EP0823945A1 - Procede de production de fibres cellulosiques - Google Patents
Procede de production de fibres cellulosiquesInfo
- Publication number
- EP0823945A1 EP0823945A1 EP97903143A EP97903143A EP0823945A1 EP 0823945 A1 EP0823945 A1 EP 0823945A1 EP 97903143 A EP97903143 A EP 97903143A EP 97903143 A EP97903143 A EP 97903143A EP 0823945 A1 EP0823945 A1 EP 0823945A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- filaments
- extruded
- drawn
- spinneret
- take
- 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
Links
Classifications
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F2/00—Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof
Definitions
- the present invention relates to a method for producing cellulosic fibers.
- a solution of cellulose in a tertiary amine oxide is extruded through spinning holes of a spinneret, whereby filaments are extruded, the extruded filaments are passed through an air gap, a coagulation bath and over a take-off device, with which the filaments are drawn, and the drawn filaments processed cellulosic fibers.
- N-methylmorpholine-N-oxide is used as the solvent.
- NMMO N-methylmorpholine-N-oxide
- Such a method is described, for example, in US Pat. No. 4,246,221 and provides fibers which are distinguished by a high strength, a high wet modulus and by a high loop strength.
- the usability of fabrics, for example fabrics made from the fibers mentioned, is severely limited by the pronounced tendency of the fibers to fibrillate when wet. Fibrillation is understood to mean breaking open the fiber in the longitudinal direction under mechanical stress in the wet state, as a result of which the fiber is given a hairy, furry appearance.
- a fabric made and dyed from these fibers loses its color intensity over the course of a few washes. In addition, there are bright stripes on the scuffed and crease edges.
- the cause of the fibrillation is assumed to be that the fiber consists of fibrils arranged in the direction of the fibers, between which there is only a small amount of cross-connection.
- WO 92/14871 describes a method for producing a fiber with a reduced tendency to fibrillation. This is achieved in that all baths with which the fiber comes into contact before the first drying have a pH of maximum 8.5.
- WO 92/07124 also describes a method for producing a fiber with a reduced tendency to fibrillation, according to which the undried fiber is treated with a cationic polymer.
- a polymer with imidazole and azetidine groups is mentioned as such a polymer.
- treatment with an emulsifiable polymer e.g. Polyethylene or polyvinyl acetate, or crosslinking with glyoxal.
- DE-A-42 19 658 and EP-A-0 574 870 describe that post-stretching of the precipitated filaments adversely affects the textile properties of the fibers, in particular their elongation.
- WO 96/18760 discloses cellulosic filaments which have a strength of 50 to 80 cN / tex, an elongation at break of 6 to 25% and a specific breaking time of at least 300 s / tex. These filaments are subjected to a tension in the range of 5 to 93 cN during manufacture. It is disclosed that these fibers have a low tendency to fibrillation.
- the present invention has in particular the object of providing a process with which fibers with improved properties are produced, in which the So-called work capacity, which is the mathematical product of fiber strength (conditioned) and elongation (conditioned), is improved.
- This aim is achieved in a process for the production of cellulosic fibers by the combination of the measures that a solution of cellulose in a tertiary amine oxide is extruded through spinning holes of a spinneret, whereby filaments are extruded, the extruded filaments through an air gap
- the drawn filaments are further processed into cellulosic fibers, the drawn filaments being subjected to a tensile stress in the longitudinal direction of not more than 5.5 cN / tex during further processing.
- further processing encompasses all the steps which are carried out on the filaments, including the transport of the filaments after they have passed the first stopping point of the take-off device.
- the drawn filaments are expediently cut during further processing and then washed. It has also been found that the length of the path along which the filaments are fed from the spinneret to the take-off device has an influence on the fiber properties in that the shorter the distance, the better the fiber properties.
- a preferred embodiment of the method according to the invention is that the length of this route is a maximum of 12 m, in particular a maximum of 1 m.
- the invention further relates to a method for producing cellulosic fibers, which is characterized by the combination of the measures that a solution of cellulose in a tertiary amine oxide is extruded through spinning holes of a spinneret, whereby filaments are extruded, the extruded filaments through an air gap
- Fibers are further processed, the length of the path on which the filaments of the
- All known cellulosic spinning materials can be processed by the process according to the invention. So these spinning masses can contain between 5 and 25% cellulose. However, cellulose contents between 10 and 18% are preferred. Hard or soft wood can be used as the raw material for pulp production, the degree of polymerization of the pulp (s) being in the range of commercially available products can lie. However, it has been shown that the spinning behavior is better with a higher molecular weight of the pulp. Depending on the degree of polymerization of the pulp or the solution concentration, the spinning temperature can be between 75 and 140 * C and can be easily optimized for each pulp or concentration.
- the friction of the fibers against one another during washing processes or during finishing processes in the wet state was simulated by the following test: 8 fibers were placed in a 20 ml sample vial with 4 ml water and in a laboratory shaker type RO-10 from Gerhardt for 9 hours, Bonn (FRG) shaken at level 12. The fibrillation behavior of the fibers was then assessed under the microscope by counting the number of fibrils per 0.276 mm fiber length.
- the loop strength was tested by forming a loop with two fibers and subjecting this loop to a tensile test. Only those fibers that tear at the loop were used for averaging.
- a vibroscope which is a Lenzing AG titer measuring device for non-destructive titer determination using the vibration method, and a Vibrodyn, which is a device for tensile tests on individual fibers with a constant deformation rate, were used to measure the loop strength and elongation.
- Air of 20 * C and a relative humidity of 65% was taken as the standard climate.
- the filaments were passed through the air gap into the precipitation bath and over a godet, with which a tension was exerted on the filaments, thereby stretching them in the air gap. After passing through the godet, the filaments were cut immediately and only then processed further by washing out the amine oxide, finishing and drying. The filaments were thus processed without tension.
- the textile data of the fibers obtained are shown in Table 1.
- Example 2 The procedure was analogous to Example 1, except that the filaments were not cut immediately after passing the godet, that is to say the first stopping point, but were fed to a further godet which was 2.2 meters from the first godet. The speed of the second godet was adjusted so that the filament cable between the the first and the second godet were under a tension of 11.6 cN / tex.
- the filaments After passing through the second godet, the filaments were cut immediately and only then processed further by washing out the amine oxide, finishing and drying. The filaments were therefore not processed without tension after the first stopping point.
- the textile data of the fibers obtained are shown in Table 1.
- the column “Fibrils” shows the average number of fibrils over a fiber length of 276 ⁇ m.
- Working capacity is the mathematical product of strength (cond.) And elongation (cond.).
- a spinning mass of the composition of Example 1 was at 120 * C through a nozzle with 1 spinning hole, which a was 100 microns in diameter, extruded into filaments with a single fiber titer of 1.8 dtex.
- a stretching load affects the tendency to fibrillation by loading the filaments with different weights, the loading time also being varied. The results are shown in Table 2.
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT407/96 | 1996-03-04 | ||
AT40796 | 1996-03-04 | ||
AT0040796A AT404032B (de) | 1996-03-04 | 1996-03-04 | Verfahren zur herstellung cellulosischer fasern |
PCT/AT1997/000041 WO1997033020A1 (fr) | 1996-03-04 | 1997-03-03 | Procede de production de fibres cellulosiques |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0823945A1 true EP0823945A1 (fr) | 1998-02-18 |
EP0823945B1 EP0823945B1 (fr) | 2001-10-31 |
Family
ID=3489811
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP97903143A Revoked EP0823945B1 (fr) | 1996-03-04 | 1997-03-03 | Procede de production de fibres cellulosiques |
Country Status (13)
Country | Link |
---|---|
US (1) | US5863478A (fr) |
EP (1) | EP0823945B1 (fr) |
JP (1) | JPH11504995A (fr) |
CN (1) | CN1072284C (fr) |
AT (2) | AT404032B (fr) |
AU (1) | AU711895B2 (fr) |
BR (1) | BR9702110A (fr) |
CA (1) | CA2219110A1 (fr) |
DE (1) | DE59705152D1 (fr) |
ID (1) | ID16121A (fr) |
NO (1) | NO310779B1 (fr) |
TW (1) | TW336259B (fr) |
WO (1) | WO1997033020A1 (fr) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP3812489A1 (fr) | 2019-10-23 | 2021-04-28 | Lenzing Aktiengesellschaft | Surface du rouleau utilisée dans la production de lyocell filaments |
CN113242917A (zh) * | 2018-12-28 | 2021-08-10 | 连津格股份公司 | 从纤维素长丝纱线或纤维中去除液体的方法 |
Families Citing this family (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6235392B1 (en) * | 1996-08-23 | 2001-05-22 | Weyerhaeuser Company | Lyocell fibers and process for their preparation |
US6221487B1 (en) | 1996-08-23 | 2001-04-24 | The Weyerhauser Company | Lyocell fibers having enhanced CV properties |
CN1061106C (zh) * | 1997-12-09 | 2001-01-24 | 宜宾丝丽雅集团有限公司 | 溶剂法纤维素纤维制造方法 |
DE10206089A1 (de) | 2002-02-13 | 2002-08-14 | Zimmer Ag | Bersteinsatz |
AT6807U1 (de) * | 2004-01-13 | 2004-04-26 | Chemiefaser Lenzing Ag | Cellulosische faser der gattung lyocell |
DE102005024433A1 (de) * | 2005-05-24 | 2006-02-16 | Zimmer Ag | Verfahren und Vorrichtung zum Schneiden von NMMO-haltigen Spinnfäden sowie für Zellulose-Stapelfasern |
AT504144B1 (de) | 2006-08-17 | 2013-04-15 | Chemiefaser Lenzing Ag | Verfahren zur herstellung von zellulosefasern aus einer lösung von zellulose in einem tertiären aminoxid und vorrichtung zur durchführung des verfahrens |
KR101580115B1 (ko) * | 2008-03-27 | 2016-01-04 | 코르덴카 게엠베하 운트 코. 카게 | 셀룰로오스 성형체 |
WO2011129444A1 (fr) | 2010-04-15 | 2011-10-20 | 株式会社ブリヂストン | Pneumatique |
PL2683858T3 (pl) * | 2011-03-08 | 2018-03-30 | Sappi Netherlands Services B.V. | Sposób suchego przędzenia obojętnej i modyfikowanej anionowo celulozy |
TWI667378B (zh) | 2014-01-03 | 2019-08-01 | 奧地利商蘭精股份有限公司 | 纖維素纖維 |
EP3467161A1 (fr) | 2017-10-06 | 2019-04-10 | Lenzing Aktiengesellschaft | Procédé de production d'un filament de cellulose de type lyocell |
EP3505659A1 (fr) | 2018-08-30 | 2019-07-03 | Aurotec GmbH | Procédé et dispositif de filage des filaments à déviation |
EP3674454A1 (fr) * | 2018-12-28 | 2020-07-01 | Lenzing Aktiengesellschaft | Procédé de filament de cellulose |
DE102019108908A1 (de) * | 2019-04-04 | 2020-10-08 | Deutsche Institute Für Textil- Und Faserforschung Denkendorf | Spannbetonkörper, Verfahren zu dessen Herstellung und dessen Verwendung |
Family Cites Families (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AT307951B (de) * | 1971-02-18 | 1973-06-12 | Deutsch Friedrich | Verfahren zur Herstellung eines Stahlbeschlagteiles für Schier, insbesondere einer Stahlkante und nach diesem Verfahren hergestellter Stahlbeschlagteil |
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 |
US4416698A (en) * | 1977-07-26 | 1983-11-22 | Akzona Incorporated | Shaped cellulose article prepared from a solution containing cellulose dissolved in a tertiary amine N-oxide solvent and a process for making the article |
DD218121A1 (de) * | 1983-10-17 | 1985-01-30 | Chemiefaser Komb Schwarza Wilh | Verfahren zur herstellung von formkoerpern aus celluloseloesungen |
GB9022175D0 (en) * | 1990-10-12 | 1990-11-28 | Courtaulds Plc | Treatment of fibres |
AT395582B (de) * | 1991-01-09 | 1993-01-25 | Brunn Betonwerk | Verfahren zur herstellung von betonpflastersteinen oder -platten mit der besonderen eigenschaft, kohlenwasserstoffe zu adsorbieren und diese auch durch wasser nicht auswaschbar einzulagern und langsam oekologisch abzubauen |
AT395862B (de) * | 1991-01-09 | 1993-03-25 | Chemiefaser Lenzing Ag | Verfahren zur herstellung eines cellulosischen formkoerpers |
GB9103297D0 (en) * | 1991-02-15 | 1991-04-03 | Courtaulds Plc | Fibre production method |
DE4308524C1 (de) * | 1992-06-16 | 1994-09-22 | Thueringisches Inst Textil | Verfahren zur Herstellung von Cellulosefasern und -filamenten nach dem Trocken-Naßextrusionsverfahren |
DE4219658C3 (de) * | 1992-06-16 | 2001-06-13 | Ostthueringische Materialpruef | Verfahren zur Herstellung von Cellulosefasern -filamenten und -folien nach dem Trocken-Naßextrusionsverfahren |
US5417909A (en) * | 1992-06-16 | 1995-05-23 | Thuringisches Institut Fur Textil- Und Kunststoff-Forschung E.V. | Process for manufacturing molded articles of cellulose |
TW256860B (fr) * | 1993-05-24 | 1995-09-11 | Courtaulds Fibres Holdings Ltd | |
AT401271B (de) * | 1993-07-08 | 1996-07-25 | Chemiefaser Lenzing Ag | Verfahren zur herstellung von cellulosefasern |
AT401063B (de) * | 1994-09-05 | 1996-06-25 | Chemiefaser Lenzing Ag | Verfahren zur herstellung von cellulosischen formkörpern |
AUPM788194A0 (en) * | 1994-09-05 | 1994-09-29 | Sterling, Robert | A building panel |
DE4444140A1 (de) * | 1994-12-12 | 1996-06-13 | Akzo Nobel Nv | Lösungsmittelgesponnene cellulosische Filamente |
-
1996
- 1996-03-04 AT AT0040796A patent/AT404032B/de not_active IP Right Cessation
-
1997
- 1997-02-26 TW TW086102333A patent/TW336259B/zh not_active IP Right Cessation
- 1997-03-03 CA CA002219110A patent/CA2219110A1/fr not_active Abandoned
- 1997-03-03 DE DE59705152T patent/DE59705152D1/de not_active Expired - Fee Related
- 1997-03-03 BR BR9702110A patent/BR9702110A/pt not_active IP Right Cessation
- 1997-03-03 AT AT97903143T patent/ATE207981T1/de not_active IP Right Cessation
- 1997-03-03 CN CN97190439A patent/CN1072284C/zh not_active Expired - Lifetime
- 1997-03-03 AU AU17594/97A patent/AU711895B2/en not_active Ceased
- 1997-03-03 JP JP9531245A patent/JPH11504995A/ja not_active Ceased
- 1997-03-03 US US08/930,132 patent/US5863478A/en not_active Expired - Fee Related
- 1997-03-03 EP EP97903143A patent/EP0823945B1/fr not_active Revoked
- 1997-03-03 WO PCT/AT1997/000041 patent/WO1997033020A1/fr not_active Application Discontinuation
- 1997-03-04 ID IDP970666A patent/ID16121A/id unknown
- 1997-10-21 NO NO19974847A patent/NO310779B1/no not_active IP Right Cessation
Non-Patent Citations (1)
Title |
---|
See references of WO9733020A1 * |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113242917A (zh) * | 2018-12-28 | 2021-08-10 | 连津格股份公司 | 从纤维素长丝纱线或纤维中去除液体的方法 |
CN113242917B (zh) * | 2018-12-28 | 2022-12-09 | 连津格股份公司 | 从纤维素长丝纱线或纤维中去除液体的方法 |
US11873580B2 (en) | 2018-12-28 | 2024-01-16 | Lenzing Aktiengesellschaft | Process for liquid removal from cellulose filaments yarns or fibers |
EP3812489A1 (fr) | 2019-10-23 | 2021-04-28 | Lenzing Aktiengesellschaft | Surface du rouleau utilisée dans la production de lyocell filaments |
Also Published As
Publication number | Publication date |
---|---|
CN1189860A (zh) | 1998-08-05 |
NO310779B1 (no) | 2001-08-27 |
ATE207981T1 (de) | 2001-11-15 |
BR9702110A (pt) | 1999-01-12 |
CN1072284C (zh) | 2001-10-03 |
JPH11504995A (ja) | 1999-05-11 |
TW336259B (en) | 1998-07-11 |
US5863478A (en) | 1999-01-26 |
EP0823945B1 (fr) | 2001-10-31 |
AT404032B (de) | 1998-07-27 |
NO974847D0 (no) | 1997-10-21 |
ATA40796A (de) | 1997-12-15 |
AU1759497A (en) | 1997-09-22 |
AU711895B2 (en) | 1999-10-21 |
NO974847L (no) | 1997-10-21 |
WO1997033020A1 (fr) | 1997-09-12 |
ID16121A (id) | 1997-09-04 |
CA2219110A1 (fr) | 1997-09-12 |
DE59705152D1 (de) | 2001-12-06 |
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