JPS59603B2 - Method for producing short fibers and/or pulp particles - Google Patents
Method for producing short fibers and/or pulp particlesInfo
- Publication number
- JPS59603B2 JPS59603B2 JP50005980A JP598075A JPS59603B2 JP S59603 B2 JPS59603 B2 JP S59603B2 JP 50005980 A JP50005980 A JP 50005980A JP 598075 A JP598075 A JP 598075A JP S59603 B2 JPS59603 B2 JP S59603B2
- Authority
- JP
- Japan
- Prior art keywords
- short fibers
- solution
- tables
- formulas
- pulp particles
- 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
Links
Landscapes
- Artificial Filaments (AREA)
- Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
- Paper (AREA)
Description
【発明の詳細な説明】
産業上の利用分野
本発明は、耐熱性、機械的性質等の優れた短繊維及び/
又はパルプ粒子を製造する方法に関する。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention is directed to short fibers and/or fibers with excellent heat resistance, mechanical properties, etc.
Or it relates to a method of producing pulp particles.
さらに詳しくは合成紙原料、樹脂補強材、摩擦材等の用
途に好適な、フィフリル化した短繊維及び/又はパルプ
粒子を工業的に製造する方法に関する。従来技術従来、
全芳香族ポリアミド、例えばポリ(パラフェニレンテレ
フタルアミド)、ポリ(メタフェニレンイソフタルアミ
ド)は耐熱性、機械的特性、電気的特性等の優れたパル
プ粒子(フィフリット)、繊維、フィルム、シート状物
、樹脂、積層材の原料として有用であることが知られて
いる。More specifically, the present invention relates to a method for industrially producing fifurlated short fibers and/or pulp particles suitable for use as synthetic paper raw materials, resin reinforcing materials, friction materials, and the like. Conventional technology
Fully aromatic polyamides, such as poly(paraphenylene terephthalamide) and poly(metaphenylene isophthalamide), have excellent heat resistance, mechanical properties, electrical properties, etc., and are useful for pulp particles (fifrites), fibers, films, sheet materials, It is known to be useful as a raw material for resins and laminated materials.
例えば、特公昭47−2489号公報にはポリ(パラフ
ェニレンテレフタルアミド)又はそのコポリマーから得
られる高強度、高モジユラスの繊維について記載されて
おり、また、特開昭47一23602号公報には、ポリ
(メタフェニレンイソフタルアミド)等の非融解性全芳
香族ポリアミドのフィフリットを用いた合成紙が記載さ
れている。For example, Japanese Patent Publication No. 47-2489 describes high strength and high modulus fibers obtained from poly(paraphenylene terephthalamide) or its copolymer, and Japanese Patent Publication No. 47-123602 describes Synthetic papers using fifrits of non-melting wholly aromatic polyamides such as poly(metaphenylene isophthalamide) have been described.
しかしながら、前述の高強度・高モジユラス繊維は、短
繊維に切断するのに特別の工夫・装置を要し、またその
ままでは合成紙原料、摩擦材等の分野には使用し難い。However, the above-mentioned high-strength, high-modulus fibers require special measures and equipment to be cut into short fibers, and are difficult to use as they are in fields such as synthetic paper raw materials and friction materials.
一方、ポリ(メタフェニレンイソフタルアミド)のフィ
フリットは耐熱性合成紙の原料として適当なものとされ
ているが、実質的に分子配向していないため強度に劣る
という問題があり、また、樹脂補強材、摩擦材等の分野
には不適当であるという問題がある。発明の目的
本発明の主たる目的は、配向した成形物をフィフリル化
させて、従来の全芳香族ポリアミド繊維やフィフリット
とは異なる短繊維及び/又はパルプ粒子を製造すること
にある。On the other hand, poly(metaphenylene isophthalamide) fifrit is considered to be suitable as a raw material for heat-resistant synthetic paper, but it has the problem of poor strength because it is not substantially oriented, and it is also used as a resin reinforcing material. , there is a problem that it is unsuitable for the field of friction materials, etc. OBJECTS OF THE INVENTION The main object of the present invention is to produce short fibers and/or pulp particles different from conventional wholly aromatic polyamide fibers and fifrites by fibrillating an oriented molded product.
本発明の他の目的は、合成紙原料、樹脂強化材、摩擦材
等として好適な剛直な全芳香族ポリアミドから成るフィ
フリル化した短繊維及び/又はパルプ粒子を製造するこ
とにある。Another object of the present invention is to produce fifurlated short fibers and/or pulp particles made of a rigid wholly aromatic polyamide suitable as a synthetic paper raw material, a resin reinforcement material, a friction material, etc.
発明の構成
本発明は、主として下記反復単位〔1〕で構成される剛
直な全芳香族ポリアミドの光学的異方性溶液から成形し
た分子配向性を有する成形物に、機械的操作によつて剪
断力を加え、該成形物を糸状に砕いてフィフリル化させ
ることを特徴とする短繊維及び/又はパルプ粒子の製造
法である。Components of the Invention The present invention relates to a molded article having molecular orientation formed from an optically anisotropic solution of a rigid wholly aromatic polyamide mainly composed of the following repeating units [1], and which is sheared by mechanical operation. This is a method for producing short fibers and/or pulp particles, which is characterized by applying force to crush the molded product into threads to form fibrils.
〔但し式中Arl及びAr2は、あるいはこれらの混合
物を表わす。[However, in the formula, Arl and Ar2 represent a mixture thereof.
〕本発明において用いる「剛直な全芳香族ポリアミド]
としては、ポリ(パラフエニレンテレフタルアミド)が
好ましいが、芳香核の水素の一部が塩素で置換されたも
のでもよい。] “Rigid wholly aromatic polyamide” used in the present invention
Although poly(paraphenylene terephthalamide) is preferable, it may also be one in which some of the hydrogen atoms in the aromatic nucleus are replaced with chlorine.
この全芳香族ポリアミドは固有粘度(ηInh)にして
1.5以上の重合度を有する必要がある。This wholly aromatic polyamide must have a degree of polymerization of 1.5 or more in terms of intrinsic viscosity (ηInh).
なお、ここで言う固有粘度(ηInll)は、ポリマー
組成物からポリマーを粉末として取り出し、濃硫酸中0
.57/100m1の濃度で30℃において測定した値
である。本発明において用いる前記の剛直な全芳香族ポ
リアミドは、種々の方法によつて溶液化できるものが多
い。Note that the intrinsic viscosity (ηInll) referred to here refers to the polymer taken out as a powder from the polymer composition and 0.0
.. The value was measured at 30° C. at a concentration of 57/100ml. Many of the rigid wholly aromatic polyamides used in the present invention can be made into a solution by various methods.
すなわち適当な溶剤又はさらに溶解助剤等と適当な温度
、圧力等の条件下に混合することによつても溶液を調製
できる。あるいは、これらのポリマーは一般に難溶性で
あるので、ポリマー組成に相当する混合比のモノマー系
から溶液重合法によつて調製せしめた重合進行系又は重
合の終了した混合系をそのまXあるいは副生するHCl
等を中和した系を成形に供することもできる。また、か
かる剛直なポリマーの一つの属性として特定の溶剤系中
で、特定の濃度範囲、特定の温度範囲では光学的異方性
溶液を与えることが知られており(特公昭47−248
9号公報、西独特許公開公報第1810426号公報、
米国特許第3671542号明細書参照)、かかる光学
的異方性溶液から湿式、乾式等の溶液成形法によつて分
子配向性を有する成型物を得ることが可能である。That is, a solution can also be prepared by mixing with a suitable solvent or a solubilizing agent under conditions such as suitable temperature and pressure. Alternatively, since these polymers are generally poorly soluble, a polymerized system prepared by a solution polymerization method from a monomer system with a mixing ratio corresponding to the polymer composition or a mixed system after polymerization can be directly used as X or as a by-product. HCl
It is also possible to use a neutralized system for molding. Furthermore, it is known that one of the attributes of such rigid polymers is that they give optically anisotropic solutions in a specific solvent system, at a specific concentration range, and at a specific temperature range (Japanese Patent Publication No. 47-248
No. 9, West German Patent Publication No. 1810426,
(See US Pat. No. 3,671,542), it is possible to obtain a molded article having molecular orientation from such an optically anisotropic solution by a wet or dry solution molding method.
本発明で用い得る分子配向性を有する成型物とは光学的
異方性溶液から得られた成形物のみに限定され、同じポ
リマーでも等方性溶液からのものはフィフリル化し難い
ので好ましくない。Molded products having molecular orientation that can be used in the present invention are limited to those obtained from optically anisotropic solutions, and even if the same polymer is produced from an isotropic solution, it is difficult to fifuryl, so it is not preferred.
すなわち、光学的異方性溶液においてはすでに溶液構造
からかなりの分子配向の状態又はより分子配向をし易い
状態にあり、得られた成形物は分子配向を有しかつフィ
フリル化し易いので本発明においては、光学的異方性溶
液からの成形物が用いられる。ここに云う光学的異方性
溶液は、例えば特開昭47−39458号にも述べられ
ているが、簡便な判定法の一つは溶液が肉眼では乳濁状
にみえ、かつ偏光顕微鏡で偏光子を回転させて観察した
場合、完全に視野が暗くなる角度の無いものである。こ
のような光学的異方性溶液は組成比、温度、添加剤等を
適当に選べば溶液成形に適する流動性、流延性、曵条性
等の特性をもたせることができる。このような光学的異
方性を有する重合体溶液は、水系沈澱中に導入し、微細
な粒子として沈澱させても良いが、口金ノズル、スリツ
ト等を通して塊状、粒状、粉末状、フイラメント状、ヒ
モ状、膜状、シート状、スプレー状に凝固浴又は凝固雰
囲気中に押し出してもよい。得られた成型物はさらに延
伸、熱処理を行つて配向・結晶化を高めるか又は処理を
行わずにそのまま糸状に砕いてフイフリル化することに
よつてもパルプ粒子及び/又は短繊維を製造することが
できる。本発明の方法では、成形時のノズル径、スリツ
ト幅、押し出し速度、凝固系の種類及び温度、巻き取り
速度、脱溶媒、脱塩速度とタイミング、あるいは成形物
の熱処理等の成形条件を適当に組み合せることにより、
後で該成形物を糸状に砕いて得られるパルプ粒子及び/
又は短繊維の諸特性、とくにその形状と機械的性質をコ
ントロールでき、さらに適当な条件では短繊維の長さ及
びその分布についてもある程度のコントロールができる
。In other words, in an optically anisotropic solution, the solution structure is already in a state of considerable molecular orientation or a state in which molecular orientation is more likely to occur, and the obtained molded product has molecular orientation and is easily fifurlated. A molded article made from an optically anisotropic solution is used. The optically anisotropic solution referred to here is described in, for example, Japanese Patent Application Laid-Open No. 47-39458, but one simple method for determining this is that the solution looks milky to the naked eye and is polarized under a polarizing microscope. When the child is rotated and observed, there is no angle at which the field of view becomes completely dark. Such an optically anisotropic solution can be made to have properties such as fluidity, castability, and stringability suitable for solution molding by appropriately selecting the composition ratio, temperature, additives, etc. A polymer solution having such optical anisotropy may be introduced into an aqueous precipitation system and precipitated as fine particles, but it may be passed through a nozzle, slit, etc. in the form of a lump, granule, powder, filament, or string. It may be extruded into a coagulation bath or coagulation atmosphere in the form of a shape, a film, a sheet, or a spray. Pulp particles and/or short fibers can also be produced by further stretching and heat-treating the obtained molded product to enhance orientation and crystallization, or by crushing it into filaments without any treatment to form fifuryls. Can be done. In the method of the present invention, the molding conditions such as the nozzle diameter, slit width, extrusion speed, type and temperature of the coagulation system, winding speed, desolvation, desalting speed and timing, or heat treatment of the molded product are adjusted appropriately. By combining,
Pulp particles and/or pulp particles obtained by crushing the molded product into threads later.
Alternatively, various properties of the short fibers, particularly their shape and mechanical properties, can be controlled, and under appropriate conditions, the length of the short fibers and their distribution can also be controlled to a certain extent.
本発明方法において、前記成形物は、必要ならば高温も
しくは低温の不活性気体雰囲気、水蒸気雰囲気、又は水
、塩化カルシウム水溶液、又は有機溶剤を含む水性凝固
浴中において、凝固、脱塩、脱溶媒を行うことができる
。なお、剛直な全芳香族ポリアミドから成る前記光学的
異方性溶液は、N−メチルピロリドン、ヘキサメチルホ
スホルアミドの如き比較的高沸点の溶媒や塩化リチウム
、塩化カルシウムの如き無機塩を含むことがある。In the method of the present invention, the molded article is coagulated, desalted, or desolventized in an inert gas atmosphere, a steam atmosphere, or an aqueous coagulation bath containing water, an aqueous calcium chloride solution, or an organic solvent, if necessary. It can be performed. The optically anisotropic solution made of rigid wholly aromatic polyamide may contain a relatively high boiling point solvent such as N-methylpyrrolidone or hexamethylphosphoramide, or an inorganic salt such as lithium chloride or calcium chloride. There is.
この場合、例えばセロフアン製造におけるが如くT型ダ
イ湿式法で膜状に成形することもできるが、押出後熱風
で溶媒の一部を除去した後適当なタイミングをもつて水
性凝固浴中に導入して浴中で脱溶媒と脱塩とを行うこと
により膜状物を成形するのがよい。一方、これらの溶液
の中には高温においてゲル化、相分離を起すものもある
のでインフレーシヨン法、カレンダー法等では一旦高温
で成形した後、適当な凝固浴中で脱溶媒、脱塩を行うこ
ともできる。さらに、とくに光学的異方性溶液は低温に
おいて溶液状からペースト状又は半固体状になるものも
あるので、冷却しながら成形物を得ることも可能である
。いずれにしても、分子配向性を有する成形物とすれば
よいのである。本発明に云う[分子配向性を有する成形
物]は、すでに内部に分子配向をした構造を有していれ
ばよく、巨視的には塊状、粒状、粉末状、シート状、フ
イルム状、膜状、ヒモ状、フイラメント状等の各種の形
態を取ることができる。In this case, it is also possible to form the film into a film using a T-die wet method, such as in the production of cellophane, but after extrusion, a part of the solvent is removed with hot air and then introduced into an aqueous coagulation bath at an appropriate timing. It is preferable to form a film-like product by removing the solvent and desalting in a bath. On the other hand, some of these solutions may undergo gelation or phase separation at high temperatures, so in the inflation method, calendar method, etc., after being molded at a high temperature, they are desolvated and desalted in an appropriate coagulation bath. You can also do this. Furthermore, since some optically anisotropic solutions change from a solution state to a paste state or a semi-solid state at low temperatures, it is also possible to obtain molded products while cooling. In any case, the molded product should have molecular orientation. The [molded product with molecular orientation] referred to in the present invention only needs to have a structure in which molecules are oriented internally, and macroscopically it can be in the form of a lump, granule, powder, sheet, film, or membrane. It can take various forms such as , string-like, filament-like, etc.
本発明者らの研究によれば、前述の如き剛直な全芳香族
ポリアミド、例えばポリ(パラフエニレンテレフタルア
ミド)からなる分子配向性を有する成形物は、一たん分
子配向した後は極めて配向緩和しにくいような高次組織
を作り易いので、配向方向に沿つて分子鎖密度の低い横
方向結合力の弱い部分を生じるため、これに適度の機械
的剪断力を加えると極めて容易にフィフリル化すること
ができ、目的とする短繊維及び/又はパルプ粒子を形成
することが判つた。According to the research conducted by the present inventors, molded articles made of rigid wholly aromatic polyamides such as those described above, such as poly(paraphenylene terephthalamide), and which have molecular orientation properties, have extremely relaxed orientation once the molecules have been oriented. Because it is easy to form a higher-order structure that is difficult to form, it creates areas along the orientation direction with a low molecular chain density and weak lateral bonding force, and when a moderate mechanical shearing force is applied to this area, it becomes extremely easy to fifuryl. It was found that the desired short fibers and/or pulp particles could be formed.
したがつて、本発明では上記の如き各種方法によつて得
られた(もしくは得られつつある)成形物を脱溶媒・脱
塩の前もしくは後、又は同時に、さらには、必要に応じ
て延伸又は圧延したりあるいはさらに熱処理した後、機
械的な剪断力を加えて糸状に砕いてフィフリル化させる
。Therefore, in the present invention, molded products obtained (or in the process of being obtained) by the various methods described above are subjected to stretching or stretching before or after desolvation and desalting, or at the same time as necessary. After rolling or further heat treatment, mechanical shearing force is applied to crush the material into threads to form fifurls.
本発明において前記成形物を糸状に砕いてフィフリル化
させるには、例えば粉砕、すり潰し、押し出し、衝撃、
叩解の様な機械的な剪断力を加えることが必要である。In the present invention, in order to crush the molded product into filiforms to form fibrils, for example, crushing, grinding, extrusion, impact,
It is necessary to apply mechanical shearing force such as beating.
剪断力を与える手段としては、各種グラインダー、ミル
、粉砕機等を用ることができる。さらに本工程は紙製造
における調整とかなりの類似性を有するので各種のヒー
ター、ジヨルダン、リフアイナ一等も適用できる。さら
にパルプ製造における砕木機グラインダーの一部も使用
できる。上述の配向した成形物に機械的な剪断力を与え
て糸状に砕く工程は成形物の製造と同時に行うこともで
きる。As means for applying shearing force, various grinders, mills, pulverizers, etc. can be used. Furthermore, since this process has considerable similarities with adjustments in paper manufacturing, various heaters, di-jordans, refiners, etc. can also be applied. Additionally, parts of the wood chipper grinder in pulp production can also be used. The above-described step of applying mechanical shearing force to the oriented molded product to crush it into threads can be performed simultaneously with the production of the molded product.
例えば溶液成形の場合は脱溶媒・脱塩と同時に又はその
後、又は熱処理の後に、湿式法あるいは乾式法によつて
行うこともできる。さらには、成形物をそのまま樹脂等
に混入し、混練時に加わる剪断力によつて糸状に砕かせ
ることも可能である。発明の効果
上述の如き本発明の方法によればポリマーの構造及び成
形に供するポリマー溶液の組成を選択することにより、
従来むしろこれら剛直なポリマーの欠点とされていた縦
方向に配向し縦方向に裂け易い(フィフリル化し易い)
という成形上の問題点をむしろ逆用して、有用なパルプ
粒子及び/又は短繊維を簡単な工程で製造することがで
きる。For example, in the case of solution molding, it can be carried out simultaneously with or after desolvation and desalination, or after heat treatment, by a wet method or a dry method. Furthermore, it is also possible to mix the molded product as it is into a resin or the like and crush it into threads by the shearing force applied during kneading. Effects of the Invention According to the method of the present invention as described above, by selecting the structure of the polymer and the composition of the polymer solution used for molding,
Traditionally, these rigid polymers were considered to have a disadvantage of being oriented in the longitudinal direction and easily tearing in the longitudinal direction (easily forming into fifurls).
By reversing this molding problem, useful pulp particles and/or short fibers can be produced in a simple process.
しかも、光学的等方性溶液を用いる場合に比して高いポ
リマー濃度で成形することができ、しかも配向し易い傾
向にあるので、これから得られた成形物は極めてフィフ
リル化し易く糸状に砕き易い。さらに大きな利点は、本
発明で特定した剛直な全芳香族ポリアミドからなる繊維
状物は高い剛性を有するものが多いので紡糸して得た糸
を短く切つて短繊維を得ることは困難が伴うか、切断機
に特殊な工夫・装置が必要であるのに比し、本発明の方
法では極めて容易に短繊維又は短繊維前1駆体を得るこ
とができる。本発明で得られたパルプ粒子及び/又は短
繊維は、そのフィフリル性及び優れた耐熱性機械的特性
を活かして耐熱性の絶縁紙などの強靭なシート状物に成
形することができる。Moreover, it is possible to mold with a higher polymer concentration than when using an optically isotropic solution, and since it tends to be more easily oriented, the molded products obtained therefrom are extremely easy to fifuril and break into threads. An even greater advantage is that many of the fibrous materials made of rigid wholly aromatic polyamides specified in the present invention have high rigidity, so it is difficult to obtain short fibers by cutting the spun yarn into short lengths. However, unlike the cutting machine that requires special measures and equipment, the method of the present invention allows short fibers or short fiber precursors to be obtained extremely easily. The pulp particles and/or short fibers obtained in the present invention can be formed into a strong sheet-like material such as heat-resistant insulating paper by taking advantage of their fifurlicity and excellent heat-resistant mechanical properties.
また、フィフリル化による大きい表面積に加えて、高い
機械的特性とくに高いモジユラスと強度を有し、さらに
ガラス繊維、炭素繊維、金属繊維等に較べて低比重であ
るので、樹脂強化用としても有用である。また、上述の
特性を利用して摩擦材に使用することもできる。実施例
以下に実施例をもつて本発明を説明する。In addition to a large surface area due to fifrillation, it has high mechanical properties, especially high modulus and strength, and has a lower specific gravity than glass fiber, carbon fiber, metal fiber, etc., so it is also useful for reinforcing resins. be. Moreover, it can also be used as a friction material by utilizing the above-mentioned characteristics. EXAMPLES The present invention will be explained below using examples.
なお実施例中有機極性溶媒はそれぞれヘキサメチルホス
ホルアミド(HMPA)、N−メチルピロリドン(NM
P)と略号を用いる。実施例 1
HMPA50m1とNMPlOOmlとからなる混合溶
媒に、パラフエニレンジアミン5661yを溶解させ炭
酸リチウム38687を加えて氷浴で冷却後、テレフタ
ル酸クロライドの粉末106297を添加して重合反応
を行つた。In the examples, the organic polar solvents were hexamethylphosphoramide (HMPA) and N-methylpyrrolidone (NMPA), respectively.
P) and abbreviations are used. Example 1 Paraphenylenediamine 5661y was dissolved in a mixed solvent consisting of 50ml of HMPA and NMPlOOml, lithium carbonate 38687 was added thereto, and after cooling in an ice bath, terephthalic acid chloride powder 106297 was added to carry out a polymerization reaction.
約30分後に光学的異方性溶液が得られた。このように
して得られたポリ(パラフエニレンテレフタルアミド)
の固有粘度は2.75であつた。この溶液は約7.5重
量%のポリマーを含んでいる。この溶液を100゜C幅
6mu1厚み0.17nrILのスリツトを通して50
m/分の速度で100℃の塩化カルシウム浴に押し出て
膜状物を得た。この膜状物を顕微鏡で観察するど縦方向
にシマ模様がみられ分子配向していることが認められた
。この膜状物をホモミキサー中で水とともに激しく攪拌
するとフィフリル化して短繊維が得られた。実施例 2
ポリ(パラフエニレンテレフタルアミド)(固有粘度5
.5)1007を85℃で硫酸400yに溶解して光学
的異方性溶液を得た。An optically anisotropic solution was obtained after about 30 minutes. Poly(paraphenylene terephthalamide) thus obtained
The intrinsic viscosity was 2.75. This solution contains approximately 7.5% by weight polymer. This solution was passed through a slit with a width of 6 mu and a thickness of 0.17 nm at 100°C for 50 min.
A membrane was obtained by extrusion into a calcium chloride bath at 100° C. at a speed of m/min. When this film-like material was observed under a microscope, a striped pattern was observed in the vertical direction, indicating that the molecules were oriented. When this film-like material was vigorously stirred with water in a homomixer, it was fifurlated and short fibers were obtained. Example 2 Poly(paraphenylene terephthalamide) (intrinsic viscosity 5
.. 5) 1007 was dissolved in 400y of sulfuric acid at 85°C to obtain an optically anisotropic solution.
この溶液を85゜Cで実施例1と同様のスリツトを用い
て5mmの空気層を通し圧延ローラーにかけながら3℃
の水中を通し得られた膜状物をNaHCO3水溶液と共
にホモミキサー中で攪拌した。得られた混合物を沢過、
水洗してボールミル中でさらに粉砕することにより短繊
維状物を得た。又ホモミキサーにかける前の膜状物を中
和、洗浄したのち緊張−Fに450℃で熱処理した後ボ
ールミルで粉砕しても短繊維状物が得られた。さらに土
述の450′Cで熱処理した膜状物を10mm長に切断
し不飽和ポリエステルのいわゆる生樹脂と混練すること
によりかなり均一に短繊維の分散した成形品を得ること
ができた。実施例 3
パラフエニレンジアミン10.817とパラフエニレン
ジアミン・2HC118.117とを、HMPA4OO
mlとNMPと200m1との混合溶媒中でテレフタル
酸クロライド40,877と重合反応させて調製した光
学的異方性を呈するぺースト状物を圧延ローラにて10
0℃で膜状に成形した後、ホモミキサー中でNaHCO
3水溶液にて中和しながら撹拌することによりパルプ状
粒子を調製した。This solution was heated at 85°C using a slit similar to that used in Example 1, passing through a 5 mm air layer and applying it to a rolling roller at 3°C.
The resulting film was stirred in a homomixer with an aqueous NaHCO3 solution. Filter the resulting mixture;
A short fibrous material was obtained by washing with water and further pulverizing in a ball mill. Further, short fibrous material was obtained even when the film-like material was neutralized and washed before being applied to the homomixer, heat-treated at 450 DEG C. under tension-F, and then ground in a ball mill. Furthermore, by cutting the film-like material heat-treated at 450'C as described above into 10 mm lengths and kneading it with so-called raw resin of unsaturated polyester, it was possible to obtain a molded article in which short fibers were dispersed fairly uniformly. Example 3 Paraphenylenediamine 10.817 and paraphenylenediamine 2HC118.117 were combined into HMPA4OO
A paste exhibiting optical anisotropy prepared by polymerization reaction with terephthalic acid chloride 40,877 in a mixed solvent of NMP and 200 ml was rolled with a rolling roller for 10 minutes.
After forming into a film at 0°C, NaHCO
Pulp-like particles were prepared by stirring while neutralizing with 3 aqueous solution.
この粒子は繊維状であつた。実施例 4
実施例1と同様にして重合、中和して調製した光学的異
方性溶液をドラム式溶液流延法フイルム製造装置で15
0℃の乾燥窒素ガスを送りつつ金属ドラム上で溶剤の一
部を除去し膜状物を成形した。The particles were fibrous. Example 4 An optically anisotropic solution prepared by polymerization and neutralization in the same manner as in Example 1 was heated for 15 minutes using a drum-type solution casting film manufacturing apparatus.
A part of the solvent was removed on a metal drum while supplying dry nitrogen gas at 0° C. to form a film.
この膜状物を水とともにヒーター(叩解機)にかけ脱水
、水洗後乾燥して短繊維を得た。実施例 5実施例1と
同様にして、調製した光学的異方性溶液を凝固浴をCa
cl2水溶液とする湿式キャスト法により成膜した。This film-like material was dehydrated by applying water to a heater (beater), washed with water, and dried to obtain short fibers. Example 5 An optically anisotropic solution prepared in the same manner as in Example 1 was added to a coagulation bath of Ca
The film was formed by a wet casting method using a Cl2 aqueous solution.
得られたフイルムをグラインダー中で砕くことにより短
繊維が得られた。実施例 6実施例3と同様にして、パ
ラフエニレンジアミン21.637とパラフェニレンジ
アミン・2HC118.I1yとをHMPA6OOml
とNMP3OOmlとの混合溶媒中でテレフノル酸クロ
ライド61.217と重合反応させて得られた重合反応
混合物を、光学的異方性を呈する高粘度の状態で、カレ
ンダー法の第1段ローラーで圧延し、第2段ローラーで
Ca(0H)2を含んだCacl2水溶液中で脱塩酸、
脱溶媒をしながらさらに圧延して得た膜状物をホモミキ
サー中に誘導して攪拌することにより短繊維を製造した
。Short fibers were obtained by crushing the obtained film in a grinder. Example 6 In the same manner as in Example 3, paraphenylenediamine 21.637 and paraphenylenediamine.2HC118. I1y and HMPA6OOml
The polymerization reaction mixture obtained by polymerizing with terephnoyl chloride 61.217 in a mixed solvent of , Dehydrochlorination in a CaCl2 aqueous solution containing Ca(0H)2 with a second stage roller,
The film-like material obtained by further rolling while removing the solvent was introduced into a homomixer and stirred to produce short fibers.
実施例 7
実施例1と同様にして調製した光学的異方性溶液を直径
0.5mTLの口金を通して糸状でホモミキサ一中に誘
導し、攪拌粉砕することにより繊維状のパルプ粒子を調
製した。Example 7 An optically anisotropic solution prepared in the same manner as in Example 1 was introduced in the form of a thread into a homomixer through a nozzle with a diameter of 0.5 mTL, and was stirred and ground to prepare fibrous pulp particles.
実施例 8
HMPA50m1とNMPlOOmlとからなる混合溶
媒にパラフエニレンジアミン5.6607を溶解させ氷
冷後、テレフタル酸クロライド10.678fを添加し
て重合反応を開始し、この重合反応が未だ完了していな
い光学的異方性溶液を遠心力で窒素気流下の壁面に衝突
させて得た主に膜状と塊状からなる成形物を、ホモミキ
サー中で水と攪拌後、Na2cO3水溶液で洗浄し、水
洗、脱水乾燥して短繊維とパルプ粒子を得た。Example 8 Paraphenylene diamine 5.6607 was dissolved in a mixed solvent consisting of 50 ml of HMPA and NMPlOOml, and after cooling on ice, 10.678 f of terephthalic acid chloride was added to start the polymerization reaction. A molded product mainly consisting of films and blocks obtained by colliding a non-optically anisotropic solution with a wall under a nitrogen stream using centrifugal force is stirred with water in a homomixer, washed with an aqueous Na2cO3 solution, and then washed with water. , dehydrated and dried to obtain short fibers and pulp particles.
Claims (1)
全芳香族ポリアミドの光学的異方性溶液から成形した分
子配向性を有する成形物に、機械的操作によつて剪断力
を加え、該成形物を糸状に砕いてフィブリル化させるこ
とを特徴とする短繊維及び/又はパルプ粒子の製造法。 ▲数式、化学式、表等があります▼………〔 I 〕〔但
し式中Ar_1及びAr_2は、▲数式、化学式、表等
があります▼、▲数式、化学式、表等があります▼、▲
数式、化学式、表等があります▼又は▲数式、化学式、
表等があります▼あるいはこれらの混合物を表わす。 〕。[Scope of Claims] 1 A molded article having molecular orientation formed from an optically anisotropic solution of a rigid wholly aromatic polyamide mainly composed of the following repeating units [I] is sheared by mechanical operation. A method for producing short fibers and/or pulp particles, which comprises applying force to crush the molded product into threads to form fibrils. ▲There are mathematical formulas, chemical formulas, tables, etc.▼……[I] [However, Ar_1 and Ar_2 in the formula are ▲There are mathematical formulas, chemical formulas, tables, etc.▼, ▲There are mathematical formulas, chemical formulas, tables, etc.▼, ▲
There are mathematical formulas, chemical formulas, tables, etc. ▼ or ▲ mathematical formulas, chemical formulas,
There are tables, etc. ▼ or a mixture of these. ].
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP50005980A JPS59603B2 (en) | 1975-01-14 | 1975-01-14 | Method for producing short fibers and/or pulp particles |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP50005980A JPS59603B2 (en) | 1975-01-14 | 1975-01-14 | Method for producing short fibers and/or pulp particles |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP22420484A Division JPS60126314A (en) | 1984-10-26 | 1984-10-26 | Production of pulp particle |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5182028A JPS5182028A (en) | 1976-07-19 |
| JPS59603B2 true JPS59603B2 (en) | 1984-01-07 |
Family
ID=11625964
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP50005980A Expired JPS59603B2 (en) | 1975-01-14 | 1975-01-14 | Method for producing short fibers and/or pulp particles |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59603B2 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002327392A (en) * | 2001-04-26 | 2002-11-15 | Sumitomo Chem Co Ltd | Low moisture absorption paper and method for producing the same |
| JP2009534550A (en) * | 2006-04-26 | 2009-09-24 | テイジン・アラミド・ビー.ブイ. | Method for purifying yarn or sliver |
| WO2012026498A1 (en) | 2010-08-27 | 2012-03-01 | 東邦テナックス株式会社 | Conductive sheet and production method for same |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59109558A (en) * | 1982-12-16 | 1984-06-25 | Matsushita Electric Ind Co Ltd | Method for producing high specific rigidity resin composition |
| JPS59163417A (en) * | 1983-03-08 | 1984-09-14 | Teijin Ltd | Production of microfine short fiber |
-
1975
- 1975-01-14 JP JP50005980A patent/JPS59603B2/en not_active Expired
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002327392A (en) * | 2001-04-26 | 2002-11-15 | Sumitomo Chem Co Ltd | Low moisture absorption paper and method for producing the same |
| JP2009534550A (en) * | 2006-04-26 | 2009-09-24 | テイジン・アラミド・ビー.ブイ. | Method for purifying yarn or sliver |
| WO2012026498A1 (en) | 2010-08-27 | 2012-03-01 | 東邦テナックス株式会社 | Conductive sheet and production method for same |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5182028A (en) | 1976-07-19 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JPS63288237A (en) | Cord from poly-p-phenylene-terephthalaminde | |
| JPH0627369B2 (en) | Aromatic polyamide fiber | |
| CN101517137B (en) | Method of manufacturing wholly aromatic polyamide filament and wholly aromatic polyamide filament manufactured thereby | |
| JP5340331B2 (en) | Fully aromatic polyamide filament | |
| JPS59603B2 (en) | Method for producing short fibers and/or pulp particles | |
| US4749753A (en) | Intimate mixture containing aromatic polyazole and aromatic copolyamide and process for its production | |
| JP2858869B2 (en) | Fiber material made from homogeneous alloy of aromatic polyamide and poly-N-vinylpyrrolidone, its production and use | |
| JP5186388B2 (en) | Process for producing para-type wholly aromatic polyamide particles | |
| EP0759454B1 (en) | para-ORIENTED AROMATIC POLYAMIDE MOLDING AND PROCESS FOR PRODUCING THE SAME | |
| JPS62162013A (en) | Production of pulp-like short fiber of poly(p-phenylene terephthalamide) | |
| JPS60126314A (en) | Production of pulp particle | |
| JP4204643B2 (en) | Aromatic polyamide pulp and method for producing the same | |
| JPH0352775B2 (en) | ||
| JPH10158213A (en) | Aromatic dicarboxylic acid fine powder | |
| US4081430A (en) | Aromatic polyamide crystalline complex and the method for producing the same | |
| KR920009000B1 (en) | Process for the production of full-aromatic polyamide short fibers | |
| CN117396643A (en) | Para-aramid fiber and method of preparing same | |
| JP2024518027A (en) | Method for producing aramid solution | |
| JPS63165514A (en) | Production of pulp granules | |
| JPS60110918A (en) | Aromatic copolyamide fiber | |
| JPH0116925B2 (en) | ||
| KR880000494B1 (en) | Aromatic Polyamide Fiber and Its Manufacturing Method | |
| JPS5933100B2 (en) | Manufacturing method for aromatic copolyamide molded products | |
| KR910004704B1 (en) | Producting process of full aromatic polyamide pulp type filament | |
| JP2007100022A (en) | Adjustment method of polymer dope |