JPS58151217A - Fiber and film obtained from cellulose dope - Google Patents

Fiber and film obtained from cellulose dope

Info

Publication number
JPS58151217A
JPS58151217A JP57034068A JP3406882A JPS58151217A JP S58151217 A JPS58151217 A JP S58151217A JP 57034068 A JP57034068 A JP 57034068A JP 3406882 A JP3406882 A JP 3406882A JP S58151217 A JPS58151217 A JP S58151217A
Authority
JP
Japan
Prior art keywords
cellulose
aqueous solution
zinc chloride
dope
water
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.)
Granted
Application number
JP57034068A
Other languages
Japanese (ja)
Other versions
JPH0324497B2 (en
Inventor
Shuji Kajita
修司 梶田
Kunihiko Okajima
邦彦 岡島
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Asahi Kasei Corp
Asahi Chemical Industry Co Ltd
Original Assignee
Asahi Chemical Industry Co Ltd
Asahi Kasei Kogyo KK
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Asahi Chemical Industry Co Ltd, Asahi Kasei Kogyo KK filed Critical Asahi Chemical Industry Co Ltd
Priority to JP57034068A priority Critical patent/JPS58151217A/en
Publication of JPS58151217A publication Critical patent/JPS58151217A/en
Publication of JPH0324497B2 publication Critical patent/JPH0324497B2/ja
Granted legal-status Critical Current

Links

Classifications

    • B29C47/92

Landscapes

  • Processes Of Treating Macromolecular Substances (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Artificial Filaments (AREA)

Abstract

PURPOSE:To provide fiber and film capable of being obtained in pollution-free and industrial economical condition, by keeping a temperature of the mixtures having a specified concentration of aqueous solution of zinc-chloride and cellulose within a fixed range of temperature and by spinning from dope composed of the dissolution of cellulose by adding a specified amount of water thereto. CONSTITUTION:The mixtures of aqueous solution containing 67wt% zinc-chloride and of cellulose are kept at a temperature of 80-105 deg.C, and the cellulose is dissolved by dropping thereto a quantity of water enough to keep a concentration of aqueous solution of zinc-chloride at not less than 50wt% and by mixing. The dope, with optical anisotropy composed 5-20wt% the obtained cellulose and the aqueous solution of 95-80wt% zinc-chloride is spinned by wet spinning or air-spilting out wet spinning. Thus, the aimed fiber and film may be obtained.

Description

【発明の詳細な説明】 本発明は、セルロースドープ1用iて成る繊維及びフィ
ルムに関する。更に詳しくはセルロースの新規な溶解方
法、得られるドープ及びそOドープを紡糸して製造され
る繊atたはフィルムKMするものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to fibers and films for cellulose dope 1. More specifically, the present invention describes a novel method for dissolving cellulose, the resulting dope, and a fiber or film KM produced by spinning the O-dope.

セルレースを溶解して得られるドープから、衣料、医用
あるいは産業資材嶋の分野に使用される繊維やフィルム
が製造されていることは周知のとおりである@41にビ
スコース法や銅アンモニアレー曹ン法は、その代表的な
ものである。しかしながら、これらの方法は、使用する
薬品が人体に対して、極めて有害であること、烏秦物が
公害の原因Kikるためその廃棄に鉱特別な処鳳を費す
る等の問題があり、その将来性が非常に憂慮されている
It is well known that fibers and films used in the fields of clothing, medicine, and industrial materials are manufactured from dope obtained by dissolving cellulose. The Ning method is a typical example. However, these methods have problems, such as the chemicals used are extremely harmful to the human body, and special treatment is required to dispose of the waste, which causes pollution. There are great concerns about the future.

一方、セルロースは天然に存在する豊富な資源であや、
原料供給の困難が将来予想される石油化学工業製品と異
なり、その有用性は将来増々高まることが予想される。
On the other hand, cellulose is a naturally occurring abundant resource.
Unlike petrochemical products, which are expected to have difficulty in supplying raw materials in the future, their usefulness is expected to increase in the future.

従って、ビスコース法や銅アンモニアレー冒ン法にかわ
る無公害で、しかも、工業的に彩算の合う新規なセルロ
ース繊維やフィルムの製造法の確立が現在版も希求され
ている。
Therefore, there is a current need for the establishment of a new method for producing cellulose fibers and films that is non-polluting and industrially suitable to replace the viscose method and the cuprammonium chloride method.

セルロースを利用して、繊維やフィルムを製造する丸め
に杜、セルロースを溶解して紡糸に適する溶液にする必
要がある。現在工業的に採用されている、ビスコース法
中銅アンモニア法の他に、古くからセルロースを溶解す
る方法として知られている方法の7つに、塩類の熱浩液
がある。しかしながら、これらの塩類の熱゛溶液は、セ
ルレースを加水分解すること、成形Kmし九良好な性質
が発現する高い#1度でセルロースを溶解することがで
きない等の理由によって、工業的に採用されていない。
When using cellulose to produce fibers and films, it is necessary to dissolve cellulose to create a solution suitable for spinning. In addition to the viscose method and the copper ammonia method currently used industrially, there are seven methods that have long been known as methods for dissolving cellulose, including hot extraction of salts. However, hot solutions of these salts have not been adopted industrially due to reasons such as hydrolysis of cellulose and inability to dissolve cellulose at a high temperature of #1 where good properties are exhibited. It has not been.

本発明者らは、これらの塩類は、毒性がなく、しかも安
価であるという、優れた点を生かし、上的W採用可能で
あるという観点に喪ち、#i意検討を重ねた結果本発明
を完成するに至った。
The inventors of the present invention realized that these salts could be used in the upper W by taking advantage of their superiority of being non-toxic and inexpensive, and as a result of repeated consideration, they developed the present invention. I was able to complete it.

すなわち、本発明の要旨紘次のとお〕である。In other words, this is the gist of the present invention.

■ z〜器型重量のセルロースと9140重量−の塩化
亜鉛水溶液よシ構成されるドーグであ〕。
■ It is a Dogue composed of cellulose weighing z ~ weight and an aqueous solution of zinc chloride weighing 9140 weight.

かつ塩化亜鉛水溶液に占める塩化亜鉛が少なくとも鱒重
量−である事を41111とするセルp−ストーブ ■ 少なくとも釘重量−の塩化亜鉛を含む水11派とセ
ルロースからなる混合物を関〜101”Cの温度に保持
し危状謝で、塩化亜鉛水溶液の1llI度を少なくとも
isS重量以上に保持するのに必ll!な量O*を滴下
することを4111とする1女ルー−ストーブの製造方
法 ■ S〜30〜量−のセルロースと−ト1重量−〇塩化
亜鉛水溶液よ〕構成されるドープであル。
and a cell p-stove in which the zinc chloride in the zinc chloride aqueous solution is at least the weight of the trout. 4111 A method for manufacturing a 1-woman roux stove that involves dropping an amount of O* that is necessary to maintain the zinc chloride aqueous solution at 111 degrees above the isS weight. The dope is composed of 30 to 1 weight of cellulose and 1 weight of zinc chloride aqueous solution.

かつ塩化亜鉛水溶液に占める塩化亜鉛が少なくともSO
型重量であるセルロースドープt11式紡糸または空中
吐出湿式紡糸して得られる繊細及びフィルム 本発明の目的とするところは、成形に適し、し1%経済
的に優れたセルロースドープとその製造法及びドープを
用いて成る繊維又はフィルムを提供するKある。
and the zinc chloride in the zinc chloride aqueous solution is at least SO
The purpose of the present invention is to provide a cellulose dope that is suitable for molding and is economically superior to 1%, and its production method and dope. K provides fibers or films made using the above.

従来セルロースの塩化亜鉛溶液はその溶解方法とともに
知られているが比較的重合度の高いセルロースをS重量
−以上含むセルロース溶液は知られていない。又、その
溶解方法についても60重量−以上の塩化亜鉛濃度む水
溶液を110℃以上に保持しながら溶解する為、セルロ
ースの解重合が起シ又溶液祉褐色管呈する。未溶解(ル
ロースが残存する等の為、成形用ドープとして不適格で
あり。
Although zinc chloride solutions of cellulose and their dissolution methods are known, cellulose solutions containing cellulose with a relatively high degree of polymerization in an amount of S weight or more are not known. Also, regarding the dissolution method, since an aqueous solution containing a zinc chloride concentration of 60% by weight or more is dissolved while being maintained at 110°C or higher, cellulose depolymerization occurs and the solution becomes brownish. It is not suitable as a molding dope because it is undissolved (lulose remains, etc.).

通常溶解されているセルロースもj1〜5iit−と低
く成形flat、ての経済性も着しく低い。本発明者勢
は先に述べた考え方及び上記従来技術の欠点を検討し、
未溶解セルロースがなく、シかもセルロースを5重量−
以上含む無色透明で成形に適したドープの製造方法を見
い出し本発明ド至ったものである。
The amount of cellulose that is normally dissolved is as low as 1 to 5 iit-, and the economic efficiency of forming flats is also quite low. The inventors studied the above-mentioned idea and the drawbacks of the above-mentioned conventional technology, and
There is no undissolved cellulose and only 5 weight of cellulose can be added.
The present invention has been achieved by discovering a method for producing a colorless and transparent dope suitable for molding.

即・・ち1本発明は少なくとも罰重量−〇塩化亜鉛水溶
液とセルロースからなる混合物tu−toi℃の温度に
保持した状態で、塩化亜鉛水溶液の塩化亜鉛濃度を少な
くとも關重量参以上に保持するOk必l!な量の水を滴
下することkよって、七ル襲−スを溶解することを特徴
とする。
Therefore, the present invention is capable of maintaining the concentration of zinc chloride in an aqueous solution of zinc chloride at a temperature of at least 90% by weight while maintaining the mixture consisting of a zinc chloride aqueous solution and cellulose at a temperature of at least 100°C. Must! It is characterized by dissolving the base by dropping a sufficient amount of water.

セルー−スを溶解する塩として知られているもoicH
lzmct、 O他K 、 LiI、 LiCN3 、
 Cm (CN8)s 。
Also known as a salt that dissolves cellulose, oicH
lzmct, O et al., LiI, LiCN3,
Cm(CN8)s.

Hg (CN8 )s KCN8 IIiがある。これ
らの塩類の水溶波も本発明の方法によって、セルロース
ドープすることが可能であるが、経済性及び、よ〕へa
mでセルー−スを溶解できる点で最も好適にセルロース
を溶解し、紡糸に好適な溶液を供与で自るOはZmCA
@水溶液である。セルロース溶解の第1段階で使用され
るzn偽水溶toe度は少なくとも67重量哄であるこ
とが好ましい。この濃度よ勤低いZC4水溶液を用いる
と後の水添加によるセルロースとの溶解が不充分となり
、未溶解物が多く残)、得られる溶液は、成形に適する
曳糸性が欠如し、未嬢解物O口過が極めて困難で紡糸1
遍さない。さらに好適に使用される濃度範囲は1丁5〜
15重量−である。
There is Hg (CN8)s KCN8 IIi. Although it is possible to dope cellulose with the method of the present invention by using the method of the present invention, it is also possible to dope the aqueous solution of these salts.
ZmCA is the most suitable O for dissolving cellulose and providing a suitable solution for spinning.
@Aqueous solution. Preferably, the ZN pseudowater solubility used in the first stage of cellulose dissolution is at least 67 kg by weight. If a ZC4 aqueous solution with a lower concentration than this is used, dissolution with cellulose by subsequent addition of water will be insufficient, and a large amount of undissolved matter will remain), and the resulting solution will lack stringiness suitable for molding, and It is extremely difficult to pass through the material O, so spinning 1
Not common. Furthermore, the concentration range suitable for use is 1 to 5 ~
15 weight.

次に調製され九ZnCj、水溶液fセルp−スを投入す
る。セルロースとしては、綿、パルプ勢の天然セルロー
スが好んで用いられるが、再生セルロース等を用いても
よく、特に限定されるものではない。6丁重量−のZn
(IJI水溶液とセルロースの混合物に水を加えて最終
的に得られる紡糸用の溶液中ノセルロースの重量分率は
、5〜20−である。
Next, the prepared nine ZnCj, aqueous solution F cell p-su is introduced. As the cellulose, natural cellulose in the form of cotton or pulp is preferably used, but regenerated cellulose or the like may also be used, and is not particularly limited. 6 pieces weight - Zn
(The weight fraction of nocellulose in the solution for spinning, which is finally obtained by adding water to a mixture of IJI aqueous solution and cellulose, is 5 to 20.

これより低い貴変のfIMi[は、当然容易に調整され
得るが紡糸に必要な曳糸性や、凝同能が不足して紡糸用
のドープとして不適当である。また、高い濃度ては、未
溶解のセルロースが多く′&〕紡糸に不適当と倉る。Z
nC4水溶液を均一にセルロースに浸透させるために遠
心力を使用する場合や、多量OZi+C4水溶液に浸漬
して、好適な濃度まで圧搾する場合もある。セルロース
の溶液中に占める割合は、使用するセルロースの平均重
合gKよって決定され、一般的に高重合度のもの騙低濃
度で使用される。%に数平均重合度が6OO以上のセル
ロースを用いる場合には、セルロースが5重量−以上の
溶液で流動複屈折が出現する。この流動複屈折は、偏光
顕微鏡のクロスニコル下で、スライドグラスの上#Ic
@液を置き、その上にカバーグラスを置いて、このカバ
ーグラスを軽く押え、せん断応力を与えることkよって
、容易Ell察することができる。ζOROR側折が容
1c出現する大め5本発明の溶液から得られる繊維は、
砥伸工―なしで繊維が配向し、好適な物性をもっ繊維が
得られる。ζOような低濃度で流動複屈折が発現するこ
とも本発明の4I徽であ〕、これは、七ルa −スを溶
解し友時のセルロースの分解・劣化がほとんどehため
に、平均重合度の^いものでは、異方性も大とtn流動
複屈折も出稿し易くなるもOと予想される。
If fIMi is lower than this, it can be easily adjusted, but it is unsuitable as a dope for spinning because it lacks the spinnability and coagulation ability necessary for spinning. In addition, at high concentrations, there is a large amount of undissolved cellulose and it is considered unsuitable for spinning. Z
In some cases, centrifugal force is used to uniformly permeate cellulose with nC4 aqueous solution, and in other cases, cellulose is immersed in a large amount of OZi+C4 aqueous solution and squeezed to a suitable concentration. The proportion of cellulose in the solution is determined by the average polymerization gK of the cellulose used, and generally those with a high degree of polymerization are used at a low concentration. When using cellulose having a number average degree of polymerization of 60% or more, flow birefringence appears in a solution containing cellulose of 5% by weight or more. This flow birefringence is measured under crossed nicols of a polarizing microscope, #Ic on the slide glass.
It can be easily detected by placing a solution, placing a cover glass on top of it, and pressing the cover glass lightly to apply shear stress. The fibers obtained from the solution of the present invention are larger in which ζOROR side folds appear in volume 1c.
The fibers are oriented without grinding, and fibers with suitable physical properties can be obtained. It is also a feature of the present invention that flow birefringence occurs at a low concentration such as ζO], and this is because the average polymerization It is expected that in the case of a material with a high degree of power, the anisotropy is also large, and the tn flow birefringence is likely to occur.

セルロース溶解に関する本発明O最大の轡黴紘セ、4−
−−スと・τ重量−以上OZnC4水溶液とO誂合物を
$O〜1・5℃の温度軸sK保持し、しかるのち、水を
滴下することKある。保持温ta好適には−・〜lO・
’C4りIl[範囲が使用される。これよ)低いiif
ては、セルロースの溶解が困難となシ。
The present invention relates to cellulose dissolution.
The OZnC4 aqueous solution and O compound are maintained at a temperature of $0 to 1.5 DEG C., and then water is added dropwise. The holding temperature ta is preferably -・~1O・
'C4Il[range is used. this) low iif
However, it is difficult to dissolve cellulose.

高い場合は、セルロースの分解−劣化が生じる。If it is high, cellulose decomposition-deterioration occurs.

1また。この1℃度での保持時間は通常数分〜細分の関
である 保持時間を長くするとセルロースの分解・劣化
が促進される恐れがある。この温[IC保持している間
、−にルロースの形態は、最初に投入した形111を保
持したままである。保持時間を長くすると部分溶解が生
じる場合もある。
1 again. The holding time at this temperature of 1° C. usually ranges from several minutes to a fraction of the time. If the holding time is extended, there is a risk that the decomposition and deterioration of cellulose will be accelerated. While this temperature is maintained, the form of luulose remains in the initially introduced form 111. Partial dissolution may occur if the holding time is increased.

次r、1a−14ei℃の駆跋範囲に保持されたセルロ
ースを含むZnC4水溶液f水を滴下し、攪拌すること
Kよって、セルロースは急激に溶解する。
Next, a ZnC4 aqueous solution containing cellulose kept in a range of 1a-14eiC is dripped with water and stirred, thereby rapidly dissolving the cellulose.

滴下する水の一度は%に限定されるものではない。The rate of dropping water is not limited to %.

滴下する水の量は、セルロースを除いたZnCj、水溶
液の一度が水を滴下稜、加熱による水分の蒸発がないと
仮定して、少なくとも50重量−になるようKすべきで
ある。水の量が多い場合にはセルロースを完全に溶解す
ることができない、好適な水の滴下量は、水音滴下後の
セルロースを除いたZmCj、水滴液の濃度が、關〜7
5重量−となるように設定される。この水を滴下すると
とKよって。
The amount of water to be dropped should be at least 50% by weight, assuming that once the ZnCj solution excluding cellulose and the aqueous solution are dropped, there is no evaporation of water due to heating. If the amount of water is large, cellulose cannot be completely dissolved.The preferred amount of water to be dropped is ZmCj excluding cellulose after dropping water, and the concentration of the water droplet is approximately 7 to 7.
5 weight -. If you drop this water, it will be K.

セル關−スは、急速に溶解し、均一で高l1llEの紡
糸罠適する溶液が得られる。
The cellulose dissolves rapidly, yielding a homogeneous, high IllE suitable solution for spin traps.

以下、実施例によって本発明をさらド詳しく説明する。Hereinafter, the present invention will be explained in more detail with reference to Examples.

実施例1 本実施例は、市販のセルロースから均一な溶液が得られ
ることを示す。
Example 1 This example shows that a homogeneous solution can be obtained from commercially available cellulose.

塩化亜111111f水3PK溶解し、塩化亜鉛水溶I
[t−1Il製した。これに市販のレオニアパルプ11
(Dr−1100)を加え、ヒータで加熱して、 SS
℃に昇温した。3分経過徒、攪拌しながら、i!温の水
4tを滴下した。セルロースは急速ド溶解し、均−tS
tとなった。仁の溶液を偏光顕微鏡Oクロスニコル下白
色光で1!察すると視野は暗黒で未溶解物社会くなかっ
た。続いて、カバーグラスを指で押して、せん断力を溶
液に与えると、視野は明るく輝き、流動複屈折が観察さ
れ良。
Zinc chloride 111111f water 3PK dissolved, zinc chloride water soluble I
[Made by t-1Il. Commercially available leonia pulp 11
(Dr-1100) and heat it with a heater, SS
The temperature was raised to ℃. After 3 minutes, while stirring, i! 4 tons of warm water was added dropwise. Cellulose dissolves rapidly and evenly
It became t. 1! Solution of nits under white light under a polarizing microscope O crossed Nicols! When I looked at it, my field of vision was dark and there was no undissolved material. Next, when the cover glass is pressed with a finger to apply shear force to the solution, the field of view becomes bright and fluid birefringence can be observed.

実施例意 本実施例は遠心力を利用すること虻よって101度で均
一なsiiが得られることを示す。
EXAMPLE This example shows that uniform sii can be obtained at 101 degrees by using centrifugal force.

塩化亜鉛11fを水NfK溶解し、市販のレオニアパル
プ(D?−1200) lj! fを加え1次に塩化亜
鉛水溶液をセルロースに均−処浸透させるために遠心分
離機に投入し、遠心効果100Gで1o分間、遠心力を
付与した。遠心分離機がら取〕出しfc ZnCL。
Zinc chloride 11f was dissolved in water NfK and commercially available Leonia pulp (D?-1200) lj! f was added, and first, the zinc chloride aqueous solution was placed in a centrifuge to uniformly permeate the cellulose, and centrifugal force was applied at a centrifugal effect of 100 G for 10 minutes. Remove fc ZnCL from centrifuge.

水溶液とセルロースの混合物を、90”C,に加熱し。The mixture of aqueous solution and cellulose was heated to 90"C.

5分間このtil度に保持し1L攪拌しながら、25℃
の水4ff滴下した。透明で、褐色に着色していない均
一な溶液が得られた。この溶液も、偏光III做鏡のク
ロスニコル下で流動複屈折を示した。
Hold at this temperature for 5 minutes and add 1L to 25°C while stirring.
4ff of water was added dropwise. A clear, non-brown, homogeneous solution was obtained. This solution also exhibited flow birefringence under crossed Nicols of a polarization III mirror.

実施例3 本実施例は、圧搾によって、 Znct、水溶液をセル
ロースに均一に浸透させ、均一な溶液が得られることを
示す。
Example 3 This example shows that an aqueous solution of Znct can be uniformly infiltrated into cellulose by squeezing, and a uniform solution can be obtained.

ZnCL禽10@ fを水totv溶解してZn cz
、水溶液t−調製し良。これに市販のレオニアパルプ!
fを開繊して浸漬し友、1時間放置彼、セルロースを引
き上げ、余分なznct1水溶液を口過で除去した後、
口紙の関にセルロースをはさみ、卓上製のプレス機を用
い、50−/ai、5分間圧搾を行なった。
Zn cz by dissolving ZnCL chicken 10@f in water totv
, aqueous solution t-prepared well. Commercially available leonia pulp for this!
After opening the fibers and soaking them, the cellulose was left for 1 hour, the cellulose was pulled up, and the excess ZNCT1 aqueous solution was removed by rinsing.
Cellulose was sandwiched between the opening paper and pressed using a tabletop press at 50 cm/ai for 5 minutes.

セルー−スを取シ出して計量し丸とζろセルロース/Z
nC4・1ト溶@0重量比は約Aであった。これを、1
0OC[加熱し、3分間この温fK保持した彼、攪拌し
ながら8fの水を滴下し、セルロースを溶解し、均一な
溶液を得た。
Take out the cellulose, weigh it, and round and zeta-filter cellulose/Z.
The weight ratio of nC4.1 to 0 was approximately A. This is 1
The mixture was heated to 0°C and kept at this temperature for 3 minutes, and 8f of water was added dropwise with stirring to dissolve the cellulose and obtain a homogeneous solution.

実施側番 本実施例は、市販の微結晶セルロース(DP諺鵞2・)
から、高濃度の均一な溶液が得られることを示す。
The implementation side number example is commercially available microcrystalline cellulose (DP 麺鵞2・)
This shows that a highly concentrated and homogeneous solution can be obtained.

ZnCts1@ fを水2tK溶解しfeoこの水f1
4111に4tの粉末状の微結晶セルロースを投入し良
0次にこれを91 ′cK加熱し、3分間放置俵、攪拌
しながら、室温の水4fを滴下してセルロースを溶解し
fico得られた溶液は透明で均一であった。
Dissolve ZnCts1@f in 2tK of water, feo this water f1
4 tons of powdered microcrystalline cellulose was put into 4111, heated to 91'cK, left for 3 minutes, and while stirring, 4 grams of room temperature water was added dropwise to dissolve the cellulose and fico was obtained. The solution was clear and homogeneous.

実施例2 本実施例は、市販のセルレースから調製され九溶液から
、繊維を製造する方法を示す。
Example 2 This example demonstrates the production of fibers from a nine solution prepared from commercially available cellulose.

ZnC4tto fを水5otK浴解し、塩化亜鉛水溶
液をIII製した。これに**のレオニアパルプ(Dp
mit・・) 101を開繊して投入した。次に加熱し
て温度を93℃に保持した。5分間この状態を保持した
後、攪拌しながら、25℃の水SOtを徐々に滴下し、
セルロースを溶解した。!WJAで均一なセルレースの
溶液が得られた。このときの重量測定から、溶解過程で
ge tの水が蒸発していることが判明し、全型tK対
するセルロースの重量分率は1845 % Kなってい
た。この溶液を偏光顕微鏡のり、ロスニコル下で皺、察
すると、せん断力をかけると視野が明るく輝き、流動複
屈折が確認された。せん断力のない場合は、視野は暗黒
で未浩解物はほとんどなかった。
ZnC4ttof was dissolved in 5 otK of water to prepare an aqueous zinc chloride solution. Add this to ** Leonia pulp (Dp
mit...) 101 was opened and introduced. It was then heated and the temperature was maintained at 93°C. After holding this state for 5 minutes, 25°C water SOt was gradually added dropwise while stirring.
Cellulose was dissolved. ! A uniform cellulose solution was obtained with WJA. From the weight measurement at this time, it was found that the water in get t had evaporated during the dissolution process, and the weight fraction of cellulose with respect to the total type tK was 1845% K. When this solution was observed under a polarizing microscope under Ross Nicol, the field of view glowed brightly when shear force was applied, confirming flow birefringence. When there was no shear force, the field of view was dark and there were almost no undissolved materials.

次にこの溶液をスクリュ一式の小型試験紡糸機に投入し
、紡糸を行なった。紡糸条件は、巻取速f 10 vn
/m、ドラフト4・、s5+のエアギャップで空中吐出
湿式紡糸を行なった。凝固浴は、−水凝固をアルコール
、二次凝向を水とし、いずれも室温であった。紡筒、紡
口のi!度も室温であった。得られ良繊維は、延伸工程
なしで配向を有しており、豪屈折率Δm=0.003!
! であった。また引張強度はり、S f/4 、伸度
は18Isテロ)7’C0集施例・ K CN8を龍重量%含む水溶tl@fK重合度3・・
に調製した木材パルプ(α化度91−以上)iFを混合
し、8!!t?:[て80分攪拌した0これに水3.1
 fを加えて攪拌したとζろセルロースは急速に溶解し
友。他方K CN8の7雪重量−水溶@に13.鵞fK
1tのセルレースを混合し、13・CKI・分間保持し
たが高度Kll#L、一部は褐色となシ低分子化して溶
解したが均一なドープを得ることは出きなかった。
Next, this solution was put into a small test spinning machine equipped with a screw, and spinning was performed. The spinning conditions are winding speed f 10 vn
Aerial discharge wet spinning was performed with an air gap of /m, draft 4., s5+. The coagulation bath used alcohol for -water coagulation and water for secondary coagulation, both at room temperature. Spinneret, spinneret i! The temperature was also room temperature. The resulting good fibers have orientation without a drawing process and have an Australian refractive index Δm=0.003!
! Met. In addition, the tensile strength, S f / 4, and elongation are 18 Is TEL) 7'C0 collection Example K A water-soluble tl@fK containing CN8 in a weight % degree of polymerization of 3...
Mix wood pulp (gelatinization degree 91- or more) iF prepared in 8! ! T? :[Stir for 80 minutes, then add 3.1 liters of water to this.
When f was added and stirred, the zeta cellulose rapidly dissolved. On the other hand, 7 snow weight of K CN8 - 13. Goose fK
1 t of cellulose was mixed and held for 13 CKI minutes, but the mixture had a high Kll#L color, some of which turned brown and became low molecular weight and dissolved, but it was not possible to obtain a uniform dope.

比較例1 本比較例は、塩の熱溶液がセルロースの分解を伴うこと
なく高濃度でセルロースを好適に溶かすことがでtil
にいことを示す。
Comparative Example 1 This comparative example shows that a hot solution of salt can suitably dissolve cellulose at a high concentration without decomposing the cellulose.
Show that you are right.

塩化亜鉛liFを水3tK溶解したこの溶液を1・0℃
に加熱し、市販のレオニアパルプ1tを投入したが溶解
は起らなかった。さらに温度を上昇させ1mI CFC
すると、セルロースは分解を伴って溶解し、褐色の溶液
となった。しかし、#!掖は粘度が極めて低く、着しい
セルロースの分解・劣化が発生し、紡糸用の原料として
使用できないものであった。このsmFi偏光顕黴鏡の
クロスニコル下で、せん断力を付与しても流動am折を
示さなかった。
This solution of zinc chloride liF dissolved in 3 tK of water was heated to 1.0°C.
1 ton of commercially available Leonia pulp was added, but no dissolution occurred. Further increase the temperature and add 1 mI CFC.
Then, the cellulose was dissolved with decomposition, resulting in a brown solution. but,#! The viscosity of this material was extremely low, and the cellulose that adhered to it was subject to decomposition and deterioration, so it could not be used as a raw material for spinning. Even when shearing force was applied under the crossed nicols of this smFi polarizing microscope, no flow am-folding was observed.

比較例2 本比較例は、最初に14製されるZnCL4水溶液のa
mが低い場合、溶液が作製できないことを示す。
Comparative Example 2 In this comparative example, the a of ZnCL4 aqueous solution prepared in
If m is low, it indicates that the solution cannot be prepared.

7mC121tを水atrc浩ML、、ZnC4水溶液
を一製した。これに1市販のレオニアパルプ1tを投入
し、温度をes′crc保持した。11分後、攪拌しな
がら水4fを滴下したが、セルロースは#−1とんど溶
解しなかつ九〇 以上の如く、本発明によれば、毒性のない、無公害な塩
水溶液から、紡糸に好適なセル四−スの溶液が得られ、
各種用途に有用な繊維やフィルムが製造可能であり、将
来の綾維産業の発展に非常に肩用である。
A ZnC4 aqueous solution was prepared using 7mC121t and water atrc Hiroshi ML. One ton of commercially available Leonia pulp was added to this, and the temperature was maintained at es'crc. After 11 minutes, 4 f of water was added dropwise with stirring, but the cellulose #1 was hardly dissolved. A suitable cell solution is obtained,
It is possible to produce fibers and films useful for various purposes, and is extremely useful for the future development of the twill textile industry.

特許出願人 旭化成工業株式余社Patent applicant: Asahi Kasei Kogyo Co., Ltd.

Claims (1)

【特許請求の範囲】 L 5〜別重量−のセルロースと95〜80重量−の塩
化亜鉛水溶液よ〕構成されるドーグであシ。 かつ塩化亜鉛水溶液に占める塩化亜鉛が少なくともgo
型重量である事を特徴とするセルロースドープ i ドープが光学異方性を示すことを特徴とする特許請
求の範囲第1113記載のセルロースドープ寡 少なく
とも67重量−の塩化亜鉛を含む水溶液とセルロースか
らなる混合物1i−80−105℃の一@r保持した状
態で、塩化亜鉛水溶液のlII&を少なくとも錦重量−
以上に保持するのに必要な量の水を嫡下することを特徴
とするセルロースドーグの製造方法 表 5〜20重量−のセルロースと95〜go 11−
の塩化亜鉛水浴液よ〕構成されるドープであシ、かつ塩
化亜鉛水溶[2占める塩化亜鉛が少なくとも50重量−
であるセルロースドーグを湿式紡糸tた社空中吐出濯式
紡糸して得られる繊維及びフィルム
[Scope of Claims] Dawg resin composed of 5 to 80 parts by weight of cellulose and 95 to 80 parts by weight of zinc chloride aqueous solution. and the zinc chloride in the zinc chloride aqueous solution is at least go
cellulose dope i characterized in that the dope exhibits optical anisotropy; cellulose dope i as claimed in claim 1113, characterized in that the dope exhibits optical anisotropy; While maintaining the mixture 1i-80-105°C at 1@r, the zinc chloride aqueous solution lII & at least brocade weight -
A method for producing cellulose doug, characterized by adding water in an amount necessary to retain the amount of water.
A dope consisting of a zinc chloride aqueous bath solution] and a zinc chloride aqueous solution [zinc chloride accounts for at least 50% by weight]
Fibers and films obtained by wet-spinning cellulose dog, which is
JP57034068A 1982-03-05 1982-03-05 Fiber and film obtained from cellulose dope Granted JPS58151217A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57034068A JPS58151217A (en) 1982-03-05 1982-03-05 Fiber and film obtained from cellulose dope

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57034068A JPS58151217A (en) 1982-03-05 1982-03-05 Fiber and film obtained from cellulose dope

Publications (2)

Publication Number Publication Date
JPS58151217A true JPS58151217A (en) 1983-09-08
JPH0324497B2 JPH0324497B2 (en) 1991-04-03

Family

ID=12403933

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57034068A Granted JPS58151217A (en) 1982-03-05 1982-03-05 Fiber and film obtained from cellulose dope

Country Status (1)

Country Link
JP (1) JPS58151217A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0513038A1 (en) * 1988-10-21 1992-11-19 Purdue Research Foundation Production of high strength cellulose fiber using zinc chloride, organic solvents and aqueous solution
JP2012519784A (en) * 2009-03-09 2012-08-30 キラム アーベー Molded cellulose production process combined with pulp machine recovery system
WO2013085053A1 (en) * 2011-12-09 2013-06-13 株式会社ダイセル Method for producing aqueous cellulose solution and method for producing cellulose derivative

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0513038A1 (en) * 1988-10-21 1992-11-19 Purdue Research Foundation Production of high strength cellulose fiber using zinc chloride, organic solvents and aqueous solution
JP2012519784A (en) * 2009-03-09 2012-08-30 キラム アーベー Molded cellulose production process combined with pulp machine recovery system
WO2013085053A1 (en) * 2011-12-09 2013-06-13 株式会社ダイセル Method for producing aqueous cellulose solution and method for producing cellulose derivative
JP2013139557A (en) * 2011-12-09 2013-07-18 Okayama Univ Method for producing aqueous cellulose solution and method for producing cellulose derivative
CN103842384A (en) * 2011-12-09 2014-06-04 株式会社大赛璐 Method for producing aqueous cellulose solution and method for producing cellulose derivative

Also Published As

Publication number Publication date
JPH0324497B2 (en) 1991-04-03

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