JPS6029739B2 - Aromatic polyamide crystalline complex and method for producing aromatic polyamide crystalline complex - Google Patents
Aromatic polyamide crystalline complex and method for producing aromatic polyamide crystalline complexInfo
- Publication number
- JPS6029739B2 JPS6029739B2 JP1752676A JP1752676A JPS6029739B2 JP S6029739 B2 JPS6029739 B2 JP S6029739B2 JP 1752676 A JP1752676 A JP 1752676A JP 1752676 A JP1752676 A JP 1752676A JP S6029739 B2 JPS6029739 B2 JP S6029739B2
- Authority
- JP
- Japan
- Prior art keywords
- crystalline complex
- caprolactam
- aromatic polyamide
- pyrrolidone
- polymer
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
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- Polyamides (AREA)
Description
【発明の詳細な説明】
本発明は溶融成型可能な芳香族ポリアミド結晶性鍔体の
製造法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a melt-formable aromatic polyamide crystalline collar body.
近年芳香族ポリアミド重合体はその優れた耐熱性のため
に繊維、フィルム、樹脂あるいは紙に成型されて衣料用
、資材用、電気絶縁等に広く使用されている。In recent years, aromatic polyamide polymers have been widely used for clothing, materials, electrical insulation, etc. by being molded into fibers, films, resins, or papers due to their excellent heat resistance.
従来かかる芳香族ポリアミド重合体は極めて高い融点を
有するため溶融成型することは不可能であり、繊維、フ
ィルムあるいは紙に成型するには重合体をジメチルホル
ムアミド、Nメチル2ピロリドン、テトラメチル尿素な
どの極性有機溶媒に一度溶解し、この重合体溶液をノズ
ル、ダイスあるいはオリフィスから液体裕又はガス流中
に押出して溶媒を除去する所謂湿式又は乾式成型法が採
用されている。Conventionally, such aromatic polyamide polymers have extremely high melting points and cannot be melt-molded, and in order to be molded into fibers, films, or paper, the polymers must be prepared using dimethylformamide, N-methyl-2-pyrrolidone, tetramethylurea, etc. A so-called wet or dry molding method is employed in which the polymer solution is once dissolved in a polar organic solvent and the solvent is removed by extruding the polymer solution through a nozzle, die, or orifice into a liquid or gas stream.
しかしながらこの方法は高価な有機溶媒が必要であり、
又溶媒回収にも多額の費用を必要とする欠点を有してい
る。However, this method requires expensive organic solvents;
It also has the disadvantage of requiring a large amount of expense for solvent recovery.
又樹脂の成型法として重合体微粉末を圧縮成型すること
が試みられているが均一な製品を製造することが困難で
ある。このような背景から本発明者らは多量の溶媒を必
要としないでしかも低温度で芳香族ポリアミド重合体を
成型する方法について鋭意研究の結果、本発明に到達し
た。Compression molding of fine polymer powder has been attempted as a resin molding method, but it is difficult to produce uniform products. Against this background, the present inventors have conducted intensive research on a method for molding aromatic polyamide polymers at low temperatures without requiring a large amount of solvent, and have finally arrived at the present invention.
即ち本発明の要旨とするところは、25q0の濃硫酸1
00cc中に1.咳熔解したときの相対粘度が1.5〜
5.5であるポリmフエニレンイソフタルアミドと2ピ
ロリドン又はごカプロラクタムとからなる結晶性錯体及
び上記のポリmフェニレンイソフタルアミドと2ピロリ
ドン又はごカブロラクタムとを接触させて結晶性錆体を
形成せしめ、次いで結晶に含まれない2ピロリドン又は
ごカプロラクタムを除去して芳香族ポリアミド結晶性錆
体を製造する製造方法にある。That is, the gist of the present invention is that 25q0 concentrated sulfuric acid 1
1 in 00cc. Relative viscosity when dissolved is 1.5~
5.5, a crystalline complex consisting of poly-m-phenylene isophthalamide and 2-pyrrolidone or caprolactam, and the above-mentioned poly-m-phenylene isophthalamide and 2-pyrrolidone or caprolactam are brought into contact to form a crystalline rust body, Next, 2-pyrrolidone or caprolactam not included in the crystals is removed to produce an aromatic polyamide crystalline rust body.
本発明の結晶性鍔体はさらさらした物質であり、芳香族
ポリアミドと2ピロリドン又はごカプロラクタムとが結
晶格子内で共存して新規な結晶性鍵体を形成しているも
のと思われる。The crystalline key body of the present invention is a free-flowing substance, and it is thought that the aromatic polyamide and 2-pyrrolidone or caprolactam coexist in the crystal lattice to form a novel crystalline key body.
このような結晶性鍔体は従来この世に知られていない全
く新規な化学物質である。Such a crystalline body is a completely new chemical substance that has not been previously known to the world.
以下具体的に本発明の結晶性銭体の製造法を記載する。The method for manufacturing the crystalline coin body of the present invention will be specifically described below.
結晶性鍵体の製造に使用される有機溶媒は2ピロリドン
又はごカプロラクタムであり、単一で使用するのが好ま
しいが水、ベンゼン、メチルアルコール、エチルアルコ
ール、Nメチルピロリドン、ジメチルホルムアミド、ジ
メチルアセトアミド、テトラメチル尿素とうの溶媒を少
量混合して使用しても差支えない。使用する芳香族ポリ
アミド重合体の形態は特に制限はなく、粉末状物、常法
により繊維賦型した未配向の又は配向した繊維状物、フ
ィルム状物あるいは樹脂状物とういずれも使用可能であ
る。The organic solvent used in the production of the crystalline key body is 2-pyrrolidone or caprolactam, and it is preferable to use it alone, but water, benzene, methyl alcohol, ethyl alcohol, N-methylpyrrolidone, dimethylformamide, dimethylacetamide, There is no problem in using a small amount of tetramethylurea mixed with the solvent. The form of the aromatic polyamide polymer to be used is not particularly limited, and any of powder, unoriented or oriented fibrous material shaped into fibers by a conventional method, film-like material, or resin-like material can be used. .
又重合体の重合度は特に制限はないが好ましくは相対粘
度1.5〜5.5(25q0の濃硫酸100cc中1.
雌濃度で測定、以下同様)のものである。工業的には比
較的低温で短時間のうちに結晶性鈴体を形成するのが好
ましく、そのためには重合体の密度は1.3斑ノの以下
で且つ35000以上で30分以上の熱履歴を受けてい
ないものであることが望ましい。The degree of polymerization of the polymer is not particularly limited, but preferably has a relative viscosity of 1.5 to 5.5 (1.5 to 5.5 in 100 cc of concentrated sulfuric acid of 25 q0).
(measured in female concentration, the same applies hereafter). Industrially, it is preferable to form a crystalline polymer in a short time at a relatively low temperature, and for this purpose, the density of the polymer must be 1.3 or less, and the thermal history must be 35,000 or more and a thermal history of 30 minutes or more. It is desirable that the
このような芳香族ポリアミド重合体と溶媒との接触法は
、2ピロリドンの融点(24.6oo)以上、ごカプロ
ラクタムの融点(69o0)以上で重合体を溶解ないい
ま吸収せしめるか、あるいは2ピロリドンもしくはどカ
プロラクタムを溶解しうる溶媒で好ましくは芳香族ポリ
アミド重合体をも膨潤なし・しは溶解せしめる有機溶媒
を併用して重合体を溶解ないいま吸収せしめる。Such a method of contacting an aromatic polyamide polymer with a solvent can be carried out by dissolving or absorbing the polymer at a temperature higher than the melting point of 2-pyrrolidone (24.6oo) or higher than the melting point of caprolactam (69o0); A solvent capable of dissolving caprolactam, preferably an organic solvent which does not swell or dissolves the aromatic polyamide polymer, is used in combination to dissolve or absorb the polymer.
このときの重合体と2ピロリドン又はどカプロラクタム
の接触割合はモル比で溶媒重合体2以上存在させること
が好ましい。At this time, the contact ratio between the polymer and 2-pyrrolidone or docaprolactam is such that two or more solvent polymers are preferably present in a molar ratio.
重合体と溶媒とを接触させるときの温度は常温で両者を
よく混合したのち2ピロリドン単一溶媒の場合は25q
o以上150qoの範囲、ごカプロラクタム単一溶媒の
場合は7000以上15000の範囲で行うのが望まし
い。The temperature when bringing the polymer and the solvent into contact is room temperature, and after mixing both well, in the case of 2-pyrrolidone single solvent, 25q
It is preferable to use a range of 0 to 150 qo, and in the case of a single caprolactam solvent, a range of 7,000 to 15,000 qo.
次いで結晶性銭体に含まれない過剰の2ピロリドン又は
ごカプロラクタムを除去するために乾燥を行うが生成錨
体は低融点であるので乾燥温度は融点より低温則ち2ピ
ロリドンの場合130oo以下好ましくは110qo以
下、ごカプロラクタムの場合150午0以下好ましくは
130qo以下の温度条件を採用するのが好ましい。Next, drying is performed to remove excess 2-pyrrolidone or caprolactam that is not contained in the crystalline body, but since the generated anchor has a low melting point, the drying temperature is lower than the melting point, preferably 130 oo or less in the case of 2-pyrrolidone. It is preferable to adopt a temperature condition of 110 qo or less, and in the case of caprolactam, 150 qo or less, preferably 130 qo or less.
混合溶媒系の場合は、遠心脱溶媒、炉過、蟹去あるいは
濃縮等の乾燥処理を行ったのちに150℃以下の温度で
乾燥するのが望ましい。In the case of a mixed solvent system, it is desirable to dry at a temperature of 150° C. or lower after performing a drying process such as centrifugal desolvation, oven filtration, filtration, or concentration.
このようにして製造された鎧体は具体的には次に示すよ
うな特性値を有している。Specifically, the armor body manufactured in this manner has the following characteristic values.
例えば相対粘度3.2のポリmフェニレンィソフタルア
ミド粉末を150q0でごカプロラクタム中にごカプロ
ラクタム/重合体10/1(重量比)の割合で20分溶
解し、次に12000で真空乾燥して、結晶に含まれな
いごカプロラクタムを除去することにより結晶性錯体(
これを以下錯体Aと称する)を得た場合の銭体の特性は
次の如くである。錨体AのX線回折図は第1表及び第1
図の通りである。For example, polyphenylene isophthalamide powder with a relative viscosity of 3.2 is dissolved in caprolactam at a ratio of caprolactam/polymer 10/1 (weight ratio) for 20 minutes at 150 q0, and then vacuum dried at 12,000 ml. , the crystalline complex (
The properties of the complex obtained when this complex is obtained (hereinafter referred to as complex A) are as follows. The X-ray diffraction diagram of anchor A is shown in Table 1 and
As shown in the figure.
第1表明らかにポリmフエニレンイソフタルアミドある
いはごカプロラクタムとは異つた結晶構造を有している
。Table 1 clearly shows that poly(m-phenylene isophthalamide) has a crystal structure different from that of caprolactam.
密度の測定をデカリン中25℃で行ったところ1.20
g/めであった。The density was measured in decalin at 25°C and was 1.20.
It was g/m.
これは錆体の生成条件によって1.19〜1.2礎/地
に変動する。尚処理していないポリmフェニレンイソフ
タルアミド繊維の理論密度は1.47g/地、実測値は
1.3隣ノがである。This varies from 1.19 to 1.2 foundation/ground depending on the rust formation conditions. The theoretical density of the untreated polym-phenylene isophthalamide fiber is 1.47 g/ground, and the actual density is 1.3 g/ground.
第2図は銭体Aの赤外吸収スペクトルを示すものである
。FIG. 2 shows the infrared absorption spectrum of Senitai A.
融点はパーキンェルマー社製DSCO型により昇温速度
10℃/分でDSC曲線を測定することにより行った。The melting point was determined by measuring a DSC curve using a PerkinElmer DSCO model at a heating rate of 10° C./min.
結果は第3図の通りであり、15がoに吸熱ピークが認
められた。これより求めた融解熱△川ま12.7Cal
/gであった。これはポリmフヱニレンィソフタルアミ
ド重合体の融点(420℃)よりはるかに低く、本発明
の結晶性銭体が全く新規なものであることを示している
。錯体Aの動的粘弾性は第4図及び第5図に示す通りで
あり、第5図は動的損失率の温度依存性を示す。The results are as shown in FIG. 3, and an endothermic peak was observed at o for 15. Heat of fusion △ Kawama 12.7 Cal calculated from this
/g. This is much lower than the melting point (420° C.) of poly(m-phenylene isophthalamide) polymer, indicating that the crystalline coin body of the present invention is completely new. The dynamic viscoelasticity of Complex A is as shown in FIGS. 4 and 5, and FIG. 5 shows the temperature dependence of the dynamic loss rate.
12ぴ0を過ぎるあたりからはn6の急激な上昇があり
それに対応してE′は急激に低下しはじめる。From around 12pi0, n6 rises rapidly, and correspondingly, E' begins to fall sharply.
150℃以上では測定不可能となりこの温度城では流動
が起ると考えられる。Measurement becomes impossible at temperatures above 150°C, and it is thought that flow occurs at this temperature range.
この現象により本発明の結晶性鏡体は溶融紡糸、溶融成
型の可能性が示される。鍔体Aから鯛水抽出で脱溶媒を
行ったところポリmフエニレンイソフタルアミドとごカ
プロラクタムのモル比は1:1.98(=重量比53:
47)であつた。This phenomenon indicates the possibility of melt spinning and melt molding of the crystalline mirror of the present invention. When the solvent was removed from Tsuba body A by extraction with sea bream water, the molar ratio of polym-phenylene isophthalamide and caprolactam was 1:1.98 (=weight ratio 53:
47).
この値も鈴体の形成条件によって変化し重合体と溶媒の
モル比は0.17〜1.98のものが得られる。This value also changes depending on the conditions for forming the polymer, and a molar ratio of polymer to solvent of 0.17 to 1.98 can be obtained.
熱重量分析の結果は第6図に示す通りであり、空気中2
.5℃/分の昇温速度でTGA曲線を測定した。15が
○が鏡体Aの融点であり400qo以上が重合体の分解
点である。The results of thermogravimetric analysis are shown in Figure 6.
.. TGA curves were measured at a heating rate of 5° C./min. 15 is the melting point of mirror A, and 400 qo or more is the decomposition point of the polymer.
100qo迄はほとんど重量減少はないが、融点近傍か
らごカプロラクタムの脱藩煤が起り30000ではほぼ
完全に除かれている。There is almost no weight loss up to 100 qo, but caprolactam soot is removed near the melting point and is almost completely removed at 30,000 qo.
このときの脱溶媒の量は約43%であり抽出減量とほぼ
一致している。本発明の結晶性錆体は特に低融点という
特徴を生かして繊維、フィルム、不織布あるいはバイン
ダー等の出発物質として好適である。The amount of solvent removed at this time was about 43%, which is almost the same as the extraction loss. The crystalline rust body of the present invention is particularly suitable as a starting material for fibers, films, nonwoven fabrics, binders, etc. by taking advantage of its low melting point.
特に芳香族ポリアミド重合体に配向繊維を使用して結晶
性鍔体を形成したものは不織布のバインダーとして優れ
た性能を示すので有用である。また溶媒量が少〈低温成
形可能であることからフィルムの作成が容易となり電気
材料として優れた性質を有する芳香族ポリアミドを安価
に提供することを可能とする。In particular, an aromatic polyamide polymer in which a crystalline collar body is formed using oriented fibers is useful as it exhibits excellent performance as a binder for nonwoven fabrics. Further, since the amount of solvent is small (low-temperature molding is possible), it is easy to prepare a film, and it is possible to provide an aromatic polyamide having excellent properties as an electrical material at a low cost.
本発明の結晶性鍔体を繊維あるいはフィルムに押出し成
形する方法は例えば次の通りである。本発明の鍔体は上
述した通り常温では粉末状又はべレツト状であり一定の
温度以上で融解し軟化する。融解温度以上では重合体の
重合度及び溶媒の共存量により異るが1ぴ〜1ぴポィズ
の溶融粘度を有し押出し成形が可能である。この場合の
溶媒の共存量は重合体当りモル比で0.5〜2.5であ
ることが好ましくこれ以上の溶媒量になると可塑効果は
著しくなり溶融押出し‘ま可能であるがゲル押出しと同
じものになり、禾延伸物の構造形成が湿式押出しのそれ
に近く、強度も繊維の場合1g/d以下となり、紙糸速
度も数十m/分以下とする必要が生じて生産性が低くな
る。錯体を次いでその融解温度の500以上好ましくは
10午0以上の温度でノズル、Tダィとうから押出す。The method for extruding the crystalline collar body of the present invention into fibers or films is, for example, as follows. As mentioned above, the collar body of the present invention is in the form of a powder or pellet at room temperature, and melts and softens above a certain temperature. Above the melting temperature, it has a melt viscosity of 1 pipoise to 1 pipoise, depending on the degree of polymerization of the polymer and the amount of solvent present, and extrusion molding is possible. In this case, the amount of solvent coexisting is preferably 0.5 to 2.5 in terms of molar ratio per polymer, and if the amount of solvent exceeds this amount, the plasticizing effect becomes significant and melt extrusion is possible, but it is the same as gel extrusion. Therefore, the structure of the drawn product is close to that of wet extrusion, the strength is less than 1 g/d in the case of fibers, and the paper yarn speed has to be less than several tens of m/min, resulting in low productivity. The complex is then extruded through a nozzle, T-die, at a temperature of 500 degrees or more, preferably 10 degrees or more, of its melting temperature.
押出された成形物は一且捲き取るか捲き取らずに洗浄、
延伸、乾燥あるいは熱延伸工程を通すことによって賦型
される。尚洗浄と延伸とは同時に行ってもよいし逆の順
序で行ってもよい。繊維の場合は10仇h/分以上の押
出しが可能であり禾延伸糸において既に高い配向を示す
ようになる。次いで100oo近くの温水中で1〜5倍
の延伸を行う。乾燥の後少くとも3000C好ましくは
330℃以上に加熱された熱坂上を通過させ結晶化させ
つつ4倍以下の延伸をほどこす。本発明の芳香族ポリア
ミド重合体は繰返し構造単位の少くとも75モル%がm
フェニレンジアミンとィソフタル酸クロラィドの如きイ
ソフタル酸ハラィドとを溶液重合あるいは界面重合とう
の方法で反応させて得られるmフェニレンィソフタルア
ミドからなるものを対象とする。The extruded molded product can be washed once or without being rolled up.
It is shaped by stretching, drying or hot stretching. Note that washing and stretching may be performed at the same time or in the reverse order. In the case of fibers, it is possible to extrude at a rate of 10 h/min or more, and the drawn yarn already exhibits a high degree of orientation. Then, it is stretched 1 to 5 times in warm water at about 100 oo. After drying, the film is passed through a heating ramp heated to at least 3,000°C, preferably 330°C or higher, to crystallize it and stretch it by a factor of 4 times or less. In the aromatic polyamide polymer of the present invention, at least 75 mol% of the repeating structural units are m
The object of the invention is m-phenylene isophthalamide obtained by reacting phenylene diamine and isophthalic acid halide such as isophthalic acid chloride by solution polymerization or interfacial polymerization.
共重合成分が25モル%を越えると生成する結晶性鈴体
の結晶性が著しく低下し取扱い上好ましくない。必要に
応じて共重合される成分は、アミン成分としてはpフヱ
ニレンジアミン、ベンジジン、44ジアミノジフエニル
エーテル、44ジアミノジフェニルスルホンなどであり
、酸成分はテレフタル酸クロライド、1.4もしくは2
.6ナフタレンジカルボン酸クロライド、ジフェニルス
ルホン44ジカルボン酸クロラィド、ジフエニルェーナ
ル44ジカルボン酸クロライド等のジカルボン酸ハラィ
ドあるいはアミノ安息香酸ハラィド等である。また重合
体に含まれるカルシウム、リチウム、アルミニウム等の
金属イオンは数千脚を越えると別構造の鈴体を構成する
ので200跡以下であることが望ましい。If the copolymerization component exceeds 25 mol %, the crystallinity of the resulting crystalline polymer will be markedly reduced, making it unfavorable for handling. The components to be copolymerized as necessary include p-phenylenediamine, benzidine, 44-diaminodiphenyl ether, 44-diaminodiphenyl sulfone, etc. as the amine component, and terephthalic acid chloride, 1.4 or 2, as the acid component.
.. These include dicarboxylic acid halides such as 6-naphthalene dicarboxylic acid chloride, diphenylsulfone 44-dicarboxylic acid chloride, and diphenylhenal-44 dicarboxylic acid chloride, or aminobenzoic acid halides. Further, if the number of metal ions such as calcium, lithium, aluminum, etc. contained in the polymer exceeds several thousand, a bell body with a different structure will be formed, so it is desirable that the number of metal ions is 200 or less.
以下実施例により本発明を具体的に説明するが、本発明
は実施例に限定されるものではない。EXAMPLES The present invention will be specifically explained below with reference to Examples, but the present invention is not limited to the Examples.
実施例 1相対粘度が3.4のポリmフェニレンイソフ
タルアミドの粉末を2ピロリドン中に2ピロリドン/重
合体;10/1(重量比)の割合で15000、2時間
浸潰し、重合体を炉別後6ぴ0、2脚Hgで5時間減圧
乾燥を行った。Example 1 Powder of polym-phenylene isophthalamide having a relative viscosity of 3.4 was soaked in 2-pyrrolidone at a ratio of 2-pyrrolidone/polymer: 10/1 (weight ratio) for 15,000 hours for 2 hours, and the polymer was separated in a furnace. After that, vacuum drying was carried out for 5 hours at 0.0 and 2-hour Hg.
このもののX線回折図には20=11.0o m,17
.40v.s,18.40w,20.20w,21.0
0w,23.20v.s,25.00s,26.20m
,27.4omに鋭い吸収が認められた。これらはポリ
mフェニレンィソフタルアミド結晶の吸収とは異るもの
である。鏡体の沸水抽出率は37M%であり又融点は1
30qoであった。銭体を10孔の続糸口金を通して1
5000で鉄糸圧力65k9/地で押出した。The X-ray diffraction diagram of this material shows 20=11.0o m, 17
.. 40v. s, 18.40w, 20.20w, 21.0
0w, 23.20v. s, 25.00s, 26.20m
A sharp absorption was observed at , 27.4 om. These are different from the absorption of polym-phenylene isophthalamide crystals. The boiling water extraction rate of the enantiomer is 37M%, and the melting point is 1
It was 30qo. Pass the coin body through the 10-hole connecting thread cap.
5000 and extruded with iron thread pressure 65k9/ground.
紡出糸を20皿/分の速度で巻取った。The spun yarn was wound at a speed of 20 plates/min.
禾延伸糸を20肌/分で俗長3hの洗浄俗に送込み10
0qoで洗浄しつつ3仇h/分のテークアップロールで
1.9音の延伸を行った。ついで150℃の乾燥ローフ
及び320qoの加熱板上を通過せしめて全部で3倍の
延伸を行った。このャーンは良好な外観と光沢を有し、
そのフィラメントは2dであり、強度4.雌ノd、伸度
35%、初期モジュラス110gノdであった。又相対
粘度3.5のポリmフェニレンイソフタルアミド粉末の
代りに平均重合度5の末端COO日のオリゴマ−を使用
して上と同機の処理を行ったところ融点は11が0であ
った。The drawn yarn was fed into a washing machine with a length of 3 hours at 20 threads/min for 10 minutes.
While washing at 0qo, stretching was carried out at 1.9 degrees using a take-up roll at 3 hours/minute. The film was then passed through a dry loaf at 150° C. and a hot plate at 320 qo to achieve a total stretching of 3 times. This yarn has good appearance and gloss,
The filament is 2d and has a strength of 4. Female No. d, elongation 35%, initial modulus 110 g No. d. When the same process as above was carried out using an oligomer with an average degree of polymerization of 5 and a terminal COO day instead of poly(m-phenylene isophthalamide powder) having a relative viscosity of 3.5, the melting point was 0 instead of 11.
実施例 2
相対粘度が3.5のポリmフェニレンィソフタルアミド
の粉末をごカプロラクタムの粉末とをモル比で1:10
の割合で混合後、15000に昇温し溶解した。Example 2 Polymer phenylene isophthalamide powder with a relative viscosity of 3.5 was mixed with caprolactam powder in a molar ratio of 1:10.
After mixing at a ratio of , the temperature was raised to 15,000 °C to dissolve.
次いで110qo、120qo、130℃で2柳Hgの
減圧下6時間乾燥した。このもののX線回折図20には
、9‐00,11‐80,17‐90,19‐80,2
3‐30,24.50及び28.70 に明瞭な吸収が
認められた。これら錆体はいずれもさらさらした乾いた
感触を与え取扱いは容易であった。これら錯体のメタノ
ール抽出減量から求めた重合体/ごカプロラクタム モ
ル比、DSC曲線から求めた融点は次の通りであった。Then, it was dried at 110 qo, 120 qo, and 130° C. for 6 hours under a reduced pressure of 2 Yanagi Hg. The X-ray diffraction diagram 20 of this product shows 9-00, 11-80, 17-90, 19-80, 2
Clear absorption was observed at 3-30, 24.50 and 28.70. All of these rust bodies had a smooth and dry feel and were easy to handle. The polymer/caprolactam molar ratio determined from the methanol extraction loss of these complexes and the melting point determined from the DSC curve were as follows.
第2表
修霧成条件
体重合参力プロラクタムもし比融点
1 110℃ 1.43 152℃
2 120 1.98
1563 1130 0.3
140No.2の鈴体を1のLの級糸口金
を通して17500で紡糸圧力65X9/地で押出して
、紙出糸を20仇h/分の速度で巻取った。Table 2: Modification of atomization conditions Polymerization prolactam If specific melting point 1 110℃ 1.43 152℃
2 120 1.98
1563 1130 0.3
140No. The threads of No. 2 were extruded through a L-grade yarn nozzle of No. 1 at 17500 at a spinning pressure of 65 x 9/cloth, and the paper yarn was wound at a speed of 20 h/min.
未延伸糸を2位h/分で俗長3mの洗浄俗に送込み10
0℃で洗浄しつつ3仇h/分のテークアップロールで1
.3音の延伸を行った。ついで17000の乾燥ローラ
及び350二0の加熱坂上を通過せしめ全部で3倍の延
伸を行った。2dのフィラメントは強度4.鴇ノd、伸
度30%、初期モジユラス100gノdであった。Feed the undrawn yarn into a washing machine with a general length of 3 m at a rate of 2 h/min for 10 minutes.
1 with a take-up roll of 3 h/min while washing at 0℃
.. Three notes were extended. Then, the film was passed through a 17,000 mm drying roller and a 35,020 mm heating ramp to achieve a total stretching of 3 times. 2d filament has a strength of 4. The initial modulus was 100g, the elongation was 30%, and the initial modulus was 100g.
実施例 3
実施例2と同一の重合体粉末をジメチルアセトアミド‘
こ溶解後常法により乾式紡糸し、沸水中で洗浄後乾燥し
て未延伸糸を得た。Example 3 The same polymer powder as in Example 2 was mixed with dimethylacetamide'.
After this dissolution, dry spinning was carried out by a conventional method, washed in boiling water, and dried to obtain an undrawn yarn.
未延伸糸は強度0.総/d、伸度230%、密度1.3
4斑/地であった。この未延伸糸を80℃の熱水中で3
.6倍に延伸し、次いで25000熱板上で1.0倍に
乾燥熱処理した。この熱処理糸を第3表に示すような溶
媒中に分散し、50ooで6時間保持た後、炉別し2肋
Hg、120こCで減圧乾燥して鏡体を形成した。The strength of undrawn yarn is 0. Total/d, elongation 230%, density 1.3
There were 4 spots/ground. This undrawn yarn was placed in hot water at 80°C for 30 minutes.
.. It was stretched to 6 times and then dry heat treated to 1.0 times on a 25,000 hot plate. This heat-treated yarn was dispersed in a solvent as shown in Table 3, held at 50 oo for 6 hours, separated in a furnace, and dried under reduced pressure at 2 Hg and 120 C to form a mirror body.
これらの鍔体は実施例2と同様なX線回折図を示し結晶
性錆体であった。第3表にこれら鍔体の特性を示した。These flanges showed an X-ray diffraction pattern similar to that of Example 2, and were crystalline rust bodies. Table 3 shows the characteristics of these collar bodies.
第 3 表
※ 6cp:6力ブロラクヌム
実施例 4
実施例1と同一の重合体粉末を100qoでごカプロラ
クタム/2ピロリドン/重合体の重合割合10/90/
20の溶液を作成し120q0で2肋Hgの減圧下6時
間乾燥した。Table 3 * 6 cp: Six-force Brolacnum Example 4 The same polymer powder as in Example 1 was added to 100 qo at a polymerization ratio of caprolactam/2-pyrrolidone/polymer 10/90/
A solution of No. 20 was prepared and dried at 120q0 under a reduced pressure of 2 Hg for 6 hours.
得られた試料のX線回折図には実施例1及び実施例2に
記載した2種類の鍔体の反射が観測され融点は130o
o及び151℃に観測された。In the X-ray diffraction diagram of the obtained sample, reflections from the two types of flanges described in Example 1 and Example 2 were observed, and the melting point was 130o.
o and 151°C.
本発明にかかる銭体Aの各特性を示すものであり、第1
図はX線回折図、第2図は赤外線吸収スペクトル、第3
図はDSC曲線、第4図及び第5図は動的粘弾性、第6
図はTGA曲線を各示す。
外′欧外2図
氷3図
外5図
外4図
外5図It shows each characteristic of the coin body A according to the present invention, and the first
The figure is an X-ray diffraction diagram, Figure 2 is an infrared absorption spectrum, and Figure 3 is an infrared absorption spectrum.
The figure shows the DSC curve, Figures 4 and 5 show dynamic viscoelasticity, and Figure 6 shows the dynamic viscoelasticity.
The figure shows each TGA curve. Outside Europe 2 figures ice 3 figures outside 5 figures outside 4 figures outside 5 figures
Claims (1)
きの相対粘度が1.5〜5.5であるポリmフエニレン
イソフタルアミドと2ピロリドン又はεカプロラクタム
とからなる結晶性錯体2 ポリmフエニレンイソフタル
アミドと2ピロリドンとからなる、X線回折角(2θ)
が11.0°(m)、17.4°(v.s)、18.4
°(w)、20.2°(w)、21.0°(w)、23
.2°(s)、25.0°(s)、26.2°(m)、
27.4°(m)に吸収を示す特許請求の範囲第1項の
結晶性錯体3 ポリmフエニレンイソフタルアミドと2
ピロリドンとを接触させて結晶性錯体を形全せしめ、次
いで結晶に含まれない2ピロリドンを除去して製造され
たX線回折角(2θ)が11.0°(m)、17.4°
(v.s)、18.4°(w)、20.2°(w)、2
1.0°(w)、23.2°(s)、25.0(s)、
26.2°(m)、27.4°(m)に吸収を示す特許
請求の範囲第1項又は第2項の結晶性錯体4 ポリmフ
エニレンイソフタルアミドとεカプロラクタムからなる
、X線回折角(2θ)が9.0°(s)、11.8°(
w)、17.9°(v.s)、19.8°(m)、23
.3°(v.s)、24.5°(m)、28.7°(v
.w)に吸収を示す特許請求の範囲第1項の結晶性錯体
5 ポリmフエニレンイソフタルアミドとεカプロラク
タムとを接触させて結晶性錯体を形成せしめ、次いで結
晶に含まれないεカプロラクタムを除去して製造された
X線回折角(2θ)が9.0°(s)、11.8°(w
)、17.9°(v.s)、19.8°(m)、23.
3°(v.s)、24.5°(m)、28.7°(v.
w)に吸収を示す特許請求の範囲第1項又は第4項の結
晶性錯体6 25℃の濃硫酸100cc中に1.0g溶
解したときの相対粘度が1.5〜5.5であるポリmフ
エニレンイソフタルアミドと2ピロリドン又はεカプロ
ラクタムとを接触させて結晶性錯体を形成せしめ、次い
で結晶に含まれない2ピロリドン又はεカプロラクタム
を除去することを特徴とする芳香族ポリアミド結晶性錯
体の製造法1 Crystalline complex consisting of poly-m phenylene isophthalamide and 2-pyrrolidone or ε-caprolactam, which has a relative viscosity of 1.5 to 5.5 when 1.0 g is dissolved in 100 cc of concentrated sulfuric acid at 25° C. 2 Poly-m phenylene isophthalamide X-ray diffraction angle (2θ) of nylene isophthalamide and 2-pyrrolidone
are 11.0° (m), 17.4° (v.s), 18.4
°(w), 20.2°(w), 21.0°(w), 23
.. 2° (s), 25.0° (s), 26.2° (m),
Crystalline complex 3 of claim 1 exhibiting absorption at 27.4° (m) Polym-phenylene isophthalamide and 2
The X-ray diffraction angles (2θ) produced by contacting with pyrrolidone to form a crystalline complex and then removing 2-pyrrolidone not included in the crystals are 11.0° (m) and 17.4°.
(v.s), 18.4° (w), 20.2° (w), 2
1.0° (w), 23.2° (s), 25.0 (s),
Crystalline complex 4 according to claim 1 or 2, which exhibits absorption at 26.2° (m) and 27.4° (m). The angle (2θ) is 9.0° (s), 11.8° (
w), 17.9° (v.s), 19.8° (m), 23
.. 3° (v.s), 24.5° (m), 28.7° (v.s.
.. Crystalline complex 5 according to claim 1 exhibiting absorption in w) Polym-phenylene isophthalamide and ε-caprolactam are brought into contact to form a crystalline complex, and then ε-caprolactam not included in the crystals is removed. The X-ray diffraction angle (2θ) produced by
), 17.9° (v.s), 19.8° (m), 23.
3° (v.s), 24.5° (m), 28.7° (v.s.
Crystalline complex 6 according to claim 1 or 4, which exhibits absorption in w) A polyester having a relative viscosity of 1.5 to 5.5 when 1.0g is dissolved in 100cc of concentrated sulfuric acid at 25°C. Production of an aromatic polyamide crystalline complex characterized by contacting m-phenylene isophthalamide with 2-pyrrolidone or ε-caprolactam to form a crystalline complex, and then removing 2-pyrrolidone or ε-caprolactam that is not included in the crystals. law
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1752676A JPS6029739B2 (en) | 1976-02-20 | 1976-02-20 | Aromatic polyamide crystalline complex and method for producing aromatic polyamide crystalline complex |
| US05/734,009 US4081430A (en) | 1975-10-20 | 1976-10-19 | Aromatic polyamide crystalline complex and the method for producing the same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1752676A JPS6029739B2 (en) | 1976-02-20 | 1976-02-20 | Aromatic polyamide crystalline complex and method for producing aromatic polyamide crystalline complex |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS52101298A JPS52101298A (en) | 1977-08-25 |
| JPS6029739B2 true JPS6029739B2 (en) | 1985-07-12 |
Family
ID=11946362
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1752676A Expired JPS6029739B2 (en) | 1975-10-20 | 1976-02-20 | Aromatic polyamide crystalline complex and method for producing aromatic polyamide crystalline complex |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6029739B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS58109618A (en) * | 1981-12-22 | 1983-06-30 | Teijin Ltd | Aromatic polyamide fiber, its aggregate and preparation thereof |
-
1976
- 1976-02-20 JP JP1752676A patent/JPS6029739B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS52101298A (en) | 1977-08-25 |
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