EP0052845B1 - Etirage dans l'eau - Google Patents
Etirage dans l'eau Download PDFInfo
- Publication number
- EP0052845B1 EP0052845B1 EP81109691A EP81109691A EP0052845B1 EP 0052845 B1 EP0052845 B1 EP 0052845B1 EP 81109691 A EP81109691 A EP 81109691A EP 81109691 A EP81109691 A EP 81109691A EP 0052845 B1 EP0052845 B1 EP 0052845B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- stretching
- predrawing
- temperature
- water
- main drawing
- 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
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 24
- 229920000728 polyester Polymers 0.000 claims abstract description 7
- 238000000034 method Methods 0.000 claims description 12
- 230000008569 process Effects 0.000 claims description 6
- 239000000835 fiber Substances 0.000 description 34
- 238000004043 dyeing Methods 0.000 description 11
- 238000010186 staining Methods 0.000 description 6
- PYWVYCXTNDRMGF-UHFFFAOYSA-N rhodamine B Chemical compound [Cl-].C=12C=CC(=[N+](CC)CC)C=C2OC2=CC(N(CC)CC)=CC=C2C=1C1=CC=CC=C1C(O)=O PYWVYCXTNDRMGF-UHFFFAOYSA-N 0.000 description 5
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 4
- 230000002093 peripheral effect Effects 0.000 description 4
- -1 polyethylene terephthalate Polymers 0.000 description 4
- 229920000139 polyethylene terephthalate Polymers 0.000 description 4
- 239000005020 polyethylene terephthalate Substances 0.000 description 4
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 2
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 description 2
- 125000002877 alkyl aryl group Chemical group 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 239000012153 distilled water Substances 0.000 description 2
- 239000003995 emulsifying agent Substances 0.000 description 2
- 239000000839 emulsion Substances 0.000 description 2
- QWVGKYWNOKOFNN-UHFFFAOYSA-N o-cresol Chemical compound CC1=CC=CC=C1O QWVGKYWNOKOFNN-UHFFFAOYSA-N 0.000 description 2
- 229920000151 polyglycol Polymers 0.000 description 2
- 239000010695 polyglycol Substances 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 239000008399 tap water Substances 0.000 description 2
- 235000020679 tap water Nutrition 0.000 description 2
- ACNUVXZPCIABEX-UHFFFAOYSA-N 3',6'-diaminospiro[2-benzofuran-3,9'-xanthene]-1-one Chemical compound O1C(=O)C2=CC=CC=C2C21C1=CC=C(N)C=C1OC1=CC(N)=CC=C21 ACNUVXZPCIABEX-UHFFFAOYSA-N 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- OFOBLEOULBTSOW-UHFFFAOYSA-N Malonic acid Chemical compound OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 238000004026 adhesive bonding Methods 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000009987 spinning Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
Images
Classifications
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D5/00—Formation of filaments, threads, or the like
- D01D5/12—Stretch-spinning methods
-
- 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
- D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
- D01F6/58—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products
- D01F6/62—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyesters
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S264/00—Plastic and nonmetallic article shaping or treating: processes
- Y10S264/28—Stretching filaments in gas or steam
Definitions
- the invention relates to a method for stretching fiber cables made of polyester with a pre-stretching and a main stretching at a predetermined value for the total stretching ratio.
- a very similar method for preheating cables made of polyester threads is known from DE-AS 2149793.
- the cables are then passed through an immersion bath at 40-65 ° e while circulating the penultimate roller of the infeed roller mill.
- the purpose is to heat the cable evenly. Even after this publication, the cable therefore always remains at an elevated temperature from the water bath until it is stretched.
- the fiber cables obtained according to this state of the art, or the staple fibers obtained from them do not yet meet the requirements placed on them in every respect, in particular not with regard to the uniformity of the dyeability.
- the object of the invention is therefore to achieve a further improvement in the uniformity of the stretching of fiber cables, which is expressed in a significant reduction in the number of dyeing errors.
- the stretching ratio, stretching temperature and stretching medium should remain freely selectable.
- the method according to the invention achieves this object in that pre-stretching in water takes place at 71-90 ° C., that the stretching ratio in the pre-stretching is chosen between 1: 1.05 and 1: 1.6 so that the main stretching takes place at a minimum of Stretching tension occurs and that the fiber cables between the preliminary and main stretching cool again to below 40 ° C.
- the draw ratio in the pre-draw zone is preferably below 1: 1.4, very particularly preferably in the range from 1: 1.1 and 1: 1.3.
- Fiber cables are endless structures made up of a large number of filaments and by combining the filaments of several spinnerets.
- the fiber cables have titers of up to 1 million dtex and more. After the common treatment of all filaments, they are usually cut into staple fibers, which in turn are further processed into spun fiber yarns
- the fiber cables used in the process according to the invention consist of polyester, i.e. from linear high polymers and at least 85% repeating units from terephthalic acid and a dihydric alcohol The remaining 15% of the repeating units of the polymer can be formed by comonomers in both the dicarboxylic acid and the glycol components.
- the pre-stretching is an orienting stretching, that is to say one which is accompanied by an increase in the birefringence, but is not yet associated with the formation of a stretching point.
- a stretch point is understood to mean the suddenly and clearly visible change in diameter (“bottle neck”) of polyester filaments with little orientation during stretching.
- the birefringence of the spun fabric only increases with a pre-stretching ratio of 1: 1.05.
- the preliminary stretching is carried out in water.
- Water means both pure water and aqueous solutions or emulsions e.g. the usual textile auxiliaries, finishing agents or preparations.
- the water has a temperature of 71-90 ° C. If the temperature is outside these limits, the number of staining errors increases significantly.
- the preliminary drawing in water at 71-90 ° C. is carried out with a drawing ratio such that the drawing tension required in the main drawing reaches a minimum. This results in pre-drawing ratios between 1: 1.05 and 1: 1.6. A deviation from these drawing ratios in the pre-drawing zone leads to a deterioration in the uniformity of dyeing.
- the main stretching is carried out as usual, for example in steam or in hot water. The best results are obtained if you do the main stretching in hot water.
- the main stretch is also an orienting stretch. In contrast to the pre-stretching, it is with Stretch point formation connected.
- the main stretching can also take place in two stages or be followed by the different fixing processes, the advantage of the method according to the invention is retained.
- the preliminary drawing is carried out in such a way that the required drawing tension in the main drawing takes a minimum.
- the minimum of the stretching tension in the main stretching zone is determined by varying the pre-stretching ratio.
- the yield stress is the quotient of the tensile force of the fiber cable, which can be measured with a commercially available tensile force meter (e.g. from Schmidt, Waldkraiburg), and the final titer of the stretched fiber cable.
- the final titer of the stretched fiber cable is the product of the spinning titer used with the total stretch ratio used.
- the fiber cables cool to below 40 ° C. between the preliminary and the main drawing. This does not necessarily require active, additional cooling, but can be achieved by routing the fiber cables around unheated rollers. Since several cables are always used in fiber cables due to the large forces that occur, e.g. Roller septets, the fiber cables then assume almost room temperature on their own, provided that there is no additional heating. However, cooling the rolls with water is advantageous.
- the number of staining errors is determined from staining with rhodamine:
- the colored cable tape is then rinsed under running tap water until the water no longer shows a red color.
- the cable tape is washed out for at least 15 minutes in a solution of 0.5 g / l of an alkylaryl polyglycol ether (emulsifier O Hostapal CV from Hoechst AG) for about 75-80 ° with frequent stirring and rinsed again with running tap water until no more foam is visible .
- an alkylaryl polyglycol ether emulsifier O Hostapal CV from Hoechst AG
- the counting of undrawn capillaries or gluing to rhodamine-colored cable ties is carried out in a dark room under UV light. Undrawn capillaries shine bright to dark red.
- a polyethylene terephthalate fiber cable made of 446080 filaments with a single titer of the stretched fiber of 1.7 dtex was stretched in two stages between roller septets.
- the width of the fiber cable was about 30 cm.
- the first septet ran at a peripheral speed of 43 m / min at room temperature. Between the first and second septet there was a water bath at 79 ° C and 3.20 m in length. The speeds of the 2nd septet are shown in Table 1, the temperature of the rolls of the 2nd septet was 14 ° C. The pre-stretching ratio VV results from the speeds of the first and second septet. From the 2nd septet the fiber cable ran through a 2nd drawing bath of 3.60 m in length and a temperature of 79 ° C to a 3rd septet which with a peripheral speed of the rollers of 118 m / min at a temperature of the rollers of 185 ° C ran. The total draw ratio GV was 2.7. A fourth septet with a temperature of 140 ° C and a peripheral speed of 116 m / min followed.
- the table also shows the properties of the fibers obtained and the measured values of the drawing tension in the pre-drawing W and in the main drawing HV and the number of dyeing errors per 20 g of staple fibers.
- Table 1 shows how the minimum number of dyeing errors per 20 g of fibers is achieved with the minimum of the stretching tension in the main drawing.
- Example 1 was repeated at a constant speed of 51.6 m / min of the 2nd septet, that is to say a pre-stretching ratio of 1: 1.2, as had been found to be ideal according to Example 1. This time, however, the temperature of the 1st bath was varied.
- Table 2 shows how the number of rhodamine events (staining error initially decreases with increasing water temperature up to 80 ° C, but then rises again with increasing water temperature.
- Fig. 4 shows this graphically.
- the 1st septet ran at a circumferential speed of 48 m / min at room temperature.
- the first water bath had a temperature of 80 ° C.
- the second septet each had a peripheral speed of 57.6 m / min, which results in a pre-stretching ratio of 1: 1.2, the godet temperature was varied.
- the second water bath was 80 ° C.
- the third septet had a temperature of 179 ° C, the fourth septet 135 ° C.
- Table 3 shows how, under largely constant drawing conditions, the number of dyeing errors increases sharply if the fiber cable cannot cool down before reaching the second water bath, but is kept at 70 ° C or 80 ° C by heated godets. With this mode of operation, the total draw ratio even had to be reduced, since a large number of torn filaments led to winding on the 3rd septet.
Landscapes
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Mechanical Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
- Water Treatment By Sorption (AREA)
- Artificial Filaments (AREA)
Claims (3)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT81109691T ATE5979T1 (de) | 1980-11-24 | 1981-11-14 | Wasserverstreckung. |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19803044073 DE3044073A1 (de) | 1980-11-24 | 1980-11-24 | Wasserverstreckung |
DE3044073 | 1980-11-24 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0052845A1 EP0052845A1 (fr) | 1982-06-02 |
EP0052845B1 true EP0052845B1 (fr) | 1984-01-25 |
Family
ID=6117356
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP81109691A Expired EP0052845B1 (fr) | 1980-11-24 | 1981-11-14 | Etirage dans l'eau |
Country Status (4)
Country | Link |
---|---|
US (1) | US4418032A (fr) |
EP (1) | EP0052845B1 (fr) |
AT (1) | ATE5979T1 (fr) |
DE (2) | DE3044073A1 (fr) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA2175875C (fr) * | 1995-05-08 | 2006-11-28 | Hoe Hin Chuah | Methode de preparation de fils de poly(trimethyleneterephtaloyl) |
CN1160492C (zh) * | 1998-03-31 | 2004-08-04 | 宇部日东化成株式会社 | 拉伸方法和拉伸产物 |
DE202007006816U1 (de) * | 2007-05-11 | 2008-09-18 | Coroplast Fritz Müller Gmbh & Co. Kg | Handeinreißbares Gewebe-Klebeband |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2918346A (en) * | 1956-08-07 | 1959-12-22 | Du Pont | Process of orienting a dense tow of polymeric ester filaments by two step hot aqueous bath treatments |
DE1660140A1 (de) * | 1965-01-29 | 1970-07-16 | Patentdienst Anstalt F | Verfahren zum kontinuierlichen Verstrecken endloser,synthetischer Faeden |
GB1088015A (en) * | 1965-02-23 | 1967-10-18 | Monsanto Co | Polyester drawing process |
JPS479226U (fr) * | 1971-02-19 | 1972-10-04 | ||
JPS4714055U (fr) * | 1971-03-18 | 1972-10-19 | ||
DE2149793B2 (de) * | 1971-10-06 | 1977-03-10 | Zimmer Ag, 6000 Frankfurt | Verfahren zum verstrecken eines kabels aus polyesterfaeden |
-
1980
- 1980-11-24 DE DE19803044073 patent/DE3044073A1/de not_active Withdrawn
-
1981
- 1981-11-14 AT AT81109691T patent/ATE5979T1/de not_active IP Right Cessation
- 1981-11-14 EP EP81109691A patent/EP0052845B1/fr not_active Expired
- 1981-11-14 DE DE8181109691T patent/DE3162051D1/de not_active Expired
- 1981-11-19 US US06/322,730 patent/US4418032A/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
DE3162051D1 (en) | 1984-03-01 |
DE3044073A1 (de) | 1982-07-08 |
EP0052845A1 (fr) | 1982-06-02 |
ATE5979T1 (de) | 1984-02-15 |
US4418032A (en) | 1983-11-29 |
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