 AA Zinc Sulfide 238 56 AA Tungsten Oxide 241 54 AA Oxidation Junction 238 54 AA Tin Oxide 200 56 AA Copper Oxide 222 62 AA Copper Phosphate 235 53 AA Indium Oxide 236 56 AA Barium Titanate 242 56 AA Boric Acid Zinc 237 49 AA zinc stannate 196 47 AA metastannic acid 234 51 AA antimony trioxide 220 42 AB five oxidation record 220 42 AB sodium citrate 220 42 AB iron oxide 233 11 AB iron phosphate 230 35 AB oxalate iron 227 28 AB vulcanization Iron 226 40 AB Oxidation _ 241 46 AB Antimony trioxide 197 43 AB Oxide 铋 191 39 AB Moth copper 203 41 AB Aluminium hydroxide 244 45. BB p-Toluene sulfonate 230 53 AA (Manufacture of _ fiber Example 1) A copolymer comprising 51% of acrylonitrile, 48% of vinylidene chloride and 1% of sodium p-styrenesulfonate was dissolved in acetone so that the resin of the obtained resin solution was 10 0 parts by mass, adding the amount of oxidation of the metal compound (2-1) (three types of zinc oxide JIS) and antimony trioxide as the metal compound (2-2) in the amount shown in the following Table 2 Silk stock solution. 152753.doc -33- 201134992 Using a nozzle with a nozzle hole diameter of 0·10 and a number of holes, the spinning dope is broadcasted to a 30% acetone aqueous solution and solidified while being 3.3 times. The stretching ratio was extended once, washed with water at 12 °t > c, and subjected to secondary stretching at a stretching ratio of 1.3 times at 140 ° C, and then heated under water vapor (saturated water vapor) at 17 ° C. The heat treatment was carried out for 20 seconds at a relaxation ratio of 0.85 times, and further cut, thereby obtaining a halogen-containing fiber. The resulting fiber had a fineness of 7.8 dtex and a short fiber length of 64 mm with a shrinkage variation of 58%. (Production Example 2 containing a ruthenium fiber) A copolymer containing 57% of acrylonitrile, 41% of ethylene diene oxide, and 2% hydrazine of allyl sulfonate was dissolved in dimethyl group at a resin concentration of 25%. In the formamide, zinc is added as a metal compound (2") as a metal compound (2-) in an amount of 1 part by mass based on the resin of the obtained resin solution, as shown in the following Table 2. 2) The ruthenium pentoxide is prepared into a spinning dope. The spinning dope is extruded into a 55% dimercaptoamine aqueous solution using a nozzle having a nozzle aperture of 0.06 mm and a number of holes of 1 boring. While solidifying, it was once stretched at a stretching ratio of 5.6 times, washed with water and dried under 12 liters, and further dried in a humidified pressurized vapor (saturated water vapor) 13 〇 c > Ct, and the relaxation ratio became Q. In the state of no tension of 85 times, the treatment was carried out for 5 minutes, and then cut, thereby obtaining the fiber containing the fiber. The obtained fiber has a fineness of 7.8 dtex, and the short fiber with a cutting length of 64 mm has a shrinkage change of 63. % 〇 (manufacturing example 3 containing spectrin fiber) is made to contain acrylonitrile 51. Diethylene carbamide and benzoate sulphate 152753.doc -34* 201134992 1 〇 / 〇 copolymer dissolved in acetone in a resin concentration of 30%, relative to the resin resin obtained i00 parts by mass The zinc oxide (three types of zinc oxide JIS) and the antimony trioxide as the metal compound (2_2) were added as a metal compound (2-1) in an amount shown in the following Table 2 to prepare a spinning dope. The spinning dope was extruded into a 30 〇/〇 acetone aqueous solution by a nozzle having a diameter of 1 〇 mm and a number of holes of 1 ,, and was solidified while being stretched at a stretching ratio of 3.3 times. After drying at 12 ° C, it was subjected to secondary stretching at a stretching ratio of 1.3 times at 140 ° C, and then heated under water vapor (saturated water vapor) * 17 〇〇 c at a relaxation ratio of 85 times for 20 seconds. The heat treatment was followed by heat treatment, and further, the halogen-containing fiber was obtained, and the obtained fiber had a fineness of 78 dtex and a short fiber length of 64 mm, and the shrinkage variation was 61%. (Manufacturing Example 4 of the tooth-containing fiber) Include acrylonitrile 51%, vinylidene chloride 48% and The copolymer of sodium sulfonate 1% was dissolved in acetone so that the resin concentration was 3% by weight, and the amount of the resin shown in the following Table 2 was added as a metal compound in an amount of 1 part by mass based on the resin of the obtained resin solution. The tin oxide is used as the metal compound (2_2) to form a spinning dope. The spinning dope is extruded to 3〇% using a nozzle having a nozzle diameter of 0.10 mm and a number of holes of 1 boring. In the aqueous acetone solution, while solidifying, the film was stretched once at a stretching ratio of 33 times, washed with water, dried under 12 Torr, and further expanded at a stretching ratio of Μ times at i4 〇t, and then heated in water. In a vapor (saturated water vapor), a ten-second tension heat treatment was carried out at a relaxation ratio of 0.85 times at a rate of 0.85 times, and further cut, thereby obtaining a tooth-containing fiber. The resulting fiber system 152753.doc •35- 201134992 has a fineness of 7.8 dtex' cut length of 64 _ and a short fiber shrinkage of 60%. (Production Example 5 of the element-containing fiber) A copolymer containing 51% of acrylonitrile, 48% of ethylene diene and 1% of sodium p-benzoate was dissolved in acetone so that the resin concentration became 3% by weight. 1 part by mass of the resin of the obtained resin solution was added with hydrazine as shown in the following Table 2, and zinc carbonate as a metal compound (2_丨) and trioxane (4) as a metal compound (2-2) were added. Into the spinning dope. The spinning dope was extruded using a nozzle having a nozzle aperture of m mm and a number of holes of 1000 holes. In the aqueous acetone solution, while solidifying, it was once stretched at a stretching ratio of 3.3 times, washed with water, dried at 12 (TC), and secondarily stretched at a stretching ratio of 13 times at 14 Torr, and then heated. In a water vapor (saturated water vapor), the ii-containing fiber was obtained by performing a two-second tension heat treatment at a relaxation ratio of 0.85 times at a relaxation ratio of 0.85 times, thereby obtaining a fiber-containing fineness of 7.8 dtex and a cutting length of 64. The short fiber of mm has a shrinkage variation of 60%. (Manufacturing Example 6 containing Nansu fiber) The surface is solidified to one side so that 51% of acrylonitrile, 48% of ethylene oxide and 1% of sodium p-styrenesulfonate are contained. The copolymer was dissolved in acetone so that the resin concentration was 3% by weight, and the amount of addition of the resin shown in Table 2 below was added as the metal compound (2-1) to 1 part by mass of the resin of the obtained resin solution. Zinc oxide (3 types of zinc oxide jIS) and antimony trioxide as the metal compound (2-2) are used to form a spinning dope. A nozzle having a nozzle aperture of 〇.1〇mm and a number of holes of 1 boring is used. The spinning dope is extruded into a 3 〇〇 /. acetone solution 152753.doc -36· 201134992 3·3 times the stretching ratio -: under-extension, after washing, drying at 12 (TC), after stretching at l4〇°C with a stretching ratio of 3 times : In the hot water vapor (saturated water vapor), the heat treatment is carried out at a relaxation rate of 85 times at a relaxation rate of 85 times, and further cut, thereby obtaining a fiber containing the fiber. The obtained fiber system has a fineness of 7 · 8 dtex, short fiber with a length of 64 mm, with a shrinkage change of 59%. (Manufacturing Example 7 of dentate fiber) 51% of acrylonitrile, 48% of ethylene dimerate and 1% of sodium p-styrenesulfonate The copolymer was dissolved in acetone so that the resin concentration was 3% by weight, and the amount of the resin represented by the following Table 2 was added as a metal compound (2_丨) with respect to 1 part by mass of the resin of the obtained resin solution. Zinc telluride (3 kinds of zinc oxide jis) and antimony trioxide as a metal compound (2·2) to prepare a spinning dope. Using a nozzle having a nozzle aperture of 〇.1 with a number of borings of 1 boring, The spinning dope is extruded into a 30% aqueous acetone solution and solidified while being stretched by 3.3 times. Perform an extension of 'washing, dry it under 12 〇, and perform a second extension at a stretching ratio of 1.3 times at 140 C, and then heat the water vapor (saturated water vapor) to $170 〇 CT, 缓 85 times the relaxation ratio. The heat treatment was carried out for 2 minutes, and further, the film was subjected to cutting to obtain a halogen-containing fiber. The fiber obtained having a fineness of 7.8 dtex and a short fiber having a length of 64 mm had a shrinkage variation of 52%. (Production Example of Halogen-Containing Fiber) 8) A copolymer containing 51% of acrylonitrile, 48% of ethylene dimerate, and 1% of sodium p-styrenesulfonate was dissolved in acetone so that the resin of the obtained resin solution was 10 〇. The mass fraction is 152753.doc •37·201134992 % as shown in Table 2 below, and is added as the oxidation word of the metal compound (2_!) (zinc oxide JIS $ species), and as the pentoxide of the metal compound (2_2). Make a spinning dope. The spinning dope is extruded into a 3〇% acetone water-reducing towel using a nozzle having a nozzle hole of 〇1〇mm and a number of holes of i-hole, and the surface is solidified, and the stretching is performed at a stretching ratio of 3β·3 times. - Sub-extension, after washing with water at 12 (drying at TC, sub-extension at a stretching ratio of 1 > 3 times at HOt, and then heating in water vapor (saturated water vapor) at 17 (rc, 〇.85 The tempering rate of the light into the lamp 20 private tension heat treatment 'and further cut, thereby obtaining the fiber containing the dentate fiber, the quasi-serving fiber has a fineness of 7.8 dtex, and the short fiber with a cutting length of 64 mm has a shrinkage of 60%. (Production Example 9 of dentate fiber) A copolymer containing 51% of acrylonitrile, 48% of ethylene dimerate, and 1% of sodium p-styrenesulfonate was dissolved in a polypropylene resin in such a manner that the resin has a moisture content of 30%. With respect to 100 parts by mass of the resin of the obtained resin solution, zinc oxide (three types of zinc oxide) as the metal compound (21) was added in an amount shown in the following Table 2 to prepare a spinning dope. 1〇 and a nozzle with a hole number of 1000 holes, and the spinning dope is extruded into a 3〇% acetone aqueous solution, While solidifying, it is stretched once at a stretching ratio of 33 times, washed with water at 12 〇t, and once extended at a stretching ratio of 3 times at 140 ° C, heated water vapor (saturated water) In the case of steam, it was subjected to a tension heat treatment for 2 minutes at a relaxation ratio of 0.85 times, and further cut, thereby obtaining a fiber containing a fiber having a fineness of 7.8 dtex and a cutting length of 64 mm. Short fiber, shrinkage change is 55 〇 / 〇. (Production Example 10 containing halogen fiber) 152753.doc -38- 201134992 Included propiononitrile 51%, vinylidene chloride 48% and sodium styrene sodium 1 The copolymer of % is dissolved in acetone so that the resin concentration is 30%, and zinc oxide is added as the metal compound (2-1) in an amount shown by the following Table 2 with respect to 100 parts by mass of the resin of the obtained resin solution. (3 kinds of zinc oxide JIS), and as a metal compound (2-2), antimony trioxide is used to prepare a spinning dope. The spinning is performed using a nozzle having a sniffer aperture of 〇mm and a number of holes of 1 boring. The stock solution is extruded into a 3〇〇/0 acetone aqueous solution and condensed on one side. One side was stretched at a stretching ratio of 3 to 3 times, and after drying, it was dried at 1 t to 140. (: The second extension was carried out at a stretching ratio of 1.3 times, and then at 182 C, the relaxation ratio was 85.85 times. The dry heat-strength heat treatment was carried out for 2 minutes, and the cutting was carried out to obtain a fiber containing the fiber. The obtained fiber had a fineness of 7.8 dtex and a short fiber length of 64 mm, and the shrinkage variation was 47%. Manufacture example of fiber η) A copolymer containing 51% of acrylonitrile, 48% of vinylidene chloride, and 1/? of sodium styrene sulfonate was dissolved in propionate at a resin concentration of 3% by weight. 1 part by mass of the resin of the resin solution, zinc oxide (zinc oxide jis ^ species) as the metal compound (2-1) and trioxide content as the metal compound (2_2) were added in the amounts shown in Table 2 below. , made into a spinning dope. Using a nozzle having a nozzle aperture of 〇.1 〇 mm and a number of holes of 1 boring, the spinning dope was extruded into a 30% aqueous solution of propylene and solidified while being subjected to a stretching ratio of 3.75 times. After stretching, the mixture was washed with water and then dried at 185 ° C for 2 minutes at a relaxation ratio of 8 times, and then cut, thereby obtaining a fiber containing the element. 152753.doc •39- 201134992 The fiber has a fineness of 7.8 dtex and a staple length of 64 mm. The shrinkage change is 41°/. . (Production Example 12 of Halogen-Containing Fiber) A copolymer containing 51% of acrylonitrile, 48% of ethylene dimerate, and 1% of sodium p-styrenesulfonate was dissolved in acetone so as to have a resin concentration of 30%. 1 part by mass of the resin of the obtained resin solution, zinc oxide (three types of zinc oxide jis) as a metal compound (2-1) and a metal compound (2-2) were added in an amount shown in the following Table 2. Antimony trioxide is made into a spinning dope. Using a nozzle having a nozzle aperture of 〇.〇6 mm and a number of holes of 1 boring, the spinning dope was extruded into a 30% acetone aqueous solution and solidified while extending at a magnification of 3·3 times. Perform one extension, dry after washing at 12 ° C. 'Secondary extension at 1.3 times extension at 140 ° C, and then heat the water vapor (saturated water vapor) at 17 ° C to 0.85. The tempering magnification was subjected to a ten-second intense heat treatment, and further cut, thereby obtaining a halogen-containing fiber. The obtained fiber system had a fineness of 丨·7 dtex and a short fiber of 64 mm in length had a shrinkage variation of 59%. (Production Example 13 of the element-containing fiber) The copolymer containing 51% of acrylonitrile, 48% of ethylene dimerate, and sodium p-styrenesulfonate was dissolved in acetone so as to have a resin concentration of 30%, relative to the obtained resin. 1 part by mass of the resin of the solution, zinc oxide (three kinds of zinc oxide JIS) as a metal compound (2-1), and trioxide as a metal compound (2·2) were added as an addition amount shown in the following Table 2锑, made into a spinning dope. Using a nozzle having a nozzle aperture of 0.14 mm and a number of holes of 1 boring, the spinning dope was extruded into a 30% aqueous acetone solution to solidify it, and a 152753.doc • 40-201134992 surface was 3.3. The stretching ratio is extended once, washed with water under i 2 〇艽, and then subjected to secondary stretching at a stretching ratio of 1.3 times at 140 ° C, and then heated under water vapor (saturated water vapor) at 17 Torr. The tensin-containing fiber was obtained by performing a ten-second intense heat treatment at a relaxation ratio of 0.85 times and further cutting. The obtained fiber had a fineness of 17 dte}i and a staple fiber length of 64 claws, and the shrinkage variation was 58%. (Production Example 14 of dentate-containing fibers) 51% of acrylonitrile, 48% of vinylidene chloride, and 1 of sodium p-styrenesulfonate were contained. The copolymer of the oxime is dissolved in acetone so that the resin concentration is 3% by weight, and is added as the metal compound (2-2) in an amount of addition shown in Table 2 below with respect to 100 parts by mass of the resin of the obtained resin solution. Antimony trioxide is made into a spinning dope. Using a nozzle having a nozzle aperture of 〇.1〇mm and a number of holes of 1000 holes, the spinning dope was broadcasted to a 30 〇/〇 acetone aqueous solution and solidified while performing an extension at a stretching ratio of 3.3 times. After washing with water, it was dried at 12 (TC), and then subjected to secondary stretching at a stretching ratio of 1.3 times at 140 ° C. After heating at a temperature of 17 ° C in saturated steam (saturated water vapor), a relaxation ratio of 0.8 times was used. After 20 seconds of intense heat treatment and further cutting, a halogen-containing fiber was obtained, and the obtained fiber had a fineness of 76 dtex and a short length of 64 mm. The shrinkage of the obtained fiber was cut during the measurement. It is impossible to measure. (Production Example 15 of the element containing fiber) The copolymer containing 51% of acrylonitrile, 48% of vinylidene chloride, and 1% of sodium p-styrenesulfonate was dissolved in such a manner that the resin concentration became 30%. In acetone, 1 part by mass of the resin of the obtained resin solution was added as 252753.doc -41 - 201134992 as shown in the following Table 2, and zinc oxide (zinc oxide jis ^ as a metal compound (2_1}) was added. Species) as a metal compound (2-2) Strontium trioxide is used to make a spinning dope. The spinning dope is extruded into a 3〇〇/0 acetone aqueous solution using a nozzle having a nozzle diameter of 010 mm and a number of holes of 1 boring, and is solidified while being solidified. The mixture was extended once at a stretching ratio of 5.9 times, washed with water at 120 ° C, and then subjected to dry heat stress treatment at a relaxation ratio of 0.85 times at 170 ° C for 2 minutes, and further cut, thereby obtaining The fiber obtained has a fiber denier of 7.8 dtex and a short fiber length of 64 mm, and the shrinkage variation is 67%. (Production Example 16 containing dentate fiber) 57% of acrylonitrile-containing ethylene oxide The copolymer of 4% by weight and 3% of allyl sulfonate was dissolved in dimethyl decylamine in such a manner that the resin concentration became 245%, and 1 part by mass of the resin of the obtained resin solution, as shown in the following table 2 Addition amount, adding antimony trioxide as the metal compound (2_2) to prepare a spinning dope. Using a nozzle having a nozzle aperture of 0.06 mm and a number of holes of 100,000, the spinning dope is extruded to 55%. In the aqueous solution of dimethyl hydrazine, one side is solidified, and one side is 5 6 times extension ratio, one extension, water washing, drying at 13 ° C, and further heat treatment at 115 ° C in a damp heat-pressurized vapor (saturated water vapor) at a relaxation ratio of 0 85 times for 15 minutes. Further, the yarn was cut to obtain a fiber containing γ. The obtained fiber had a fineness of 1.9 dtex and a short fiber having a length of 38 mm, and the shrinkage variation was 68%. (Production Example j of a halogen-containing fiber) Acetonitrile 57%, diethylene oxide 41% and allyl sulfonate 2〇/〇152753.doc •42· 201134992 /, the polymer is dissolved in the dimercapto by the resin concentration of 25% In the amine, with respect to 100 parts by mass of the resin of the obtained resin solution, zinc p-toluate as a metal compound (2·丨) and ruthenium pentoxide as a metal compound (2_2) are added as shown in Table 2 below. , made into a spinning dope. Using a nozzle having a nozzle aperture of 0.06 mm and a number of holes of 1 boring, the spinning dope was extruded into a 55% aqueous solution of dimethylguanamine to solidify it, and the surface was 5.6 times. The stretching ratio is extended once, and after washing with water, it is dried at 12 (TC, and then in a moist heat-pressurized vapor (saturated water vapor) 125 lt;), and the tempering ratio is 0.85 times in a state of no tension for 2 minutes. The relaxation treatment was further carried out to obtain a halogen-containing fiber. The obtained fiber had a fineness of 丨.7 dtex 'short fiber having a cut length of 64 mm, and the shrinkage variation was 85%. (Manufacturing Example 18 of a halogen-containing fiber) The copolymer containing 50% of acrylonitrile, 49% of ethylene, and 苯乙烯5〇/〇 of styrenesulfonate was dissolved in acetone so as to have a resin concentration of 30%, and 100 parts by mass or less of the resin of the obtained resin solution. Addition of 堇' added as a metal compound (2-1), zinc stannate, and polyglycidyl methacrylate containing an epoxy group (weight average molecular weight: 40,000) Raw liquid. Also, in the above spinning original "TINUVIN1577FF" (2-(4,6-diphenyl-1,3,5-tris-2-yl)), manufactured by Ciba Specialty Chemicals Co., Ltd., was added to the liquid, and the nozzle aperture was 〇. .1 nozzle with 12 pupils, the spinning dope is extruded into a 25% acetone aqueous solution, and is solidified while stretching once at a stretching ratio of 2.18 times. After washing, U5<;>c proceeded to 152753.doc •43·201134992, and dried at 145 ° C, then extended twice at a stretching ratio of 2.75 times 'and further at 170. (:, at a relaxation ratio of 0.92 times After 3 minutes of dry heat and heat treatment, and further cutting, the fiber containing the fiber was obtained. The obtained fiber has a fineness of 2.2 dtex and a short fiber length of 51 mm, and the shrinkage variation was 160% » (containing halogen fiber) Production Example 19) A copolymer comprising 52% of acrylonitrile, 46.8% of ethylene glycol and 1.2% of sodium styrene was dissolved in C-propane in a manner to have a resin concentration of 30%, relative to the obtained resin solution. 100 parts by mass of the resin, added as a metal in the amount shown in Table 2 below The zinc hydroxystannate of the compound (2-1) and the antimony trioxide of the metal compound (2-2) are used as a spinning dope. A nozzle having a nozzle aperture of 〇.〇8 mm and a number of holes of 15,000 holes is used. The spinning dope was extruded into a 38% aqueous acetone solution and solidified while being stretched once at a stretching ratio of 22 MPa. After washing with water, it was dried at 12 Torr and then at 15 ° C. The stretching was carried out at a stretching ratio of 3.0 times, and further, a dry heat treatment at a relaxation ratio of 0.80 times at a relaxation ratio of 0.80 times was carried out at 17 ° C to further perform cutting, thereby obtaining a fiber containing γ. The resulting fiber had a fineness of 3 dtex and a short fiber length of 38 mm and a shrinkage change of 73%. (Production Example 2 of Halogen-Containing Fiber) A copolymer containing 52% of acrylonitrile, 47% of ethylene diethylene oxide, and 1% of sodium methyldithioacetate was dissolved in dimethyl group at a resin concentration of 25%. In the formamide, the amount of the resin ruthenium of the obtained resin solution was added as the metal compound (η) in the amount of addition shown in Table 2 below, and 152753.doc 201134992 was used as the metal compound (2-2). ) pentoxide, made into a spinning dope, using a nozzle having a nozzle aperture of 0.07 mm and a number of holes of 30,000 holes. The spinning dope is extruded into a 50% aqueous solution of dimethylformamide to solidify it. One side was stretched at a stretching ratio of 8.0 times, washed with water at i3 (drying under rc), and then in a damp heat-pressurized vapor (saturated water vapor) at 120 〇C, and the relaxation ratio was 0.8 times in a state of no tension. The yarn was subjected to a relaxation treatment for 15 minutes to carry out cutting, thereby obtaining a fiber containing γ. The obtained fiber had a fineness of 7.8 dtex and a short fiber having a length of 64 mm, and the shrinkage variation was 72%. Production Example 21) Acrylonitrile was contained. The copolymer of 48% of gaseous ethylene and 2% of sodium decylallylsulfonate was dissolved in acetone so that the resin concentration became 30%, and the raw material of the spinning and bismuth was prepared. The nozzle aperture was 〇min and the number of holes was 30,000. The nozzle of the hole, the spinning dope was extruded into a 30% aqueous acetone solution, and the solidified surface was stretched once at a stretching ratio of 3.3 times, washed with water and dried at 135 ° C, and then at 145 ° > (:, the second extension is carried out at a stretching ratio of 2 to 49 times, and further, i5 minutes of relaxation is performed in a state where the relaxation ratio becomes 〇·7 times in a state of no tension in the wet heat-pressurized vapor (saturated water vapor) U5t. After the treatment and the relaxation treatment, it is dried for 1 minute in the crucible 5, and then stretched until the crimping is eliminated, and further cut, thereby obtaining the fiber containing the cellulose. The obtained fiber has a fineness of 7 8 I, cut into short fibers of 64 claws. The shrinkage fluctuation of the obtained fiber was not measured because it was cut at the time of measurement. (Production Example 22 containing _-fibers) 152753.doc •45- 201134992 Contains 51% acrylonitrile, 48% ethylene oxide and para-benzene The copolymer of 1% of sodium sulfonate was dissolved in acetone so that the resin concentration was 3% by weight, and 100 parts by mass of the resin of the obtained resin solution was added as a metal compound (2d) in an amount shown in Table 2 below. Zinc oxide (3 kinds of zinc oxide Jls) and antimony trioxide as the metal compound (2-2) are used as a spinning dope. The nozzle aperture is 〇·1〇mm and the number of holes is 1 boring. The nozzle was extruded into a 30 〇/〇 acetone aqueous solution and solidified while being stretched once at a stretching ratio of 3.3 times. After washing with water, it was dried to '140. (: After the second extension was carried out at a stretching ratio of 1.3 times, the dry heat-strength heat treatment was performed at a relaxation ratio of 0.85 times at 170 C for 2 minutes, and further cutting was performed, whereby the fibers containing the teeth were obtained. The short fiber with a fineness of 7.8 dtex and a length of 64 mm is cut, and the shrinkage variation is 70%. The shrinkage variation of the 'followed fiber' is measured as follows. (Method for measuring fiber shrinkage) The halogen-containing fiber produced in the example is 3333 dtex (after a taxi), using about 5 mm, using tma (thermal stress strain measuring device [manufactured by Seiko Instrument Co., Ltd., trade name ^ TMA/SS150C"], using gas: Nitrogen, gas flow rate: 3 〇 L / min 'heating rate: 2 〇 eC / min 'load 18 mN) is measured. If the initial sample length is set to X ' and the sample length at any temperature is set to γ, then the fiber The shrinkage ratio is represented by the following formula: The so-called functional fiber of the present invention has a temperature of from 50 〇 c to 3 〇〇 ° c under a load of 0.0054 mN/dtex, and is not cut and remains. 〇〇〇54 mN/dtex load When the temperature 152753.doc -46·201134992 degrees is increased from 50 ° C to 300 ° C ' while the fiber shrinkage ratio (also referred to as shrinkage ratio in the present specification) is measured by the above measurement method, the present invention contains The dentate fiber is not cut and remains: Fiber shrinkage ratio (°/.) = 1 00 - [(100 χΥ) / Χ]. (Method for calculating shrinkage fluctuation) The temperature is increased from 50 ° C to 300. (: The change in shrinkage at the time refers to the difference between the highest point (α%) and the lowest point (p%) of the fiber shrinkage rate in the temperature range of 5 (rc to 3 〇〇〇c) in the measurement of the fiber shrinkage rate. In the measurement of the shrinkage ratio of the fiber, the shrinkage variation is set to be infinite when the fiber is cut. One of the manufacturing examples 1 to 22 - female it # position, east, T of the person extension ratio, twice The spinning conditions such as the stretching ratio, the tempering ratio in the heat, and the total stretching ratio are also shown in the following Table 2, the extension ratio of the stretching extension H, the second extension ratio, and the relaxation ratio at the time of treatment. Value. 152753.doc -47. 201134992

(N 152753.doc S 塄 00 … m v〇 s § 〇s <N »〇 s V) Os V) 00 »〇 5 00 v〇 <n 00 P cs 〇 卜 墀 S» ^ m rn ο W-ϊ ΓΛ o m ro d m m 〇 cn 〇 CN m m o <N <N CN m m d cn ΡΊ d cn cn o CN W"1 (Ν fn ο in •«μ ^Τί ψ-^ (N W 峨 揉 溫度 CC) ο 〇 o o o 〇 VMM o o (N 00 οο o o o 〇 iT) CS ο V-H ο 〇 卜 sg sg sg sg sM sg sg sg ϊ§ ϊ§ 狳 鉍 紅 鉍 鉍 鉍 絲 躲 躲 揉· m 戚 4i 癍 揉 揉- 戚 4ί 戚 戚 4ί 戚 戚 瘦 暌 喫 m m 45? 祐 m m 瘐 m 祐 總延伸 倍率 (倍) \Τ) Ό rn v〇 — κη v〇 rn Ό ΓΛ KTi v〇 ΓΊ yn 〇 r^ Μ-) VD r^i VO CO κη v〇 ΓΛ vo ΓΛ ο cn Ό rn yn v〇 rn cn S uS ^D — ν〇 甘· <N i〇 … η ο vd JO in ^> ΓΟ 熱處理 緩和倍率 (倍) 00 00 in 00 00 u-> 00 00 w-> 00 wo 00 00 00 οο 00 in 00 00 in oo 00 »0 00 (Ν On 〇〇 00 卜 tn 00 d d o ο o o ο o o d ο o 〇 〇 d ο ο Ο 〇 ο 〇 d -a- jn CN 2次延 倍率 (倍) rn o ΓΛ cn ΓΟ rn r-· rn rn cn »—· ΓΊ ο rn rn cn· p p ρ 〇 cn ο 寸 (N ΓΛ jn ro 1次延 倍率 (倍) ro CO VO CO cn m ΓΛ m co m rn m rn cn ΓΛ ro m m cn CO CO m 一 Os VO ν〇 … <N <Ν ο 00 m rn cn rn /*—S (Ν -¾ 〇H U"> o 寸 V) a 〇 1 <η »r> yn Ο »-^ 1 Ο 1 <n 's—✓ 娥 璜 璜 璜 璜 璜 珑 璜 缋 丄) *τ· -O Λ2 λΟ jJ jJ A3 jJ *τ- λ3 A3 JJ aJ a) 〇J XJ JJ irf jJ *t- <0 iisf J3 Η| 'Ί >Ί 、丨1 >Ί »1 、丨1 >Ί '丨i 、'i 'Ί ,丨1 ,丨1 Η >Ί Η u| /—N φΐ ^ CN 〇 s ο -¾ φ! (N (N 〇 <N (N CN 〇 o v^ CS <N (Ν <Ν CN CN 1 ο 1 T·^ ra 1 <N '·-^ *4〇 /—S 化合物名 竑 對甲苯磺酸鋅 敢 璨 竑 欺 欺 4 竑 欺 對曱苯磺酸鋅 敢 敢 t 竑 Jj 03 A3 JJ JJ JJ JJ JJ 03 1 1 5| 璨 jD 1 -L) •x- «f iSif 一 iiSif 二 4〇 9 4〇装·被 <n W"» in i〇 ^Τ) r^m yn m i〇 in »〇 (S v-i (N 龄 Vt *— <N m yn ^O 卜 00 On Ο (N m 寸 v〇 卜 00 ON <N CS ·48· 201134992 (單纖維強度) 依據JIS L 10 1 5測定上述製造例1、丨丨、1 5、16、18〜2 1 之含齒素纖維及Protex-M之單纖維強度。將其結果示於下 述表3中。 [表3] 含鹵素纖維 製造例 1 11 15 16 18 19 20 21 Protex-M 單纖維強度 (cN/dtex) 0.97 0.92 1.4 1.65 2.01 1.95 2.2 3 2.1 (實施例1〜15、17〜33) 將以下所示之纖維以成為下述表4所示之預定混率之方 式加以混合,藉由梳棉而開纖後,利用通常之熱溶著方 式,製作預定之單位面積重量之熱黏合不織布《使用製造 例1〜13之含鹵素纖維作為含鹵素纖維,使用通用之聚酿纖 維即東麗(TORAY)公司製造之商品名「Tet〇ron」(纖度為6 dtex,切割長為51 mm,LOI值為21,以下亦稱作 reg.PET)、及熱熔著聚酯纖維即東麗(TORAY)公司製造之 商品名「Safmet」(纖度為4.4 dtex,切割長為5 1 mm,熔 點為110°C,LOI值為20,以下有時稱作meh PET)作為聚 酯系纖維,使用含有矽成分之再生纖維素纖維即Daiwabo Rayon公司製造之商品名「FR Corona」(纖度為2.2 dtex, 切割長為5 1 mm,LOI值為25,矽元素之含量為14質量%, 以下亦稱作FR螺縈)、含有鱗系難燃劑之再生纖維素纖維 即Lenzing公司製造之商品名「Lenzing FR」(纖度為2.2 dtex ’ 切割長為 51 mm,LOI 值為 28)、自 Jones Fiber 152753.doc • 49- 201134992(N 152753.doc S 塄00 ... mv〇s § 〇s <N »〇s V) Os V) 00 »〇5 00 v〇<n 00 P cs 〇卜墀S» ^ m rn ο W- ϊ ΓΛ om ro dmm 〇cn 〇CN mmo <N <N CN mmd cn ΡΊ d cn cn o CN W"1 (Ν fn ο in •«μ ^Τί ψ-^ (NW 峨揉temperature CC) ο 〇 Ooo 〇VMM oo (N 00 οο ooo 〇iT) CS ο VH ο 〇 s sg sg sg sg sm sg sg sg ϊ§ ϊ§ 狳铋红铋铋铋丝躲躲揉 · m 戚4i 癍揉揉- 戚4ί戚戚4ί 戚戚 暌 暌 eat mm 45? 佑mm 瘐m 佑 total extension ratio (times) \Τ) rn rn v〇— κη v〇rn Ό ΓΛ KTi v〇ΓΊ yn 〇r^ Μ-) VD r^i VO CO κη v〇ΓΛ vo ΓΛ ο cn Ό rn yn v〇rn cn S uS ^D — ν〇甘· <N i〇... η ο vd JO in ^> 热处理 Heat treatment relaxation ratio (times) 00 00 in 00 00 u-> 00 00 w-> 00 wo 00 00 00 οο 00 in 00 00 in oo 00 »0 00 (Ν On 〇〇00 卜 tn 00 ddo ο oo ο ο ο 〇〇 〇 - - - - 2 2 2 2 2 ρ 〇cn ο 寸 (N ΓΛ jn ro 1 time extension ratio (double) ro CO VO CO cn m ΓΛ m co m rn m rn cn ΓΛ ro mm cn CO CO m an Os VO ν〇... <N <Ν ο 00 m rn cn rn /*—S (Ν -3⁄4 〇H U"> o inch V) a 〇1 <η »r> yn Ο »-^ 1 Ο 1 <n 's-✓ 娥璜璜璜璜璜珑璜缋丄) *τ· -O Λ2 λΟ jJ jJ A3 jJ *τ- λ3 A3 JJ aJ a) 〇J XJ JJ irf jJ *t- <0 iisf J3 Η| 'Ί >Ί ,丨1 >Ί »1 ,丨1 >Ί '丨i , 'i 'Ί ,丨1 ,丨1 Η >Ί Η u| /—N φΐ ^ CN 〇s ο -3⁄4 φ! (N (N 〇<N (N CN 〇ov^ CS <N (Ν <Ν CN CN ο 1 T·^ ra 1 <N '·-^ *4〇/-S Compound name 竑 p-toluene sulfonate zinc dare to bully 4 竑 曱 曱 曱 j j j j j Jj 03 A3 JJ JJ JJ JJ JJ 03 1 1 5| 璨jD 1 -L) • x- « f iSif one iiSif two 4〇9 4 armored · by <n W"» in i〇^Τ) r^m yn mi〇in »〇(S vi (N age Vt *— <N m yn ^O 00 00 Ο (N m inch v 〇 00 ON < N CS · 48· 201134992 (single fiber strength) According to JIS L 10 1 5, the above manufacturing example 1, 丨丨, 1, 5, 16, 18 to 2 1 The fiber strength of the dentate fiber and Protex-M. The results are shown in Table 3 below. [Table 3] Halogen-containing fiber Production Example 1 11 15 16 18 19 20 21 Protex-M Single fiber strength (cN/dtex) 0.97 0.92 1.4 1.65 2.01 1.95 2.2 3 2.1 (Examples 1 to 15, 17 to 33) The fibers shown are mixed so as to have a predetermined mixing ratio as shown in the following Table 4, and after being opened by carding, a heat-bonded nonwoven fabric having a predetermined basis weight is produced by a usual heat-dissolving method. The halogen-containing fibers of Examples 1 to 13 are used as halogen-containing fibers, and the general-purpose fiber-reinforced fiber, that is, the product name "Tet〇ron" manufactured by Toray Co., Ltd. (denier 6 dtex, cutting length 51 mm, LOI value) is used. 21, hereinafter also referred to as reg.PET), and the hot-melt polyester fiber, manufactured by TORAY, under the trade name "Safmet" (denier of 4.4 dtex, cutting length of 51 mm, melting point of 110 °C) The LOI value is 20, and the following is sometimes referred to as meh PET. As the polyester fiber, the regenerated cellulose fiber containing the bismuth component, the product name "FR Corona" manufactured by Daiwabo Rayon Co., Ltd. (denier of 2.2 dtex, the cutting length is 5 1 mm, the LOI value is 25, and the content of the lanthanum element is 14% by mass. The following is also known as FR screw), a regenerated cellulose fiber containing a scale-based flame retardant, which is manufactured by Lenzing, under the trade name "Lenzing FR" (denier of 2.2 dtex 'cut length 51 mm, LOI value of 28), Jones Fiber 152753.doc • 49- 201134992

Products公司獲得之塗布右雜丨处t 々有難燃劑之後加工難燃纖維素纖 維即後加工嫘縈(纖度為3 3 ^ Λ 〇 u dtex,切割長為64 mm,[〇1值 為33)、及Dupont公司製造夕龙。 「 适之商。〇名「Nomex」(纖度為2.2 dtex,切割長為50 mm,lot枯*a认人 值為30)作為含鹵素纖維以外 之難燃性纖維。 (實施例16) 將利用上述製造例1所示之製Α古 方法而製作之含鹵素纖 維、作為聚醋系纖維之通用平祕、地B由__ 通用眾S曰纖維即東麗(T〇RAY)公司 製造之商品名「Tetoron」' 及作為含函素纖維以外之難炒 性纖維™紫’以成為下述表4所示之預定混率之方式 加以混合’藉由梳棉而開纖後’利用通常之針刺方式製作 預疋之單位面積重量之針刺不織布。 (比較例1、2、4〜20) 將以下所不之纖維以成為下述表5所示之預定混率之方 式加以混合,藉由梳棉而開纖後,利用通常之熱熔 式,製作預定之單位面積重量之熱黏合不織布。使用製造 例1 I4〜22之含鹵素纖維及Kaneka股份有限公司製造之商 品名「IWex-M」(纖度為2.2 dtex,切割長為Μ _)作為 含齒素纖維,使用通用之聚醋纖維即東麗(t〇Ray)公司製 造之商品名「Tet〇ron」、及熱熔著聚醋纖維即東麗 (TORAY)公司製造之商品名「Safmet」作為聚醋系纖維, 且使用FR螺繁作為含函素纖維以外之難燃性纖維。 (比較例3) 藉由梳棉將100質量%iFR嫘縈開纖後,利用通常之針 152753.doc 201134992 刺方式t作預疋之單位面積重量之針刺不織布。 使用實施例及比較例之不織布,製作如下所述之試驗 體,§f價難燃性,將其結果示於下述表4及5中。 <迷你床墊型試驗體之製作方法> 將迷如、床墊型試驗體之結構示於圖丨〜4中。首先,使用 尼龍、”糸 以2〇 cm之街縫間隔,將2片縱45 cm、橫60 cm、厚1.9 cm、密度22 kg/m3之聚胺基甲酸酯發泡體 l(Toyo Rubber Industry公司製造,類型 36〇s),丨片縱45 cm、橫60 cm、厚i,27 cm、密度22 kg/m3之聚胺基甲酸酯 發泡體2(Toyo Rubber Industry股份有限公司製造,類型 360S) ’ 1片實施例或比較例之不織布3、及丨片作為外層之 表面原材料4之聚醋/聚丙烯製織布(單位面積重量ι2〇 g/m2)绗縫成如圖以般重疊之結構物,製作如圖lB所示之 板部6。繼而,使用尼龍絲5,以5 em之绗縫間隔,將μ 上述不織布3、1片作為外層之表面原材料4之聚酯/聚丙烯 製織布(單位面積重量為120 g/m2)绗縫成如圖2八般重疊之 結構物,製作如圖2B所示之縱22 cm、橫212 邊緣部 7。繼而’使用尼龍絲5 ’以2〇 cm之绗縫間隔,將i片上述 不織布3、1片作為外層之表面原材料4之聚酯/聚丙烯製織 布(單位面積重量為120 g/m2)绗縫成如圖2A般重疊之結構 物’製作如圖2C所示之縱45 cm、橫60 cm之底部8。進 而’於縱45 cm、橫60 cm、高20 cm之螺旋彈簧16上搭載2 片縱45 cm、橫60 Cm、厚1.27 cm、密度22 kg/m3之聚胺基 甲酸酯發泡體(Toyo Rubber Industry股份有限公司製造, 152753.doc 201134992After the coating of the right chowder at the product, the processing of the flame retardant cellulose fiber after the processing of the flame retardant is processed (the fineness is 3 3 ^ Λ d u dtex, the cutting length is 64 mm, [〇1 value is 33) And Dupont Company manufactures Xi Long. "Appropriate quotient. The name "Nomex" (denier of 2.2 dtex, cut length of 50 mm, and bit dryness *a value of 30) is used as a flame retardant fiber other than halogen-containing fibers. (Example 16) A halogen-containing fiber produced by the above-described production method shown in the above-mentioned Production Example 1 was used as a general flat for the polyester fiber, and the ground B was made of __ GM S-fiber, Toray (T 〇RAY) The product name "Tetoron" manufactured by the company and the hard-to-scrape fiber TM purple other than the functional fiber are mixed in such a manner as to be the predetermined mixing ratio shown in Table 4 below. After that, the needle-punched non-woven fabric of the pre-twisted unit weight is produced by the usual acupuncture method. (Comparative Examples 1, 2, 4 to 20) The following fibers were mixed so as to have a predetermined mixing ratio as shown in the following Table 5, and after being opened by carding, they were produced by a usual hot melt method. A predetermined heat-bonding non-woven fabric per unit area weight. The halogen-containing fiber of Production Example 1 I4 to 22 and the trade name "IWex-M" (having a fineness of 2.2 dtex and a cut length of Μ _) manufactured by Kaneka Co., Ltd. were used as the dentate-containing fiber, and a general-purpose polyester fiber was used. The product name "Tet〇ron" manufactured by Toray (T〇Ray) Co., Ltd., and the hot-melt polyglycol fiber, the product name "Safmet" manufactured by Toray Co., Ltd., is used as a polyester fiber, and FR screw is used. It is a flame retardant fiber other than the fiber containing the element. (Comparative Example 3) After 100% by mass of iFR was opened by carding, a needle-punched nonwoven fabric having a basis weight of a predetermined amount was prepared by a conventional needle 152753.doc 201134992. Using the nonwoven fabrics of the examples and the comparative examples, the test bodies described below were produced, and the flammability was § f, and the results are shown in Tables 4 and 5 below. <Production Method of Mini Mattress Type Test Body> The structure of the mattress type test body is shown in Figs. First, use nylon, "糸" with a gap of 2 〇cm, two sheets of 45 cm long, 60 cm horizontal, 1.9 cm thick, and a density of 22 kg/m3 of polyurethane foam (Toyo Rubber) Produced by Industry, type 36〇s), polyurethane 45 cm, 60 cm horizontal, thickness i, 27 cm, density 22 kg/m3 polyurethane foam 2 (manufactured by Toyo Rubber Industry Co., Ltd. , type 360S) '1 piece of the non-woven fabric 3 of the embodiment or the comparative example, and the crepe sheet as the outer surface material 4 of the polyester/polypropylene woven fabric (weight per unit area ι 2 〇 g / m 2 ) quilted into the figure For the structure which is superimposed, a plate portion 6 as shown in Fig. 1B is produced. Then, a nylon yarn 5 is used, and the above-mentioned non-woven fabric 3 and 1 are used as the outer surface material 4 of the outer polyester 4 at a quilting interval of 5 em. A polypropylene woven fabric (having a weight per unit area of 120 g/m2) was quilted into a structure as shown in Fig. 2, and a length of 22 cm and a width 212 edge portion 7 as shown in Fig. 2B were produced. 5 'The polyester/polypropylene woven fabric of the surface material 4 of the outer layer is made of 3 pieces of the above non-woven fabrics at a quilting interval of 2 〇 cm. The weight of the surface area is 120 g/m2) quilted into a structure as shown in Fig. 2A. A bottom portion 8 of 45 cm in length and 60 cm in width as shown in Fig. 2C is produced. Further, '45 cm in length and 60 cm in width, The coil spring 16 with a height of 20 cm is equipped with two polyurethane foams of 45 cm in length, 60 cm in width, 1.27 cm in thickness and 22 kg/m3 in density (Manufactured by Toyo Rubber Industry Co., Ltd., 152753.doc) 201134992

之方式,於其上 帶(單位面積重量為2〇〇 g/m2, 置邊緣部7,且於底面配置底部 10而縫合成沿著螺旋 圖3所示般,利用聚丙烯製縫邊 寬36 mm)9與克維拉絲1〇, 4所示之迷你床墊。 <大型床墊型試驗體之製作方法> 將板部6與邊緣部7、邊緣部7與底部8進行縫合,製作如圖 將大型床墊型試驗體之結構示於圖5〜8中。首先,使用 尼龍絲5,以20 cm之绗縫間隔, cm、厚 1.27 cm、密度 22 kg/m3. 間隔,將2片縱190 cm、橫97 kg/m3之聚胺基甲酸酯發泡體 ll(T〇y〇 Rubber Industry股份有限公司製造,類型36〇s),In the manner of the belt (the weight per unit area is 2〇〇g/m2, the edge portion 7 is placed, and the bottom portion 10 is disposed on the bottom surface and sewn to be along the spiral pattern 3, and the width of the seam is made of polypropylene 36 Mm) 9 with a mini mattress shown in the 1st, 4th. <Manufacturing Method of Large Mattress Type Test Body> The plate portion 6 and the edge portion 7, the edge portion 7 and the bottom portion 8 are sewn together, and the structure of the large mattress type test body is shown in Figs. 5 to 8 as shown in the figure. . First, use nylon wire 5 to foam 2 pieces of 190 cm long and 97 kg/m3 of polyurethane at intervals of 20 cm, cm, 1.27 cm thick and 22 kg/m3. Body ll (T〇y〇Rubber Industry Co., Ltd., type 36〇s),

成如圖5A般重疊之結構物,製作如圖5B所示之板部12。 繼而,使用尼龍絲5,以5 Cm之绗縫間隔,將丨片上述不織 布3、1片作為外層之表面原材料4之聚酯/聚丙烯製織布(單 位面積重量為120 g/m2)绗縫成如圖6A般重疊之結構物,製 作如圖6B所示之縱22 cm、橫576 Cm之邊緣部13。繼而, 使用尼龍絲5 ’以20 cm之绗縫間隔,將1片上述不織布3、 1片作為外層之表面原材料4之聚醋/聚丙烯製織布(單位面 積重量為120 g/m2)衍縫成如圖6A般重疊之結構物,製作如 圖6C所示之縱190 cm、橫97 cm之底部Η。進而,於縱19〇 cm、橫97 cm、高20 cm之螺旋彈簧17上搭載縱19〇 cm、橫 152753.doc -52- 201134992 97 cm、厚1 cm之聚醋製毛氈ls(單位面積重量為12〇〇 g/m2) ’以表面原材料4成為外側之方式,於其上表面配置 板部12,於側面配置邊緣部13,且於底面配置底部14,邊 緣部13係利用克維拉絲10而縫合成沿著螺旋彈簧17之側面 之筒狀,如圖7所示般,利用聚丙烯製縫邊帶(單位面積重 量為200 g/m2,寬40 mm)9與克維拉絲1〇,將板部^與邊 緣部13、邊緣部13與底部14進行縫合,製作如圖8之大型 床墊。 (難燃性評價方法) &lt;燃燒假疋時之屏障背面溫度&gt; 厚10 mm之珠光板之中 準備於縱200 mm、橫200 mm 心形成有直徑55 mm之孔者,於其上放置實施例或比較例 之不織布’製作以夾子固定4邊以使加熱時不織布不收縮 之„式料。垂直固定該試料,相對於實施例或比較例之不織 布之面於自β式料起至水平方向42 mm之部位垂直設置美 國的床之燃燒試驗方法16(:1^1633的床侧面試驗用τ型燃 燒器。燃燒氣體係使用丙烷氣體,於氣體壓力為ι〇; kPa、軋體流量為6 6 L/min之條件下接焰9〇秒,利用非接 觸式紅外線放射溫度計(Anritsu Meter公司製造,^叫, 對此時之不織布中央部之接焰側與相反側之溫度(以下, 亦可簡稱為背面溫度)進行測定。利用本測定法所得之屏 障背面溫m係指防透熱性優異。用於床塾之胺基甲 I酉曰發A體通常多形成與屏障*織布接觸之結構。該胺基 甲馱知發泡體之熱分解多開始於約220〜300。(:,此時釋放 152753.doc •53- 201134992 出可燃ι·生之分解氣體。因此,就抑制胺基甲酸醋發泡體本 身之燃燒而且抑制床墊結構物整體之燃燒之觀點而言, 更佳為屏障背面溫度低,即與屏障接觸之胺基甲酸醋發泡 體溫度低’進而更佳為該屏障背面溫度低於分解溫度。再 者’屏障背面溫度係將最大溫度之個位四捨五入而記載。 &lt;迷你床墊型試驗體評價法&gt; 依據美國的床之燃燒試驗方法16(:1^1633之燃燒試驗方 法而實施。若對美國16CFR1633之床之燃燒試驗方法加以 簡單說明’則為如下之試驗方法:於自床之上表面起至垂 直方向39 mm之部位水平設置1字型燃燒器,且於自侧面 起至水平方向42 mm之部位垂直設置τ字型燃燒器,同時 開始接焰’使上表面接焰7〇秒,使側面接焰5〇秒。燃燒氣 ,係使用丙燒氣體’氣體壓力為1G1仍,上表面之燃燒 态之氣體机置為12.9 L/min.,側面之燃燒器之氣體流量為 6·6 L/min.。難燃性之評價係以如下方式進行。 A等級之合格:利用上述試驗方法進行試驗時,自媳, 且曝露於火中之部分未產生龜裂或孔洞。 B等級之合# :進行相同試驗時,自媳、,但於曝露於火 中之部分產生未達1 cm之龜裂。 C等級之合格:進行相同試驗時,自熄,但於曝露於火 中之部分產生1 cm以上之龜裂。 ^等級之合格:進行相同試驗時,内部易燃性胺基甲酸 酯—度著火,但立即熄滅,最終自熄。 不合格:進行相同試驗時,内部易燃性胺基曱酸酯著 152753.doc -54- 201134992 火,強制性滅火,中止試驗。 &lt;迷你床墊型試驗體之板部10分鐘後之延燒面積評價&gt; 依據美國的床之燃燒試驗方&amp;16CFR1633之燃燒試驗方 法’自上表面實施70秒之預定之燃燒器接焰,並自側面實 施50秒之預定之燃燒器接焰。以百分率表示測試開始1〇分 鐘後之板部的延燒部分(燃燒而碳化之部分)面積相對於板 部整體面積之比。數值越低,表示延燒面積越小,滅火 性、難燃性越優異。即便於1 〇分鐘以内1 〇〇%燃燒之情形 時,亦評價為100。/〇。又,於内部易燃性胺基甲酸酯著 火,強制滅火而中止試驗之情形時,評價為無法計測。再 者’延燒面積係將個位四捨五入而記載。 &lt;大型床墊型試驗體之3〇分鐘之總發熱量&gt; 依據美國的床之燃燒試驗方法16CFR1633之燃燒試驗方 法,自上表面實施70秒之預定之燃燒器接焰,並自側面實 施50秒之預定之燃燒器接焰。此時,利用設置於排氣管中 之錐形熱量計測定發熱量,算出自試驗開始30分鐘後之總 發熱量。該數值較低時,意味著發熱量、即燃燒物量較 少,難燃性優異。再者,16CFR1633之合格標準係開始1〇 分鐘後之總發熱量不超出15 MJ,且開始3〇分鐘後之最大 發熱速度不超出2GG kW。於本評價中,於3G分鐘以内超出 30 MJ之情形時’中止試驗。再者,總發熱量係將小數點 後第一位四捨五入而記載。 152753.doc •55- 201134992 【寸&lt;】 m 織 大型床墊型 試驗體 Q w 璨 〇〇 对 〇 〇〇 ο Cj (N 00 On 〇 ο On m 〇 Ο 〇 ψ^· T—^ m 〇 yn 00 00 〇 〇 迷你床墊型試驗體 Φν§ 5¾ § § S 〇 〇 § g 〇 S ο § S s % 〇 § % 〇 § S ο s S S S 合否評價 &lt; &lt; &lt; 0D U υ Ο &lt; &lt; &lt; &lt; U U &lt; &lt; &lt; &lt; m &lt; &lt; &lt; &lt; &lt; U &lt; Q Ο &lt; &lt; &lt; &lt; &lt; &lt; 鉍χυ 1 280 I I 260 1 I 280 I ί 290 I 1 300 | I 330 1 ο 1 260 1 1 280 1 1 270 1 1 270 1 1 280 1 1 290 I 〇 Os CS I 280 | 1 280 1 1 330 1 1 320 1 I 280 | 1 290 1 1 290 1 1 290 1 I 280 | 1 280 1 | 290 I 300 \ 300 1 270 1 260 1 320 I 350 I 280 I 270 雔 單位面積 重量 ! (g/m) 230 I 230 I 1 230 I 1 230 I I 230 I 1 230 1 1 230 1 1_270 1 I 270 | 1 230 1 ο m &lt;N 1 230 1 1 230 I 〇 (N 〇 1 230 1 1 230 1 1 230 1 〇 (N 1 230 1 〇 〇 ΓΟ &lt;Ν I 230 | 1 230 1 〇 1 230 I 1 230 1 1 230 1 I 230 | 1_230 1 230 1 〇 〇 μΛ &lt;3v U黎 嗯W 纖維種類 鲅 Uh 筚 筚 赜 oi lx 鲅 α; Uh 鲅 鲅 麵 鲅 tC tu cC 筚 Η 靼 UL· bi C *N S 1 Nomex | 鲅 od ti- 麵 鲅 CEi tu U, 鲅 tu 鲅 cd 筚 £ 鲅 οά 鲅 Di U. 筚 ct IX 鲅 〇ί ti, 槳 cd tu ex 鲅 鲅 鲅 Pi (JU 锻 ot 質量% »ri 〇 m ίη Ό S 〇 o 沄 费 am «3 melt.PET | 質量% 宕 〇 1 Η UL) cu ώ 質量% 宕 卜 o 1 Ο 1 〇 含鹵素織維 質量% m υΊ 〇 u~&gt; (N &lt;〇 〇 00 o 〇 〇 〇 〇 ο 〇 〇 〇 〇 〇 〇 〇 〇 〇 〇 〇 〇 〇 〇 00 00 ^r\ 00 ΙΓ5 00 yr\ 00 00 00 κη 00 00 yn 00 V-) 00 m 00 00 〇〇 00 00 V) 00 «η 00 v-i 2 S S On ν*ϊ (N § v*&gt; m s ON l〇 〇〇 製造例 一 ψ-*· — *— »— — *—1 ·«· — &lt;N ΓΛ 寸 &lt;n 卜 00 Cn (N 〇 r^· »·· ·— (N i (N m ¥ 1 vo 00 〇\ ο i 嫁 SK CN 1 m 1 ► 1 1 ν〇 i 卜 1 00 i 省 Os i |ϋ ¥ ¥- fS CN §; (N 1¾ 00 (N 苳 ON fS s®: 〇 $ac : ϋκ (N co m 苳 ·56· 152753.doc 201134992 難燃性 大型床墊型 試驗體 30分鐘之 總發熱量(MJ) (N (N 超出30 超出30 超出30 超出30 超出30 超出30 超出30 超出30 (N 超出30 超出30 1 超出30 超出30 超出30 超出30 超出30 超出30 超出30 迷你床墊型試驗體 « * Ξ趣 〇 無法計測 〇 無法計測 無法計測 無法計測 無法計測 〇 無法計測 無法計測 〇 無法計測 無法計測 無法計測 無法計測 無法計測 無法計測 無法計測 無法計測 無法計測 合否評價 &lt; 不合格^ &lt; |不合格 |不合格| |不合格| |不合格| D 不合格| 不合格| &lt; |不合格| |不合格| 不合格 不合格 不合格 不合格 不合格 不合格 不合格 岔《 A 趣時B自 m ^ 300 無法計測 360 410 380 380 330 330 350 340 320 330 350 380 330 340 330 370 370 330 複合體 單位面積 重量 (g/m2) 230 (N 230 j 270 230 230 230 230 230 230 230 230 230 230 230 230 230 230 230 230 $ € il 纖維種類 FR嫘縈 1 FR嫘縈 1 FR嫘縈 | FR嫘縈| FR嫘縈 FR嫘縈 | FR嫘縈| | FR嫘縈| FR嫘縈 FR嫘縈 FR嫘縈 FR嫘縈 FR嫘縈 FR嫘縈 FR嫘縈 FR嫘縈 FR嫘縈 FR嫘縈 質量% Ό 1 〇 1 〇 聚酯纖維 melt.PET 質量% yn 〇 1 〇 reg.PET 質量% 1 1 1 〇 1 〇 含鹵素纖維 質量% 1 1 1 〇 〇 〇 〇 〇 〇 1 m 〇 〇 〇 〇 〇 〇 〇 收縮變動 (%) 1 1 1 00 yn 00 |無限大| 無限大 00 00 1 00 00 V) 00 無限大 (Ν 無限大 〇 製造例 1 1 1 — 对 寸 VO 卜 ψ-^ Protex-M 00 〇\ 比較例1 比較例2 比較例3 ! 比較例4 |比較例5 1 比較例6 比較例7 比較例8 比較例9 比較例10 比較例11 比較例12 比較例13 比較例14 比較例15 比較例16 比較例17 |比較例18 I 比較例19 比較例20 -57- 152753.doc 201134992 由上述表4及5之結果可知,在使用於0.0054 mN/dtex之 荷重下將溫度自50。(:提高至3〇〇t時之收縮變動為65%以 下的含南素纖維,且使用表4所示之預定構成之實施例之 不織布的迷你床塾型試驗體之燃燒試驗中,1〇分鐘後之延 燒面積未達麵’合否判定為合格。又,藉由抑制延燒 面積’使得與崎狀不織布彳目比,❹實施狀不織布 時’大型㈣型試驗體3〇分鐘之總發熱量純低,故良 好0 又,於使用FR螺榮作為含_素纖維以外之難燃性纖維, 且含有含函素纖維3〜10質量%之情形時,在使用迷你床塾 型試驗體之難燃性評價中進行燃燒試驗時,於不織布中未 產生龜裂或孔洞而合格。又’於使用❿嫘榮作為含齒素纖 維以外之難燃性纖維,且含有含商素纖維3〜2〇質量%之情 形時,燃燒假定時之屏障背面溫度(以下稱作屏障背面溫 度)低於比較例,大型床墊型試驗體3〇分鐘之總發熱量亦 ^低,故良好。又,可知,雖然不織布中之含齒素纖維之 含量越高,迷你床墊型試驗體於燃燒試驗中1〇分鐘後之延 燒面積越低,但存在上述試驗體之難燃性評價等級越差之 傾向’於含鹵素纖維之含量為3〜3〇質量%時,表現出較先 前品更加優異之難燃性。 又,由實施例3、28及29之比較可知,不織布中所含之 含南素纖維於0.0054 mN/dtex之荷重下將溫度自5〇。〇提高 至300。〇時之收縮變動越低,則屏障背面溫度越降低, 又,大型床墊型試驗體30分鐘之總發熱量亦降低,故良 152753.doc •58· 201134992 好。其由實施例7與實施例30之比較亦明示,存在於 0.0054 mN/dtex之荷重下將溫度自50。〇提高至3〇〇t時之收 縮變動較低時’難燃性評價結果良好之傾向。又,由實施 例8與比較例5之比較可知,於〇〇〇54 mN/dtex之荷重下將 溫度自50°C提高至300X:時之收縮變動為41%時,即便不 織布中所含之含鹵素纖維之含量超出3〇質量%,難燃性評 價結果亦良好。 另一方面,由表5之結果可明確,不織布中不含有含鹵 素纖維之比較例1 ' 3及11於迷你床墊型試驗體之燃燒試驗 中,於10分鐘以内延燒面積達到1〇〇%。其原因在於,不 織布中不含有含_素纖維,容易延燒,故而難燃性差。 又,如比較例2般,僅以聚酯系纖維製作不織布之情形 時,燃燒時未形成碳化膜,因此難燃性差。又,如比較例 3般,僅以FR嫘縈製作不織布之情形時,於迷你床墊型試 驗體之燃燒試驗中,於1〇分鐘以内延燒面積達到1〇〇%。The structure is stacked as shown in Fig. 5A, and the plate portion 12 as shown in Fig. 5B is produced. Then, a nylon/polypropylene woven fabric (unit weight: 120 g/m2) of the surface material 4 of the outer layer was used as the outer layer of the nonwoven fabric 3 at a gap of 5 cm. The structure overlapped as shown in Fig. 6A, and the edge portion 13 having a length of 22 cm and a width of 576 cm as shown in Fig. 6B was produced. Then, using a nylon yarn 5' at a quilting interval of 20 cm, one piece of the above-mentioned non-woven fabric 3, 1 piece was used as the outer surface material 4 of the polyester/polypropylene woven fabric (weight per unit area: 120 g/m2). The structure was superposed as shown in Fig. 6A, and a bottom Η of 190 cm in length and 97 cm in width as shown in Fig. 6C was produced. Further, on a coil spring 17 of 19 cm in length, 97 cm in width, and 20 cm in height, a vinegar felt ls (unit weight) having a length of 19 cm, a width of 152753.doc -52 - 201134992 97 cm, and a thickness of 1 cm was placed. 12〇〇g/m2) 'The surface material 4 is provided on the upper surface, and the plate portion 12 is disposed on the upper surface thereof, and the edge portion 13 is disposed on the side surface, and the bottom portion 14 is disposed on the bottom surface, and the edge portion 13 is made of Kevlars 10 Sewing into a cylindrical shape along the side of the coil spring 17, as shown in Fig. 7, a side belt (a weight per unit area of 200 g/m2, a width of 40 mm) of 9 is used, and a Kevlar wire is used. The plate portion ^ and the edge portion 13, the edge portion 13 and the bottom portion 14 are sewn to form a large mattress as shown in FIG. (Inflammability evaluation method) &lt;Barrier back surface temperature at the time of burning false &&gt; A pearl having a thickness of 10 mm is prepared for a hole having a diameter of 55 mm and a hole having a diameter of 55 mm. The non-woven fabric of the example or the comparative example was prepared by fixing the four sides with a clip so that the non-woven fabric did not shrink when heated. The sample was vertically fixed, and the surface of the non-woven fabric of the example or the comparative example was from the β-type material to the level. In the direction of 42 mm, the American bed burning test method 16 (: 1^1633 bed side test τ type burner is used vertically. The combustion gas system uses propane gas at a gas pressure of ι 〇; kPa, the rolling body flow rate is Under the condition of 6 6 L/min, the flame is exposed for 9 seconds, and the non-contact infrared radiation thermometer (manufactured by Anritsu Meter Co., Ltd., the temperature of the flame side and the opposite side of the central portion of the non-woven fabric at this time (hereinafter, also The back surface temperature m obtained by the present measurement method is excellent in heat radiation resistance. The amine group A used for the mattress is usually formed in contact with the barrier fabric. Structure It is known that the thermal decomposition of the foam starts at about 220 to 300. (: At this time, 152753.doc • 53- 201134992 is released. The decomposition gas of the flammable gas is produced. Therefore, the urethane foam itself is inhibited. From the viewpoint of burning and suppressing the combustion of the mattress structure as a whole, it is more preferable that the temperature of the back surface of the barrier is low, that is, the temperature of the urethane foam which is in contact with the barrier is low, and it is more preferable that the temperature of the back surface of the barrier is lower than decomposition. In addition, the temperature at the back of the barrier is recorded by rounding off the maximum temperature. &lt;Mini mattress type test body evaluation method&gt; According to the United States bed burning test method 16 (: 1^1633 combustion test method) Implementation. If the method of burning the 16CFR1633 bed in the United States is simply described, the test method is as follows: a 1-shaped burner is placed horizontally from the upper surface of the bed to a vertical direction of 39 mm, and from the side The τ-shaped burner is placed vertically at a position of 42 mm in the horizontal direction, and the flame is started at the same time. The upper surface is flamed for 7 seconds, and the side is flamed for 5 sec. The combustion gas is made of a propane gas. In 1G1, the gas state of the upper surface is 12.9 L/min., and the gas flow of the burner on the side is 6·6 L/min. The evaluation of the flame retardancy is carried out as follows. : When the test is carried out by the above test method, the part which is exposed to the fire and which is exposed to the fire does not have cracks or holes. B grade combination #: When the same test is carried out, it is self-producing, but it is generated in the part exposed to the fire. C. No. 1 cm. Qualified for C grade: self-extinguishing when performing the same test, but cracking more than 1 cm in the part exposed to fire. ^Qualification of grade: Internal flammability when performing the same test The urethane is on fire, but it is extinguished immediately and eventually self-extinguishes. Failed: When the same test was carried out, the internal flammable amino phthalate was 152753.doc -54- 201134992 fire, mandatory fire extinguishing, suspension test. &lt;Evaluation of the area to be burned after 10 minutes of the plate portion of the mini mattress type test body&gt; According to the combustion test method of the bed test of the United States & 16 CFR 1633, the predetermined burner flame was performed for 70 seconds from the upper surface. A 50 second predetermined burner flame is applied from the side. The ratio of the area of the burned portion (the portion burned and carbonized) of the plate portion after the start of the test to the total area of the panel after 1 minute of the test is expressed as a percentage. The lower the value, the smaller the area to be burned, and the more excellent the fire extinguishing property and the flame retardancy. That is, when it is convenient to burn 1 〇〇% within 1 〇 minutes, it is also evaluated as 100. /〇. Further, when the internal flammable urethane was ignited and the fire was extinguished and the test was stopped, the evaluation was impossible. Furthermore, the area of the "expansion area" is recorded by rounding off one place. &lt;Total calorific value of 3 minutes of the large mattress type test body&gt; According to the combustion test method of the American bed burning test method 16CFR1633, a predetermined burner flame is applied for 70 seconds from the upper surface, and is implemented from the side. The 50 second predetermined burner is connected to the flame. At this time, the calorific value was measured by a cone calorimeter provided in the exhaust pipe, and the total calorific value after 30 minutes from the start of the test was calculated. When the value is low, it means that the calorific value, that is, the amount of the combustibles is small, and the flame retardancy is excellent. Furthermore, the 16CFR1633 eligibility standard does not exceed 15 MJ of total heat generation after 1 minute, and the maximum heating rate after 3 minutes has not exceeded 2 GG kW. In this evaluation, the test was aborted when the temperature exceeded 30 MJ within 3 G minutes. Furthermore, the total calorific value is recorded by rounding off the first place after the decimal point. 152753.doc •55- 201134992 [inch&lt;] m woven large mattress type test body Q w 璨〇〇 〇〇〇ο Cj (N 00 On 〇ο On m 〇Ο 〇ψ^· T—^ m 〇 Yn 00 00 〇〇 Mini Mattress Type Test Body Φν§ 53⁄4 § § S 〇〇§ g 〇S ο § S s % 〇§ % 〇§ S ο s SSS No evaluation&lt;&lt;&lt; 0D U υ Ο &lt ; &lt;&lt;&lt; UU &lt;&lt;&lt;&lt;&lt;&lt;&lt;&lt;&lt;&lt;&lt;&lt;&lt;&lt;&lt;&lt;&lt;&lt;&lt;&lt;&lt;&lt;&lt;&lt; 1 I 280 I ί 290 I 1 300 | I 330 1 ο 1 260 1 1 280 1 1 270 1 1 270 1 1 280 1 1 290 I 〇Os CS I 280 | 1 280 1 1 330 1 1 320 1 I 280 | 1 290 1 1 290 1 1 290 1 I 280 | 1 280 1 | 290 I 300 \ 300 1 270 1 260 1 320 I 350 I 280 I 270 雔 Unit weight! (g/m) 230 I 230 I 1 230 I 1 230 II 230 I 1 230 1 1 230 1 1_270 1 I 270 | 1 230 1 ο m &lt; N 1 230 1 1 230 I 〇 (N 〇1 230 1 1 230 1 1 230 1 〇 (N 1 230 1 〇 〇ΓΟ &lt;Ν I 230 | 1 230 1 〇1 230 I 1 230 1 1 230 1 I 230 | 1_230 1 230 1 〇〇μΛ &lt;3v U WW fiber type 鲅Uh 筚筚赜oi lx 鲅α; Uh 鲅鲅 鲅 tC tu cC 靼 ·UL· bi C *NS 1 Nomex | 鲅od ti- 鲅 i i i 鲅 鲅 鲅 鲅 鲅 鲅 鲅鲅οά 鲅Di U. 筚ct IX 鲅〇ί ti, paddle cd tu ex 鲅鲅鲅Pi (JU forged ot mass% »ri 〇m ίη Ό S 〇o 沄fe am «3 melt.PET |质量% 宕〇 1 Η UL) cu ώ mass % 宕o o 1 Ο 1 〇 halogen-containing weave quality % m υΊ 〇u~&gt; (N &lt;〇〇00 o 〇〇〇〇ο 〇〇〇〇〇〇〇〇〇 〇〇〇〇〇00 00 ^r\ 00 ΙΓ5 00 yr\ 00 00 00 κη 00 00 yn 00 V-) 00 m 00 00 〇〇00 00 V) 00 «η 00 vi 2 SS On ν*ϊ (N § V*&gt; ms ON l〇〇〇 Manufacturing example ψ-*· — *— »— — *—1 ·«· — &lt;N ΓΛ inch&lt;n 卜 Cn (N 〇r^· »·· ·—(N i (N m ¥ 1 vo 00 〇\ ο i marry SK CN 1 m 1 ► 1 1 ν〇i 卜 1 00 i province Os i |ϋ ¥ ¥- fS CN §; (N 13⁄4 00 (N 苳ON fS s®: 〇$ac : ϋκ (N co m 苳·56· 152753.doc 201134992 flammable large mattress type test body 30 minutes total calorific value (MJ) (N ( N over 30 over 30 over 30 over 30 over 30 over 30 over 30 over 30 (N over 30 over 30 1 over 30 over 30 over 30 over 30 over 30 over 30 over 30 over 30 mattress type test body « * Measurement 〇 Unable to measure Unable to measure Unable to measure Unable to measure 〇 Unable to measure Unable to measure 〇 Unable to measure Unable to measure Unable to measure Unable to measure Unable to measure Unable to measure Unable to measure Unable to measure Unable to measure Consolidated evaluation < Unqualified ^ &lt; | Unqualified | Unqualified | |Failed | |Failed | D Failed | Failed | &lt; |Failed | |Failed | Unqualified Unqualified Unqualified Unqualified Unqualified Unqualified 岔 "A Interesting B from m ^ 300 Measurement 360 410 380 380 330 330 350 340 320 330 350 380 330 340 330 370 370 330 Complex unit area weight (g/m2) 230 (N 230 j 270 230 230 230 230 230 230 230 230 230 230 230 230 230 230 230 230 230 $ € il Fiber type FR嫘萦1 FR嫘萦1 FR嫘萦| FR嫘萦| FR嫘萦FR嫘萦| FR嫘萦| | FR嫘萦| FR嫘萦FR嫘萦FR嫘萦FR嫘萦FR嫘萦FR嫘萦FR嫘萦FR嫘萦FR嫘萦FR嫘萦% by mass Ό 1 〇1 〇 polyester fiber melt.PET% by mass yn 〇1 〇reg.PET% by mass 1 1 1 〇1 〇 Halogen-containing fiber mass % 1 1 1 〇〇〇〇〇〇1 m 〇〇〇〇〇〇〇 shrinkage change (%) 1 1 1 00 yn 00 | Infinity | Infinity 00 00 1 00 00 V) 00 Unlimited Large (Ν Infinity 〇 Manufacturing Example 1 1 1 - 寸 VO ψ ψ -^ Protex-M 00 〇 \ Comparative Example 1 Comparative Example 2 Comparative Example 3 ! Comparative Example 4 | Comparative Example 5 1 Comparative Example 6 Comparative Example 7 Comparison Example 8 Comparative Example 9 Comparative Example 10 Comparative Example 11 Comparative Example 12 Comparative Example 13 Comparative Example 14 Comparative Example 15 Comparative Example 16 Comparative Example 17 | Comparative Example 18 I Comparative Example 19 Comparative Example 20 -57- 152753.doc 201134992 From the above table The results of 4 and 5 show that the temperature is from 50 at a load of 0.0054 mN/dtex. (: In the combustion test of the mini-bed type test body containing the non-woven fabric of the embodiment of the predetermined configuration shown in Table 4, the shrinkage variation to 3 〇〇t is 65% or less, and 1 〇 After the minute, the area of the burnt surface was not met, and it was judged to be qualified. In addition, by suppressing the area of the burnt surface, it was compared with the shape of the smear-like non-woven fabric, and when the non-woven fabric was applied, the total calorific value of the large (four) type test body was 3 minutes. In the case of using FR rongrong as a flame retardant fiber other than the γ-containing fiber, and containing 3 to 10% by mass of the element-containing fiber, it is difficult to use the mini bed type test body. When the combustion test was carried out in the evaluation, the cracks or holes were not produced in the non-woven fabric, and it was qualified as the flame retardant fiber other than the dentate fiber, and the quality of the fiber containing the commercial fiber was 3 to 2 〇. In the case of %, the barrier back surface temperature (hereinafter referred to as the barrier back surface temperature) of the combustion assumption is lower than that of the comparative example, and the total calorific value of the large mattress type test body is also low for 3 minutes, so that it is good. Non-woven fabric The higher the content of the fiber, the lower the calcination area of the mini mattress type test body after 1 minute in the burning test, but the tendency of the test piece to be inferior in the evaluation of the flame retardancy is 'the content of the halogen-containing fiber is When it is 3 to 3 % by mass, it exhibits more excellent flame retardancy than the prior art. Further, from the comparison of Examples 3, 28 and 29, the load of the non-woven fabric containing the Nansu fiber at 0.0054 mN/dtex is known. The temperature is increased from 5〇.〇 to 300. The lower the shrinkage change at the time of the ,, the lower the temperature at the back of the barrier, and the lower the total calorific value of the large mattress type test body for 30 minutes, so the good 152753.doc • 58· 201134992. It is also clear from the comparison between Example 7 and Example 30 that it is difficult to ignite when the temperature changes from 50 〇 to 3 〇〇t when the temperature changes from 50 〇 to 3 〇〇t under the load of 0.0054 mN/dtex. The tendency of the evaluation results was good. Further, from the comparison between Example 8 and Comparative Example 5, it was found that when the temperature was changed from 50 ° C to 300 X at a load of 54 mN/dtex, the shrinkage variation was 41%. Even if the content of halogen-containing fibers contained in the non-woven fabric is super 3〇% by mass, the flame retardancy evaluation result is also good. On the other hand, from the results of Table 5, it can be clarified that the non-woven fabric does not contain the halogen-containing fiber Comparative Example 1 '3 and 11 in the mini mattress type test body burning test In the case where the non-woven fabric does not contain the γ-containing fiber, it is easy to be burned, and thus the flame retardancy is poor. Further, as in Comparative Example 2, only the polyester fiber is used. In the case of non-woven fabric, a carbonized film is not formed during combustion, so that the flame retardancy is poor. Further, as in the case of Comparative Example 3, when the nonwoven fabric is produced only by FR, in the combustion test of the mini mattress type test body, Within a few minutes, the area burned up to 1%.

又,不織布中之於0.0054 mN/dtex之荷重下將溫度自50°C 提局至300 C時之收縮變動超出45%的含鹵素纖維之含量 超出30質量%的比較例4及5於迷你床墊型試驗體之燃燒試 驗中,在進行試驗時於不織布中產生孔洞,内部易燃性胺 基曱酸酯著火’強制滅火而中止試驗,因此不合格。認為 其原因在於,由於不織布中之含鹵素纖維之含量較多,故 無法充分抑制燃燒時之收縮應力,或燃燒時之碳化成分之 量不足。 又,不織布中之聚酯系纖維之含量未達質量之比較 152753.doc •59· 201134992 例12於迷你床墊型試驗體之燃燒試驗評價中,在進行燃燒 試驗時不織布開裂,產生孔洞,内部易燃性胺基曱酸酯著 火’強制滅火而中止試驗,因此不合格。推定其原因在 於,不織布中具有燃燒時熔融而接著之作用的聚酯成分較 少。又,不織布中之聚酯系纖維之含量超出5 〇質量〇/❶之比 較例13於迷你床墊型試驗體之燃燒試驗評價中,在進行燃 燒試驗時不織布開裂,產生孔洞,内部易燃性胺基甲酸酯 者火,強制滅火而中止試驗,因此不合格。認為其原因在 於,由於不織布中之聚酯系纖維之量過剩,故燃燒時之碳 化成分之量不足。 又,不織布中之含鹵素纖維以外之難燃性纖維的含量未 達30質量%之比較例14於迷你床墊型試驗體之燃燒試驗評 價中,在進行燃燒試驗時不織布開裂,產生孔洞,内部易 燃性胺基曱酸酯著火,強制滅火而申止試驗,因此不合 格。認為其原因在於’不織布中之含鹵素纖維以外之難燃 性纖維不足,燃燒時之碳化成分之量不足。 不織布中所含之含鹵素纖維於0 0054 mN/dtex之荷重下 將溫度自50。(:提高至300°C時之收縮變動超出65°/。的比較 例6、7、9、10、20於迷你床墊型試驗體之燃燒試驗中, 在進行燃燒試驗時不織布開裂,產生孔洞,内部易燃性胺 基甲酸酯著火’強制滅火而中止試驗,因此不合格。又, 不織布中所含之含鹵素纖維於0.0054 mN/dtex之荷重下將 溫度自50。(:提高至300°C時之收縮變動超出65%的比較例8 於迷你床墊型試驗體之燃燒試驗中,於1〇分鐘以内延燒面 152753.doc -60· 201134992 積達到10 0 0/。。由於比較例6〜i 〇中任一者均為不織布中的 含li素纖維之收縮變動較高,故燃燒時之不織布之結構較 弱,難燃性差。再者,於比較例9中,使用追加試驗了曰 本專利特開平6-287806之實施例之製造例16之含鹵素纖 維。 又,使用於0.0054 mN/dtex之荷重下將溫度自5〇艽提高 至300°C時之收縮變動無限大的「Protex_M」(Kaneka股份 有限公司製造)作為含鹵素纖維之比較例15於迷你床墊型 武驗體之燃燒試驗評價中,在進行燃燒試驗時不織布開 裂’產生孔洞,内部易燃性胺基甲酸酯著火,強制滅火而 中止試驗,因此不合格。認為其原因在於,pr〇tex_M在於 0.0054 mN/dtex之荷重下將溫度自50°C提高至300。(:時,收 縮後切斷’故進行燃燒試驗時容易於不織布中產生孔洞。 於比較例16中使用追加試驗了日。本專利特開2004-197255之實施例的製造例18之含鹵素纖維。日本專利特開 2004-197255係與本申請人所申請之專利申請相關之先前 技術。由表2可知,製造例18之含鹵素纖維於0.0054 mN/dtex之荷重下將溫度自5〇°c提高至30(TC時之收縮變動 超出65%。因此’使用製造例18之含鹵素纖維之比較例16 於使用迷你床墊型試驗體之燃燒試驗評價中,在進行燃燒 試驗時於不織布中產生孔洞,内部易燃性胺基曱酸酯著 火,強制滅火而中止試驗,因此不合格。 於比較例17中使用追加試驗了 WO 01/32968之實施例的 製造例19之含鹵素纖維。w〇 01/32968係與本申請人所申 152753.doc •6卜 201134992 請之專利申請相關之先前技術。由表2可知,製造例19於 0.0054 mN/dtex之荷重下將溫度自50°C提高至300°C時之收 縮變動超出65%。因此,使用製造例19之含鹵素纖維之比 較例1 7於使用迷你床墊型試驗體之燃燒試驗評價中,在進 行燃燒試驗時於不織布中產生龜裂,自該龜裂處引入火, 而使内部易燃性胺基甲酸酯著火,強制滅火而中止試驗, 因此不合格。 於比較例18中使用追加試驗了日本專利特開昭61 -282420之實施例的製造例20之含ii素纖維。由表2可知, 製造例20之含鹵素纖維於0.0054 mN/dtex之荷重下將溫度 自5〇CI«c尚至300C時之收縮變動超出65%。因此,使用 製造例20之含鹵素纖維之比較例18於使用迷你床墊型試驗 體之燃燒試驗評價中,在進行燃燒試驗時於不織布中產生 孔洞,内部易燃性胺基甲酸酯著火,強制滅火而中止試 驗,因此不合格》 於比較例19中使用追加試驗了日本專利特開昭53_ 1 06825之實施例的製造例21之含鹵素纖維。曰本專利特開 昭53-106825係與本申請人所申請之專利申請相關之先前 技術。由表2可知’製造例2 1之含鹵素纖維於〇. 〇 〇 $ 4 mN/dtex之荷重下將溫度自50°C提高至3〇CTc時之收縮變動 超出65%。因此,使用製造例21之含!|素纖維之比較例19 於使用迷你床墊型試驗體之燃燒試驗評價中,在進行燃燒 試驗時於不織布中產生孔洞’内部易燃性胺基曱酸醋著 火,強制滅火而中止試驗,因此不合格。 152753.doc • 62· 201134992 【圖式簡單說明】 圖1A係用於難燃性評價之迷你床塾型試驗體之板部的側 剖面圖,圖1B係該板部之整體圖。 圖2 A係用於難燃性評價之迷你床墊型試驗體之邊緣部與 底。卩的側剖面圖,圖2B係該邊緣部之整體圖,圖2C係該 底部之整體圖。 圖3係對用於難燃性評價之迷你床墊型試驗體之組裝進 行說明的說明圖。 圖4係用於難燃性5平價之迷你床墊型試驗體之整體圖。 圖5 A係用於難燃性評價之大型床墊型試驗體之板部之側 剖面圖,圖5B係該板部之整體圖。 圖6 A係用於難燃性評價之大型床墊型試驗體之邊緣部與 底邙的側剖面圖,圖6B係該邊緣部之整體圖,圖6C係該 底部之整體圖。 圖7係對用於難燃性評價之大型床墊型試驗體之組裝進 行說明的說明圖。 圖8係用於難燃性評價之大型床墊型試驗體之整體圖。 圖9係表不本發明之一實施例中之含函素纖維之收縮圖 案的圖表。 圖係表示比較例甲之含鹵素纖維之收縮圖案的圖表。 圖U係表示比較例令之含鹵素纖維之收縮圖案的圖表。 圖12係表示本發明之—實施例中之含齒素纖維之收縮圖 案的圖表。 152753.doc -63- 201134992 圖13係表示本發明之一皆 貫施例中之含_素纖維之收縮圖 案的圖表。 圖14係表示本發明之_眚&amp; + n貫施例中之含函素纖維之收縮圖 案的圖表。 圖15係表示比較例中之含齒素纖維之收縮圖案的圖表。 【主要元件符號說明】 1 ' 2 &gt; 11 聚胺基曱酸酯發泡體 3 不織布 4 外層之表面原材料 5 尼龍絲 6、 12 板部 7、 13 邊緣部 8 &gt; 14 底部 9 聚丙烯製縫邊帶 10 克維拉絲 15 聚酯製毛氈 16 、17 螺旋彈簧 152753.doc 64·Further, in the non-woven fabric under the load of 0.0054 mN/dtex, the temperature was changed from 50 ° C to 300 C, and the shrinkage variation exceeding 45% of the halogen-containing fibers exceeded 30% by mass of Comparative Examples 4 and 5 in the mini bed. In the burning test of the mat type test body, a hole was formed in the non-woven fabric during the test, and the internal flammable amino phthalate was ignited to extinguish the test, which was unsatisfactory. The reason for this is considered to be that since the content of the halogen-containing fibers in the nonwoven fabric is large, the shrinkage stress at the time of combustion cannot be sufficiently suppressed, or the amount of carbonized components at the time of combustion is insufficient. Moreover, the content of the polyester fiber in the non-woven fabric is not comparable to the quality. 152753.doc • 59· 201134992 Example 12 In the combustion test evaluation of the mini mattress type test body, the non-woven fabric is cracked during the burning test, and a hole is generated. The flammable amino phthalate ignited 'compulsory fire extinguishing and the test was terminated, so it was unqualified. The reason for this is presumed to be that the non-woven fabric has less polyester component which melts upon combustion and then acts. Further, in Comparative Example 13 in which the content of the polyester fiber in the nonwoven fabric exceeded 5 〇 mass 〇 / 于, in the combustion test evaluation of the mini mattress type test body, the nonwoven fabric was cracked during the combustion test, and voids were generated, and internal flammability was generated. The urethane fire was extinguished and forced to extinguish the fire and the test was terminated, so it was unqualified. The reason for this is considered to be that the amount of the carbonaceous component at the time of burning is insufficient because the amount of the polyester-based fiber in the nonwoven fabric is excessive. In addition, in Comparative Example 14 in which the content of the flame-retardant fiber other than the halogen-containing fiber in the nonwoven fabric was less than 30% by mass, in the combustion test evaluation of the mini mattress type test body, the nonwoven fabric was cracked during the burning test, and voids were generated and the inside was formed. The flammable amino phthalate ignited and forced to extinguish the fire and the test was terminated, so it was unqualified. The reason is considered to be that the flame retardant fiber other than the halogen-containing fiber in the nonwoven fabric is insufficient, and the amount of the carbonized component at the time of combustion is insufficient. The halogen-containing fiber contained in the nonwoven fabric has a temperature of 50 at a load of 0 0054 mN/dtex. (Comparative Examples 6, 7, 9, 10, and 20 in which the shrinkage variation at 300 ° C was increased to more than 65 ° C. In the combustion test of the mini mattress type test body, the nonwoven fabric was cracked during the burning test, and voids were generated. The internal flammable urethane fired 'compulsory fire extinguishing and stopped the test, so it was unqualified. Moreover, the halogen-containing fiber contained in the non-woven fabric will have a temperature from 50 at a load of 0.0054 mN/dtex. (: Increase to 300 In Comparative Example 8 in which the shrinkage variation at °C exceeded 65%, in the burning test of the mini mattress type test body, the product was 152753.doc -60·201134992 in less than 1 minute, and the product reached 100%. In any of 6 to i, the li-containing fiber in the non-woven fabric has a high shrinkage fluctuation, so that the structure of the non-woven fabric at the time of burning is weak, and the flame retardancy is poor. Further, in Comparative Example 9, an additional test was used. The halogen-containing fiber of Production Example 16 of the embodiment of the Japanese Patent Laid-Open No. Hei 6-287806. Further, when the temperature is increased from 5 至 to 300 ° C under an load of 0.0054 mN/dtex, the shrinkage variation is infinitely large. Protex_M" (made by Kaneka Co., Ltd.) as Comparative Example 15 of the halogen fiber In the combustion test evaluation of the mini mattress type test body, the non-woven fabric cracked during the burning test to generate a hole, and the internal flammable urethane was ignited, and the fire was extinguished to stop the test, so Qualified. It is considered that the reason is that pr〇tex_M increases the temperature from 50 ° C to 300 under the load of 0.0054 mN/dtex. (: When it is cut after shrinking, it is easy to produce voids in the non-woven fabric when the combustion test is performed. The addition test was carried out in Comparative Example 16. The halogen-containing fiber of Production Example 18 of the example of the present invention is disclosed in Japanese Patent Application Laid-Open No. 2004-197255. The Japanese Patent Application Publication No. 2004-197255 is a prior art related to the patent application filed by the present applicant. As can be seen from Table 2, the halogen-containing fiber of Production Example 18 increased the temperature from 5 ° C to 30 under a load of 0.0054 mN/dtex (the shrinkage variation at TC exceeded 65%. Therefore, the halogen containing the manufacturing example 18 was used. Comparative Example 16 of the fiber In the combustion test evaluation using the mini mattress type test body, a hole was formed in the nonwoven fabric during the combustion test, and the internal flammable amino phthalate was ignited to extinguish the fire. The test was tested and was therefore unsatisfactory. In Comparative Example 17, the halogen-containing fiber of Production Example 19 of the example of WO 01/32968 was additionally used. w〇01/32968 is related to the applicant's application 152753.doc • 6 201134992 The prior art related to the patent application. As can be seen from Table 2, the manufacturing example 19 has a shrinkage variation exceeding 65% when the temperature is raised from 50 ° C to 300 ° C under a load of 0.0054 mN/dtex. Therefore, in Comparative Example 17 using the halogen-containing fiber of Production Example 19, in the combustion test evaluation using the mini mattress type test body, cracks were generated in the nonwoven fabric during the combustion test, and fire was introduced from the crack. The internal flammable urethane was ignited, the fire was extinguished and the test was terminated, so it was unqualified. In the comparative example 18, the ii-containing fiber of Production Example 20 of the example of the Japanese Patent Laid-Open Publication No. 61-282420 was used. As is apparent from Table 2, the halogen-containing fiber of Production Example 20 exhibited a shrinkage variation of more than 65% from 5 〇 CI «c to 300 C under a load of 0.0054 mN/dtex. Therefore, in Comparative Example 18 using the halogen-containing fiber of Production Example 20, in the combustion test evaluation using the mini mattress type test body, voids were generated in the nonwoven fabric during the burning test, and the internal flammable urethane was ignited. In the case of the comparative example 19, the halogen-containing fiber of the production example 21 of the example of the Japanese Patent Laid-Open Publication No. SHO 53_186825 was used. Japanese Patent Laid-Open No. Sho 53-106825 is a prior art related to the patent application filed by the present applicant. As can be seen from Table 2, the shrinkage variation of the halogen-containing fiber of Production Example 2 under the load of 4. 〇 〇 $ 4 mN/dtex increased from 50 ° C to 3 〇 CTc exceeded 65%. Therefore, in Comparative Example 19 using the ?-containing fiber of Production Example 21, in the combustion test evaluation using the mini mattress type test body, a hole was formed in the nonwoven fabric during the burning test, and the internal flammable amine oleic acid vinegar was produced. Fired, forced to extinguish the fire and stopped the test, so it was unqualified. 152753.doc • 62· 201134992 [Brief Description of the Drawings] Fig. 1A is a side cross-sectional view of a plate portion of a mini bed type test body for evaluation of flame retardancy, and Fig. 1B is an overall view of the plate portion. Fig. 2 A is an edge portion and a bottom of a mini mattress type test body for evaluation of flame retardancy. A side cross-sectional view of the crucible, Fig. 2B is an overall view of the edge portion, and Fig. 2C is an overall view of the bottom portion. Fig. 3 is an explanatory view for explaining the assembly of a mini mattress type test body for evaluation of flame retardancy. Fig. 4 is an overall view of a mini mattress type test body for a flame retardant 5 parity. Fig. 5A is a side cross-sectional view of a plate portion of a large mattress type test body for evaluation of flame retardancy, and Fig. 5B is an overall view of the plate portion. Fig. 6A is a side sectional view showing the edge portion and the bottom cymbal of the large mattress type test body for evaluation of flame retardancy, Fig. 6B is an overall view of the edge portion, and Fig. 6C is an overall view of the bottom portion. Fig. 7 is an explanatory view for explaining the assembly of a large mattress type test body for evaluation of flame retardancy. Fig. 8 is an overall view of a large mattress type test body for evaluation of flame retardancy. Fig. 9 is a graph showing a shrinkage pattern of a fiber containing a fiber in an embodiment of the present invention. The figure shows a graph of the shrinkage pattern of the halogen-containing fiber of Comparative Example A. Figure U is a graph showing a shrink pattern of a halogen-containing fiber of a comparative example. Fig. 12 is a graph showing a shrinkage pattern of a dentate-containing fiber in the embodiment of the present invention. 152753.doc -63- 201134992 Figure 13 is a graph showing the shrinkage pattern of the γ-containing fiber in one of the embodiments of the present invention. Fig. 14 is a graph showing the shrinkage pattern of the element-containing fibers in the _眚&amp; + n embodiment of the present invention. Fig. 15 is a graph showing a shrinkage pattern of a dentate-containing fiber in a comparative example. [Description of main component symbols] 1 ' 2 &gt; 11 Polyurethane phthalate foam 3 Non-woven fabric 4 Surface material of outer layer 5 Nylon wire 6, 12 Plate part 7, 13 Edge part 8 &gt; 14 Bottom 9 Polypropylene Sewing side band 10 gram of fifteen 15 polyester felt 16 , 17 spiral spring 152753.doc 64·

Claims (1)

201134992 七、申請專利範圍:201134992 VII. Patent application scope: 體’其特徵在於:其係含有含齒素纖 及含齒素纖維以外之難燃性纖維者; 維集合體之總量設為100質量%時,上 量為3〜30質量。/〇,上述聚酯系纖維之 上述含i素纖維以外之難燃性纖維 上述3鹵素纖維於0.0054 mN/dtex之荷重下將溫度自 50C提问至3〇〇它時之收縮變動為65%以下; 上述含鹵素纖維包含聚合物(1)、及促進上述聚合物 (1)之燃燒時之脫齒反應及燃燒時之碳化反應的至少1種 金屬化合物(2);並且 當將上述聚合物(i)之總量設為1〇〇質量%時,上述聚 合物(υ包含丙烯腈30〜70質量%、含鹵素亞乙烯基單體 及/或含_素乙烯基單體70〜30質量%、及可與該等共聚 合之乙烤基系單體〇〜丨〇質量%。 2. 如請求項1之難燃纖維集合體,其中上述含齒素纖維之 單纖維強度為0.5〜1.6 cN/dtex。 3. 如請求項1之難燃纖維集合體,其中上述含齒素纖維於 0·0054 mN/dtex之荷重下將溫度自50°C提高至300。(:時, 並未切斷而殘存。 4. 如請求項2之難燃纖維集合體,其中上述含函素纖維於 0.0054 mN/dtex之荷重下將溫度自50°C提高至300。(:時, 並未切斷而殘存。 152753.doc 201134992 5. 如請求項1至4中任一項之難燃纖維集合體,其中上述金 屬化合物(2)包含促進脫_反應及碳化反應之兩反應之金 屬化合物(2])、或者上述金屬化合物㈤)與促進脫齒反 應之金屬化合物(2-2)之組合。 6. 如請求項1至4中任一項之難燃纖維集合體,其中上述含 齒素纖維係藉由將含有上述聚合物⑴與上述金屬化合物 (2)之紡絲液擠出,進行一次延伸與水洗其後加以乾 燥,進行二次延伸,並實施熱處理而進行紡絲,並且於 上述延#時之延伸倍率乘以上述熱處理時纖維收縮之比 例、即緩和倍率所得之總延伸倍率為5倍以下之條件下 製造。 7. 如請求項1至4中任一項之難燃纖維集合體,其中相對於 上述聚合物(1) 1〇〇質量份,上述含齒素纖維含有上述金 屬化合物(2) 0.05〜50質量份。 8. 如請求項5之難燃纖維集合體,纟中相對於上述聚合物 (1) 100質量份,上述含齒素纖維含有上述金屬化合物Ρ-2) 5〜30質量份。 9. 如請求項5之難燃纖維集合體,其中上述金屬化合物(2_ D係選自由氧化辞、碳酸鋅、硫化鋅、硼酸辞、錫酸 辞偏錫I、氧化鎢、氧化錯、氧化錫、氧化銅、璃酸 銅 '三氧化銦、欽㈣、及對甲苯續酸鋅所組成之群中 之至少一種。 Η)·如請求項5之難燃纖維集合體,其中上述金屬化合物(2_ 2)係選自由銻化合物、氧化鐵、磷酸鐵、草酸鐵、硫化 152753.doc 201134992 鐵、氧化ϋ、三氧㈣、氧氣㈣、及蛾化銅所組成之 群中之至少一種。 11·如請求項5之難燃纖維集合體,其中上述金屬化合物⑺ 包含促進脫_反應及碳化反應之兩反應之金屬化合物(2_ 1)、或者上述金屬化合物(2·1)與促進脫鹵反應之金屬化 • 合物(2-2)之組合。 12.如請求項1至4中任一項之難燃纖維集合體,其中上述含 画素纖維以外之難燃性纖維係選自由芳族聚醯胺纖維、 笨曱酸酯纖維、聚笨硫醚纖維、聚醚醚酮纖維、聚醯亞 胺纖維、聚醯胺醯亞胺纖維、難燃聚酯纖維、三聚氰胺 纖維、丙烯酸酯纖維、聚苯氧化物纖維、聚氯乙烯纖 維、聚偏二氣乙烯纖維、聚氣乙烯醇纖維、聚四氟乙烯 纖維、含有無機化合物之再生纖維素纖維、含有磷系難 燃劑之再生纖維素纖維、塗布有難燃劑之後加工難燃纖 維素纖維、氧化丙烯酸纖維、碳纖維、玻璃纖維、活性 碳纖維所組成之群中之至少一種。 13 如請求項12之難燃纖維集合體,其中上述含齒素纖維以 外之難燃性纖維係選自由含有矽成分之再生纖維素纖 維、含有填系難燃劑之再生纖維素纖維、塗布有難燃劑 ' 之後加工難燃纖維素纖維、三聚氰胺纖維、難燃聚酯纖 維、丙烯酸酯纖維、芳族聚醯胺纖維所組成之群中之至 少一種。 14.如請求項π之難燃纖維集合體,其中上述含函素纖維以 外之難燃性纖維係選自由含有石夕成分之再生纖維素纖 152753.doc 201134992 維、含有磷系難燃劑之再生纖維素纖維、塗布有難燃劑 之後加工難燃纖維素纖維、芳族聚醯胺纖維所組成之群 中之至少一種。 15. —種難燃纖維集合體之製造方法,其特徵在於:上述難 燃纖維集合體係含有含齒素纖維、聚酯系纖維、及含鹵 素纖維以外之難燃性纖維者; 上述製造方法包括如下步驟:當將上述難燃纖維集合 體之總量設為1〇〇質量%時,將3〜30質量%之上述含鹵素 纖維、20~50質量%之上述聚酯系纖維、及3〇〜77質量% 之上述含齒素纖維以外之難燃性纖維加以混合; 上述含鹵素纖維於0.0054 mN/dtex之荷重下將溫度自 5〇C提高至300°C時之收縮變動為65%以下; 上述含鹵素纖維係藉由將包含聚合物(1)、與促進上述 聚合物⑴之崎時之脫敍應及㈣時之碳化反應的至 少1種金屬化合物(2)之組合物進行纺絲後,實施熱處理 而獲得;並且 當將上述聚合物⑴之總量設為1〇〇質量〇/。時,上述聚 合物⑴包含丙婦腈30〜7〇質量%、含齒素亞乙稀基單體 及/或含齒素乙烯基單體7〇〜3〇質量%、及 合之乙稀基系單體。〜1〇質量%。 丄、聚 16.如請求項15之難燃纖維集合體之製造方法,纟中上述含 齒素纖維之紡絲係藉由將含有上述聚合物⑴與上述金屬 化合物(2)之纺絲液擠出,進行一次延伸與水洗其後加 以乾燥,進行二次延伸,並實施熱處理而進行,並且上 152753.doc 201134992 述延伸時之延伸倍率乘以上述熱處理時纖維收縮之比 例、即緩和倍率所得之總延伸倍率為5倍以下。 17.如請求項15或16之難燃纖維集合體之製造方法,其中上 述熱處理為140°C以上之乾熱 '或9〇。〇以上之濕熱中之 鬆他熱處理。 8如吻求項15或16之難燃纖維集合體之製造方法,其中上 述熱處理為180°C以上之乾熱、或15〇乞以上之濕熱中之 緊張熱處理。 19·如凊求項17之難燃纖維集合體之製造方法,其中上述熱 處理為90〜15(TC之濕熱中之鬆弛熱處理。 … 20. 如吻求項15或16之難燃纖維集合體之製造方法,其中上 述熱處理為100〇C以上之濕熱加壓蒸氣中之鬆弛熱處 理。 21. —種纖維製品,其特徵在於包含如請求項丨至丨々中任一 項之難燃纖維集合體。 22. 如請求項丨至4中任一項之難燃纖維集合體,其中上述含 齒素纖維以外之難燃性纖维係L〇I值為25以上之纖維。 23. 如請求項5之難燃纖維集合體,其中上述含鹵素纖維以 外之難燃性纖維係LOI值為25以上之纖維。 24_ —種纖維製品,其特徵在於包含如請求項或η之難燃 纖維集合體。 25.如請求項15或16之難燃纖維集合體之製造方法,其中上 述含函素纖維以外之難燃性纖維係L0I值為25以上之纖 維。 152753.doc 201134992 26. 如請求項19之難燃纖維集合體之製造方法,其中上述含 鹵素纖維以外之難燃性纖維係LOI值為25以上之纖維。 27. 如請求項20之難燃纖維集合體之製造方法,其中上述含 鹵素纖維以外之難燃性纖維係LOI值為25以上之纖維。 152753.docThe body ' is characterized in that it contains a refractory fiber other than the dentate fiber and the dentate-containing fiber; and when the total amount of the aggregate is 100% by mass, the upper amount is 3 to 30 mass. /〇, the flame retardant fiber other than the i-containing fiber of the polyester fiber, the three-halogen fiber has a shrinkage fluctuation of 65% or less at a load of 0.0054 mN/dtex from 50C to 3〇〇. The above halogen-containing fiber comprises a polymer (1), and at least one metal compound (2) which promotes a denaturation reaction upon combustion of the above polymer (1) and a carbonization reaction upon combustion; and when the above polymer ( When the total amount of i) is 1% by mass, the above polymer (υ includes 30 to 70% by mass of acrylonitrile, halogen-containing vinylidene monomer, and/or 70% to 30% by mass of the monomer-containing vinyl monomer) And the unheated fiber aggregate of the above-mentioned dentate-containing fiber having a strength of 0.5 to 1.6 cN. /dtex 3. The flame-retardant fiber assembly of claim 1, wherein the dentate-containing fiber is increased in temperature from 50 ° C to 300 under a load of 0·0054 mN/dtex (::, not cut off) 4. Residue 4. The flame-retardant fiber assembly of claim 2, wherein the above-mentioned element-containing fiber is at 0.0054 The load of mN/dtex increases the temperature from 50 ° C to 300. (: When it is not cut off, it remains. 152753.doc 201134992 5. The flame-retardant fiber assembly according to any one of claims 1 to 4, The metal compound (2) contains a metal compound (2)) which promotes two reactions of the de-reaction and carbonization reaction, or a combination of the above-mentioned metal compound (5)) and a metal compound (2-2) which promotes a degumming reaction. The flame-retardant fiber assembly according to any one of claims 1 to 4, wherein the dentate-containing fiber is subjected to one-time stretching by extruding a spinning solution containing the polymer (1) and the metal compound (2) After washing with water, it is dried, subjected to secondary stretching, and subjected to heat treatment to be spun, and the stretching ratio at the time of the stretching is multiplied by the ratio of the fiber shrinkage at the time of the heat treatment, that is, the ratio of the relaxation is 5 times or less. 7. The flame-retardant fiber assembly according to any one of claims 1 to 4, wherein the dentate-containing fiber contains the above-mentioned metal compound (1) with respect to 1 〇〇 by mass of the polymer (1). ) 0.05 The non-flammable fiber assembly of claim 5, wherein the dentate fiber contains the metal compound Ρ-2) 5 to 30 parts by mass based on 100 parts by mass of the polymer (1). 9. The flame-retardant fiber assembly of claim 5, wherein the metal compound (2_D is selected from the group consisting of oxidized words, zinc carbonate, zinc sulfide, boric acid, tin stannate, tin oxide, oxidized erbium, tin oxide) At least one of a group consisting of copper oxide, copper silicate, indium trioxide, indium (tetra), and zinc p-toluene. The flame retardant fiber assembly of claim 5, wherein the metal compound (2-2) is selected from the group consisting of ruthenium compounds, iron oxide, iron phosphate, iron oxalate, sulfurization 152753.doc 201134992 iron, ruthenium oxide, trioxane (tetra) At least one of the group consisting of oxygen (four), and moth copper. 11. The flame-retardant fiber assembly according to claim 5, wherein the metal compound (7) comprises a metal compound (2_1) which promotes both the de-reaction and the carbonization reaction, or the metal compound (2·1) and promotes dehalogenation. A combination of metallization of the reaction (2-2). 12. The flame-retardant fiber assembly according to any one of claims 1 to 4, wherein the flame-retardant fiber other than the above-mentioned pixel-containing fiber is selected from the group consisting of an aromatic polyamide fiber, a benzoic acid fiber, and a polystyrene sulfide. Fiber, polyetheretherketone fiber, polyimine fiber, polyamidimide fiber, flame retardant polyester fiber, melamine fiber, acrylate fiber, polyphenylene oxide fiber, polyvinyl chloride fiber, polyethylene gas Ethylene fiber, polystyrene fiber, polytetrafluoroethylene fiber, regenerated cellulose fiber containing inorganic compound, regenerated cellulose fiber containing phosphorus-based flame retardant, processed flame retardant cellulose fiber after coating with flame retardant, oxidized acrylic acid At least one of a group consisting of fibers, carbon fibers, glass fibers, and activated carbon fibers. The flame-retardant fiber assembly according to claim 12, wherein the flame-retardant fiber other than the dentate-containing fiber is selected from the group consisting of regenerated cellulose fibers containing a bismuth component, regenerated cellulose fibers containing a refractory filler, and coated The fuel agent is then processed into at least one of a group consisting of a flame retardant cellulose fiber, a melamine fiber, a flame retardant polyester fiber, an acrylate fiber, and an aromatic polyamide fiber. 14. The flame-retardant fiber assembly according to claim π, wherein the flame-retardant fiber other than the above-mentioned element-containing fiber is selected from the group consisting of regenerated cellulose fiber containing diarrhea component, 152753.doc 201134992, containing a phosphorus-based flame retardant. At least one of a group consisting of regenerated cellulose fibers, a flame retardant-coated cellulose fiber, and an aromatic polyamide fiber coated with a flame retardant. A method for producing a flame-retardant fiber assembly, characterized in that the flame-retardant fiber assembly system comprises a tooth-containing fiber, a polyester fiber, and a flame-retardant fiber other than a halogen-containing fiber; When the total amount of the above-mentioned flame-retardant fiber aggregate is 1% by mass, 3 to 30% by mass of the halogen-containing fiber, 20 to 50% by mass of the polyester fiber, and 3〇 ~77 mass% of the flame retardant fibers other than the dentate fibers are mixed; and the shrinkage fluctuation of the halogen-containing fiber at a load of 0.0054 mN/dtex from 5 〇C to 300 °C is 65% or less The halogen-containing fiber is spun by a composition comprising at least one metal compound (2) comprising a polymer (1) and a carbonization reaction which promotes the refinement of the polymer (1) and (4) Thereafter, it is obtained by performing heat treatment; and when the total amount of the above polymer (1) is set to 1 〇〇 mass 〇 /. In the above, the polymer (1) contains 30 to 7 % by mass of acrylonitrile, a styrene-containing ethylene monomer, and/or a dentate-containing vinyl monomer of 7 〇 to 3 〇% by mass, and a mixed ethylene group. Is a monomer. ~1〇% by mass. The method for producing a flame-retardant fiber assembly according to claim 15, wherein the spinning of the dentate-containing fiber is carried out by extruding a spinning solution containing the polymer (1) and the metal compound (2) After performing one extension and water washing, drying, second stretching, and heat treatment are carried out, and the stretching ratio at the time of stretching is multiplied by the ratio of fiber shrinkage at the above heat treatment, that is, the relaxation ratio is obtained by the above-mentioned 152753.doc 201134992 The total stretch ratio is 5 times or less. 17. The method of producing a flame-retardant fiber assembly according to claim 15 or 16, wherein the heat treatment is dry heat of 140 ° C or more or 9 Torr.热处理 Heat treatment in the above moist heat. 8. The method for producing a flame-retardant fiber assembly according to the item 15 or 16, wherein the heat treatment is a dry heat of 180 ° C or more or a heat treatment of moist heat of 15 Torr or more. 19. The method for producing a flame-retardant fiber assembly according to claim 17, wherein the heat treatment is 90 to 15 (relaxation heat treatment in wet heat of TC. 20. 20. a flame-retardant fiber assembly such as Kiss 15 or 16) The manufacturing method, wherein the heat treatment is a relaxation heat treatment in a moist heat pressurized steam of 100 〇 C or more. 21. A fibrous product, characterized by comprising a flame-retardant fiber assembly according to any one of the claims 丨 to 丨々. The flame-retardant fiber assembly according to any one of claims 4 to 4, wherein the flame-retardant fiber other than the dentate-containing fiber is a fiber having a L〇I value of 25 or more. A flame-retardant fiber assembly, wherein the flame-retardant fiber other than the halogen-containing fiber has a fiber having an LOI value of 25 or more. The fiber product is characterized by comprising a flame-retardant fiber assembly as claimed or η. The method for producing a flame-retardant fiber assembly according to claim 15 or 16, wherein the flame-retardant fiber other than the above-mentioned element-containing fiber has a L0I value of 25 or more. 152753.doc 201134992 26. The flame retardant of claim 19 Fabric assembly The method wherein the flame-retardant fiber other than the halogen-containing fiber has a LOI value of 25 or more. 27. The method for producing a flame-retardant fiber assembly according to claim 20, wherein the flame-retardant fiber other than the halogen-containing fiber is Fibers with an LOI value of 25 or higher. 152753.doc
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