NZ263770A - Production of cellulose fibres having a reduced tendency to fibrillation - Google Patents

Production of cellulose fibres having a reduced tendency to fibrillation

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Publication number
NZ263770A
NZ263770A NZ263770A NZ26377094A NZ263770A NZ 263770 A NZ263770 A NZ 263770A NZ 263770 A NZ263770 A NZ 263770A NZ 26377094 A NZ26377094 A NZ 26377094A NZ 263770 A NZ263770 A NZ 263770A
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NZ
New Zealand
Prior art keywords
fibres
process according
fibrillation
textile
agent
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Application number
NZ263770A
Inventor
Heinrich Firgo
Markus Eibl
Johann Schickermueller
Original Assignee
Chemiefaser Lenzing Ag
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Application filed by Chemiefaser Lenzing Ag filed Critical Chemiefaser Lenzing Ag
Publication of NZ263770A publication Critical patent/NZ263770A/en

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Classifications

    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F11/00Chemical after-treatment of artificial filaments or the like during manufacture
    • D01F11/02Chemical after-treatment of artificial filaments or the like during manufacture of cellulose, cellulose derivatives, or proteins
    • 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
    • D01F2/00Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
  • Artificial Filaments (AREA)
  • Chemical Treatment Of Fibers During Manufacturing Processes (AREA)
  • Polysaccharides And Polysaccharide Derivatives (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Description

<div class="application article clearfix" id="description"> <p class="printTableText" lang="en">New Zealand Paient Spedficaiion for Paient Number £63770 <br><br> New Zealand No. 263770 International No. PCT/AT94/00049 <br><br> TO BE ENTERED AFTER ACCEPTANCE AND PUBLICATION <br><br> Priority dates: a &lt;■ if- -°l3, <br><br> International fifing date: ao^-9/- <br><br> Classification: Do\F2joo) xsoipnjoa <br><br> Publication date: 2 6 MAY 1997 <br><br> Journal No.: f{uL <br><br> NEW ZEALAND PATENTS ACT 1953 <br><br> COMPLETE SPECIFICATION <br><br> Title of invention: <br><br> Method of producing cellulose fibres with a decreased tendency to fibrillation <br><br> Name, address and nationality of ' <br><br> applicant(s) as in international application form: <br><br> Lenzing Aktiengesellschaft Werkstrasse 1, A-4860 Lenzing, Austria a* • <br><br> (FOLLOWED BY PAGE 1A) <br><br> 2C <br><br> 9 94/24343 <br><br> -iA- <br><br> PCT/AT94/00049 <br><br> PROCESS FOR THE PRODUCTION OF CELLULOSE FIBRES HAVING A REDUCED <br><br> TENDENCY TO FIBRILLATION <br><br> The invention is concerned with a process for the production of cellulose fibres having a reduced tendency to fibrillation. <br><br> As an alternative to the viscose process, in recent years there has been described a number of processes in which cellulose, without forming a derivative, is dissolved in an organic solvent, a combination of an organic solvent and an inorganic salt, or in aqueous saline solutions. Cellulose fibres made from such solutions have received by BISFA (The International Bureau for the Standardisation of man made Fibres) the generic name Lyocell. As Lyocell, BISFA defines a cellulose fibre obtained by a spinning process from an organic solvent. By "organic solvent", BISFA understands a mixture of an organic chemical and water. "Solvent-spinning" ist considered to mean dissolving and spinning without the forming of a derivative. <br><br> So far, however, only one process for the production of a cellulose fibre of the Lyocell type has achieved industrial-scale realization. In this process, a tertiary amine-oxide, particularly N-methylmorpholine-N-oxide (NMMO), is used as a solvent. Such a process is described for instance in US-A -4,246,221 and provides fibres which present a high tensile strength, a high wet-modulus and a high loop strength. <br><br> However, the usefulness of plane fibre assemblies, for example fabrics, made from the above fibres, is significantly restricted by the pronounced tendency of such fibres to fibrillate when wet. Fibrillation means the breaking up of the wet fibre in longitudinal direction at mechanical stress in a wet condition, so that the fibre gets hairy, furry. A fabric made from these fibres and dyed significantly looses colour intensity as it is washed several times. Additionally, light stripes are formed at the abrasion and crease edges. The reason may be that the fibres consist of fibrils which are arranged in the longitudinal direction of the fibre axis and that the crosslinking between these is reduced. <br><br> • 94/24343 -2- PCT/AT94/00049 <br><br> WO 92/14871 describes a process for the production of a fibre having a reduced tendency to fibrillation. The reduced tendency to fibrillation is attained by providing all the baths with which the freshly spun fibre is contacted before the first drying with a maximum pH of 8,5. <br><br> WO 92/07124 also describes a process for the production of a fibre having a reduced tendency to fibrillation, according to which the freshly spun, i.e. not yet dried, fibre is treated with a cationic polymer. As such a polymer, a polymer with imidazole and azetidine groups is mentioned. Additionally, <br><br> there may be carried out a treatment with an emulsifiable polymer, such as polyethylene or polyvinylacetate, or a crosslinking with glyoxal. <br><br> In a lecture given by S. Mortimer at the CELLUCON conference in 1993 in Lund, Sweden, it was mentioned that the tendency to fibrillation rises as drawing is increased. <br><br> It is the objective of the invention to provide a process which can be carried out in an easy way, allowing the production of cellulose fibres of the Lyocell type having a reduced tendency to fibrillation. <br><br> The process according to the invention for the production of cellulose fibres having a reduced tendency to fibrillation consists in that the freshly spun, not yet dried fibres are contacted with a textile agent, which carries at least two reactive groups, and are washed with an aqueous buffer, <br><br> provided glyoxal is not used as textile agent. <br><br> As textile agents, especially dyes having two reactive groups have shown good results. According to the invention, however, <br><br> textile agents which are colourless, i.e. do not absorb visible light, may also be used. <br><br> According to the invention, the use of textile agents which carry one or two vinylsulfone groups as reactive groups is preferred. <br><br> ®70 94/24343 -3- PCT/AT94/00049 <br><br> A convenient embodiment of the process according to the invention is characterized in that the freshly spun fibres are contacted with the textile agent in an aqueous alkaline medium. <br><br> It was shown that the tendency to fibrillation is especially reduced when an alkali carbonate and an alkali hydroxide is chosen as the alkaline medium. <br><br> Another preferred embodiment of the process according to the invention consists in that the fibres contacted with the textile agent are heat-treated. The heat treatment drastically reduces the impregnation time. <br><br> EP-A - 0 538 977, published on April 28, 1993, describes heat treatment of cellulose fibres impregnated with a dye. It was shown, however, that heating of the fibres impregnated with the textile agent by means of hot air may reduce the impregnation time, but that this carries the risk of the fibres not being heated uniformly. Thus for example, the fibres on the outside of a fibre bundle to be dried may already be partly dried, <br><br> while the fibres inside the bundle have not yet reached the required temperature. This has a negative effect on the quality of the fibres produced. <br><br> It has been found that this drawback occurring in a simple heat treatment can be overcome by irradiating the fibres with electromagnetic waves, particularly microwaves. When irradiated with microwaves, on the one hand the fibres are heated uniformly and on the other hand premature drying of the fibres can be avoided, since irradiation with electromagnetic waves provides the possibility to weld the fibre bundle for example into a plastic wrapping and expose it in a welded condition to the electromagnetic field. <br><br> The above advantages are also given when the fibres, for example lying as plane fibre assembly on a conveyor, are moved through a narrow channel, in which they are exposed to electromagnetic, waves. This channel can be designed in a way that only little air space above the fibres is left, thereby <br><br> 0k&gt; 94/24343 -4- PCT/AT94/00049 <br><br> preventing a partial drying of the outer fibres of the bundle. Simultaneously, this way of fixation of the textile agent also offers the possibility of a large-scale production easy to put into practice. <br><br> Thus, the invention further refers to a process for the production of cellulose fibres having a reduced tendency to fibrillation, in which a solution of cellulose in a tertiary amine-oxide is spun into fibres, and the freshly spun fibres are contacted with a textile agent which carries at least two reactive groups and are heat-treated, characterized in that the heat treatment is carried out by irradiation with electromagnetic waves. <br><br> Also according to this embodiment of the process according to the invention, the use of a textile agent which carries vinylsulfone groups as the reactive groups, is preferred, preferably being a dye. However, textile agents which are colourless, i.e. do not absorb visible light, can also be used. <br><br> Another preferred embodiment of the process according to the invention consists in carrying out the heat treatment by means of microwaves. <br><br> The invention will be explained in more detail by the following examples. All references to % are to be understood as weight %. <br><br> Production of the cellulose fibres <br><br> According to the process described in EP-A - 0 356 419, a solution of cellulose in NMMO was prepared and extruded through a spinneret. The filaments thereby obtained were conducted through an air gap into an aqueous precipitation bath, in which the cellulose coagulated. The fibres obtained in the precipitation bath were washed, presenting a titer of 1,7 dtex. The washed fibres were used for the examples hereinafter described and represent those fibres which in the present description and in the present claims are referred to as fibres freshly spun, not yet dried. <br><br> 63770 <br><br> to 94/24343 -5- PCT/AT94/00049 <br><br> 1) Treatment with textile agents without subsequent heat treatment <br><br> A) General procedure <br><br> 1 g of each of the fibres produced according to the above process were impregnated in 190 ml of an aqueous solution (bath), which contained a textile agent comprising two reactive groups and Na2S04, at 40°C for 30 minutes. Then NaOH (3%), <br><br> Na2C03 (4%) or a mixture of NaOH, Na2C03 (4% Na2C03 and 0,2 g/1 NaOH) were added for the fixation of the textile agent. After another 60 minutes at 40°C the fibres were washed several times, in order to remove the textile agent not fixed to the fibre. Then the washed fibres were treated for 30 minutes with an aqueous buffer, then again washed with water (for 15 minutes) and dried at 60°C. Afterwards the fibres were examined to determine their tendency to fibrillation and to determine other fibre parameters. <br><br> Evaluation of fibrillation <br><br> The abrasion of the fibres among each other in washing processes and finishing processes in wet condition was simulated by the following test: 8 fibres with a length of 20 mm each were put into a 20 ml sample bottle with 4 ml of water and shaken during 9 hours in a laboratory mechanical shaker of the RO-IO type of the company Gerhardt, Bonn (Germany), at stage 12. Afterwards the fibrillation behaviour of the fibres was evaluated by microscope, by means of counting the number of fibrils per 0,276 mm fibre length. <br><br> 7 <br><br> 94/24343 <br><br> -6- <br><br> PCT/AT94/00049 <br><br> Further fibre parameters <br><br> The fibre tensile strength and fibre elongation at break were tested following the BISFA rule on "Internationally agreed methods for testing viscose, modal, cupro, lyocell, acetat and triacetat staple fibres and tows", edition 1993. <br><br> B) Examples <br><br> According to the above process, fibres were treated with the dye Remazol Black B and Remazol Red RB as textile agent (made by Hoechst AG). The dye Remazol Black B carries two vinylsulfone groups and the dye Remazol Red B carries one vinylsulfone group and one monochlorotriazine group. <br><br> The bath contained 3% Remazol Black B and 0,5% Remazol Red RB respectively. The pE of the bath was 4,6 in each example. The used aqueous buffer was an aqueous solution which contained 3% acetic acid and 7% sodium acetate. The pH value of this solution was 4,6. After the treatment with the buffer, the fibres were washed with water for 15 minutes and afterwards examined. Table la indicates the fixing agent used in each case, the fibrillation (number of fibrils), the titer (dtex), the fibre strength (cH/tex) and the fibre elongation at break (%) . Examples 1, 2 and 3 were carried out with the dye Remazol Black B and Example 4 with the dye Remazol Red RB. <br><br> Table lb shows the results of comparative tests carried out without dye. <br><br> fO 94/24343 <br><br> -7- <br><br> Table la (Textile Agent) <br><br> PCT/AT94/00049 <br><br> Ex. <br><br> Fixing agent <br><br> Fibrils <br><br> Titer <br><br> Tensile Strength <br><br> Elongation <br><br> 1 <br><br> NaOH <br><br> 22 <br><br> 1,82 <br><br> 28,81 <br><br> 11,14 <br><br> 2 <br><br> Na^CO^ <br><br> 2 <br><br> 2,07 <br><br> 26,39 <br><br> 10,67 <br><br> 3 <br><br> NaOH+Na?COq <br><br> 0 <br><br> 2,34 <br><br> 24,94 <br><br> 10,04 <br><br> 4 <br><br> NaOH+Na^CO^ <br><br> 5 <br><br> 2,34 <br><br> 30, 00 <br><br> 11,74 <br><br> Table lb (Comparative Examples) <br><br> Ex. <br><br> Fixing agent <br><br> Fibrils <br><br> Titer <br><br> Tensile Strength <br><br> Elongation <br><br> 5 <br><br> NaOH <br><br> &gt;60 <br><br> 1,80 <br><br> 33,76 <br><br> 12,71 <br><br> 6 <br><br> Na^COs <br><br> 60 <br><br> 1,56 <br><br> 33,78 <br><br> 12,15 <br><br> . 7 <br><br> NaOH+Na?CO^ • <br><br> &gt;60 <br><br> 1,72 <br><br> 30,18 <br><br> 12,14 <br><br> 8 <br><br> NaOH+Na^CO^ <br><br> &gt;60 <br><br> 1,72 <br><br> 32,00 <br><br> 12,70 <br><br> A comparison of the results of Tables la and lb shows that the textile agent, in the present case the dyes Remazol Black B and Remazol Red RB, drastically reduces the tendency to fibrillation and that the combination of Na0H+Na2C03, which is used for the fixation of the textile agent, also drastically further reduces the tendency to fibrillation. <br><br> It was shown that the above results are obtained also when using other textile agents which comprise two reactive groups. Thus, Remazol Black B and Remazol Red RB may represent other textile agents which also carry at least two reactive groups. <br><br> 2) Treatment with textile agents and subsequent heat treatment <br><br> 1 g of each of the fibres produced according to the above process was impregnated in 190 ml of a bath (containing 0,2% Remazol Black B, 2% Na2C03, 0,2% NaOH, pH = 11,5) three times for 30 seconds each, the fibres being squeezed off after each impregnation. Afterwards, each sample was heat-treated twice for 40 seconds in each case in a circulating-air oven at 180°C. Subsequently, each heat-treated sample was treated for 30 minutes with the above mentioned acetate buffer (pH = 4,6), <br><br> • 94/24343 -8- PCT/AT94/00049 <br><br> washed with water for 15 minutes, dried at 60#C and examined. The results are shown in Table 2, Example 10 representing a Control Sample (for Example 10, Example 9 was repeated without using a textile agent). <br><br> Table 2 <br><br> Ex. <br><br> Fibrils <br><br> Titer <br><br> Tensile Strength <br><br> Elongation <br><br> 9 <br><br> 24 <br><br> 1,56 <br><br> 33,78 <br><br> 12,15 <br><br> 10 <br><br> &gt;57 <br><br> o <br><br> 00 H <br><br> 33,76 <br><br> 12,71 <br><br> From table 2 it can be seen that a heat treatment of the fibres impregnated with the textile agent drastically reduces the impregnation time, as well as the tendency to fibrillation is reduced. <br><br> With the dye Remazol Red RB, similarly good results could be attained. <br><br> 3. Treatment with textile agents and subsequent irradiation with microwaves <br><br> 10 g of the fibres produced according to the above process were impregnated in a 900 ml bath (10% Remazol Black B, 10% Na2S04, 8% Na2C03? the pH was adjusted with NaOH to 11,5) for 9 minutes. Afterwards, the fibres were squeezed off and divided into 2 parts of equal amount (Examples 12, 13). Example 11 was a Control Sample, indicating the properties of the fibres not treated with a textile agent. For Examples 12 and 13, the fibres were squeezed off after impregnation with the bath, and they either were heated to 180°C for 180 seconds (Example 12) or irradiated with 90 watt microwaves for 50 seconds (Example 13). Afterwards, the fibres were treated for 30 minutes in the above acetate buffer at a pH of 4,6, washed with water for 15 minutes and dried at 60°C. The results of the tests are shown in Table 3. <br><br> pi "5? <br><br> n b 94/24343 -9- PCT/AT94/00049 <br><br> Table 3 <br><br> Ex. <br><br> Heating <br><br> Fibrils <br><br> Titer <br><br> Tensile Strength <br><br> Elongation <br><br> 11 <br><br> 56 <br><br> 1,83 <br><br> 31,98 <br><br> 11,52 <br><br> 12 <br><br> 180 sec.;180°C <br><br> 11 <br><br> 1,91 <br><br> 23,70 <br><br> 9,77 <br><br> 13 <br><br> 50 sec.; 90 W <br><br> 7 <br><br> 1,92 <br><br> 31,23 <br><br> 11,34 <br><br> From Table 3 it can be seen that the irradiation with microwaves further reduces the heating time, the tendency to fibrillation being still further reduced. Similarly good results in terms of a reduced tendency to fibrillation were obtained, when instead of Remazol Black B other textile agents with at least two reactive groups were used. Particularly it was shown that the positive effect upon the tendency to fibrillation is similarly pronounced as with glyoxal. Furthermore it was shown that the above positive effect brought about by irradiation with microwaves can also be observed with glyoxal and other dialdehydes, as can be deduced from the following example. <br><br> 2 g of fibres produced according to the process described in section 1 were impregnated twice for 3 minutes each with 140 ml of a bath, containing 2% glyoxal and 0,66% crosslinking catalyst (for example Condensol FB, a mixture of ZnCl2 and MgCl2, made by BASF). Afterwards, the fibres were squeezed off and divided into 2 parts (Examples 15, 16). Example 14 was a Control Sample, for Example 15 the fibres were treated for 10 minutes in a circulating-air oven at 100°C, and for Example 16 the fibres were subjected to a power of 500 watt by means of a microwave. The fibrillation results are indicated in the following Table 4. <br><br> The above methode was repeated, using glutardialdehyde (3,4%) instead of glyoxal. The fibrillation results of the obtained fibres are also reflected in Table 4 (Examples 17, 18 and 19 correspond to Examples 14, 15 and 16 respectively). <br><br></p> </div>

Claims (14)

  1. <div class="application article clearfix printTableText" id="claims"> <p lang="en"> 2637<br><br> ^0 94/24343 -10- PCT/AT94/00049<br><br> Table 4<br><br> Example<br><br> Textile agent<br><br> Treatment<br><br> Fibrils<br><br> 14<br><br> 35,5<br><br> 15<br><br> Glyoxal<br><br> 10 min.; 100°C<br><br> 24,0<br><br> 16<br><br> Glyoxal<br><br> 60 sec.; 500w<br><br> 8,5<br><br> 17<br><br> 35,5<br><br> 18<br><br> Glutardialdehyde<br><br> 10 min.; 100°C<br><br> 10,5<br><br> 19<br><br> Glutardialdehyde<br><br> 60 sec.; 500 w<br><br> 21,0<br><br> 263 7 70<br><br> WO 94/24343<br><br> -11-<br><br> PCT/AT94/00049<br><br> WHAT WE CLAIM IS:<br><br> 1.
  2. A process for the production of cellulose fibres having a reduced tendency to fibrillation, in which a solution of cellulose in a tertiary amine-oxide is spun into fibres and the freshly spun fibres are contacted with a textile agent,<br><br> which carries at least two reactive groups, and are washed with an aqueous buffer, provided that as a textile agent glyoxal is not used.<br><br> 2.
  3. A process according to Claim 1, characterized in that as a textile agent a dye or a colourless substance is used.<br><br> 3.
  4. A process according to Claim 1 or 2, characterized in that a textile agent is used which carries at least one vinylsulfone group as reactive group.<br><br> 4.
  5. A process according to any one of Claims 1 to 3,<br><br> characterized in that the freshly spun fibres are contacted with the textile agent in an aqueous alkaline medium.<br><br> 5.
  6. A process according to Claim 4, characterized in that water, an alkali carbonate and an alkali hydroxide is chosen as the aqueous alkaline medium.<br><br> 7.
  7. A process for the production of cellulose fibres having a reduced tendency to fibrillation, in which a solution of cellulose in a tertiary amine-oxide is spun into fibres and the freshly spun fibres are contacted with a textile agent, which carries at least two reactive groups, and heat-treated, characterized in that the heat treatment is carried out by irradiation with electromagnetic waves.<br><br> 6.
  8. A process according to any one of Claims 1 to 5, characterized in that the fibres contacted with textile agent are heat-treated.<br><br> 8.
  9. A process according to Claim 7, characterized in that as a textile agent a dye or a colourless substance is used.<br><br> 263770<br><br> WO 94/24343<br><br> -12-<br><br> PCT/AT94/00049<br><br> 9.
  10. A process according to Claim 7 or 8, characterized in that a te;cti '.e agent is used which carries at least one vinyls^ .fone group as reactive group.<br><br> 10.
  11. A process according to any one of Claims 7 to 9, characterized in that the freshly spun fibres are contacted with the textile agent in an aqueous alkaline medium.<br><br> (.1.
  12. A process according to Claim 10, characterized in that the aqueous alkaline medium comprises water, an alkali carbonate and an alkali hydroxide.<br><br> 12.
  13. A process according to any one of Claims 7 to 11,<br><br> characterized in that the heat treatment is carried out by means of microwaves.<br><br> 13- A process for the production of cellulose fibres having a reduced tendency to fibrillation according to any one of Claims 1 to 12, substantially as herein described.<br><br>
  14. 14. Cellulose fibres whenever produced by the process of any one of Claims 1 to 13.<br><br> I isea agents<br><br> It SON<br><br> END OF CLAIMS<br><br> </p> </div>
NZ263770A 1993-04-21 1994-04-20 Production of cellulose fibres having a reduced tendency to fibrillation NZ263770A (en)

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KR (1) KR0183419B1 (en)
CN (1) CN1041948C (en)
AU (1) AU684274B2 (en)
BG (1) BG63049B1 (en)
BR (1) BR9405150A (en)
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CZ (1) CZ303094A3 (en)
DE (1) DE4492198D2 (en)
FI (1) FI945695A (en)
GB (1) GB2284177B (en)
HR (1) HRP940261A2 (en)
HU (1) HU214882B (en)
LV (1) LV11194B (en)
MD (1) MD906C2 (en)
NZ (1) NZ263770A (en)
PL (1) PL176125B1 (en)
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RU (1) RU2127775C1 (en)
SK (1) SK152994A3 (en)
TR (1) TR27503A (en)
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UA (1) UA32560C2 (en)
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GB2307203B (en) * 1993-04-21 1997-09-10 Chemiefaser Lenzing Ag Process for the production of cellulose fibres having a reduced tendency to fibrillation
AT401271B (en) * 1993-07-08 1996-07-25 Chemiefaser Lenzing Ag METHOD FOR PRODUCING CELLULOSE FIBERS
ATA249893A (en) * 1993-12-10 1994-12-15 Chemiefaser Lenzing Ag METHOD FOR PRODUCING CELLULOSIC MOLDED BODIES AND MOLDED OR. SPIDING MASS
GB9407496D0 (en) * 1994-04-15 1994-06-08 Courtaulds Fibres Holdings Ltd Fibre treatment
GB9408742D0 (en) * 1994-05-03 1994-06-22 Courtaulds Fibres Holdings Ltd Fabric treatment
US5902532A (en) * 1994-12-02 1999-05-11 Akzo Nobel Nv Process for manufacturing cellulose objects
AT403296B (en) * 1995-08-11 1997-12-29 Chemiefaser Lenzing Ag METHOD FOR PRODUCING A CELLULOSE MOLDED BODY
RU2156839C2 (en) 1996-03-06 2000-09-27 Мицубиси Рэйон Ко., Лтд. Fibril system filaments (versions), formed article, fibril system filament manufacture method, spinning die for manufacture of fibril system filaments
AT409144B (en) * 1996-06-21 2002-05-27 Chemiefaser Lenzing Ag METHOD FOR TREATING CELLULOSE FIBERS AND FORMS OF THESE FIBERS
DE19919259A1 (en) * 1999-04-28 2001-01-11 Thueringisches Inst Textil Process for reducing the fibrillation tendency of cellulose fibers spun from solvents
AT507051B1 (en) * 2008-06-27 2015-05-15 Chemiefaser Lenzing Ag CELLULOSE FIBER AND METHOD FOR THE PRODUCTION THEREOF
WO2012137219A2 (en) 2011-04-05 2012-10-11 Grasim Industries Limited A process for making fibril-free lyocell fabrics
TWI667378B (en) * 2014-01-03 2019-08-01 奧地利商蘭精股份有限公司 Cellulosic fibre
CN104005225B (en) * 2014-06-05 2016-08-24 山东英利实业有限公司 A kind of method reducing lyocell fiber cellulose fiber fibrillation tendency

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US4246221A (en) * 1979-03-02 1981-01-20 Akzona Incorporated Process for shaped cellulose article prepared from a solution containing cellulose dissolved in a tertiary amine N-oxide solvent
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PL306801A1 (en) 1995-04-18
JP2753396B2 (en) 1998-05-20
AU6499294A (en) 1994-11-08
GB9424722D0 (en) 1995-03-01
RO112768B1 (en) 1997-12-30
KR950702264A (en) 1995-06-19
MD940168A (en) 1996-10-31
HU214882B (en) 1998-07-28
SK152994A3 (en) 1995-05-10
FI945695A0 (en) 1994-12-02
AU684274B2 (en) 1997-12-11
CA2137232A1 (en) 1994-10-27
TR27503A (en) 1995-06-07
RU94046330A (en) 1996-10-27
BR9405150A (en) 1999-06-15
MD906C2 (en) 1998-09-30
CN1041948C (en) 1999-02-03
GB2284177A (en) 1995-05-31
UA32560C2 (en) 2001-02-15
PL176125B1 (en) 1999-04-30
LV11194B (en) 1996-08-20
DE4492198D2 (en) 1995-06-01
TW257811B (en) 1995-09-21
KR0183419B1 (en) 1999-05-01
LV11194A (en) 1996-04-20
MD906B2 (en) 1998-01-31
HRP940261A2 (en) 1996-08-31
JPH07508320A (en) 1995-09-14
RU2127775C1 (en) 1999-03-20
ZA942727B (en) 1995-01-09
GB2284177B (en) 1997-09-17
HU9403717D0 (en) 1995-03-28
EP0647281A1 (en) 1995-04-12
BG99236A (en) 1996-01-31
HUT70085A (en) 1995-09-28
CN1108032A (en) 1995-09-06
CH685944A5 (en) 1995-11-15
CZ303094A3 (en) 1995-07-12
FI945695A (en) 1994-12-02
WO1994024343A1 (en) 1994-10-27

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