The present invention relates to a regenerated cellulose fiber in the form of a solid viscose flat fiber.
Flat Fibers and their manufacture are known. In contrast to the cross-section of fibers which commonly is essentially round, flat fibers have an essentially flat or, respectively, oblong cross-section.
On the one hand, cellulosic flat fibers can be produced by spinning a cellulose or a spinning dope containing a cellulose derivative through slot-shaped spinnerets. In case of viscose fibers, flat fibers can alternatively be produced in the form of collapsed hollow fibers. In doing so, a gas, e.g. nitrogen, or a blowing agent, e.g., sodium carbonate, is admixed to the spinning viscose. During the spinning of the fibers through dies, which are per se conventional, hollow fibers are formed whose walls, however, are so thin when appropriate process conditions are chosen that the Fibers will collapse and will then be provided in the form of flat fibers.
The article by C. R. Woodings, A. J. Bartholomew; “The manufacture properties and uses of inflated viscose rayon Fibers”; TAPPI Nonwovens Symposium; 1985; pp. 155-165.
Source: http://www.nonwoven.co.uk/publications_cat4.php, describes different types of hollow fibers and their uses.
WO 2006/134132 describes the use of viscose flat fibers in a fiber composite for the purpose of improving the dissolubility of the fiber composite in water. According to WO 2006/134132, the flat fibers used preferably have a crenelated (pinnacle-type) surface and, in contrast to collapsed hollow fibers, are produced by being spun through a slot die.
The manufacture of cellulosic flat fibers is known, for example, from GB 945,306 A, U.S. Pat. Nos. 3,156,605 A, 3,318,990, GB 1,063,217 A. Such fibers have been recommended especially for use in paper production, as is described in part in the above-mentioned documents.
DE 1 254 955 as well as GB 1,064,475 deal with paper produced from viscose fibers having flat cross-sections.
In these documents, it is thereby described as desirable that the fibers exhibit high transparency so that the paper produced from the fibers is transparent as well.
Regarding the production of flat viscose fibers, DE 1 254 955 describes five distinct variants. However, as to the production of a transparent fiber, only one exemplary embodiment is disclosed concretely. In this example, a high-molecular substance swelling in water, namely polyvinyl alcohol (PVA), is admixed to the viscose spinning dope. Sodium carbonate is also added to the spinning dope. The resulting fiber is thus a collapsed hollow fiber which contains a certain amount of PVA.
It is the object of the present invention to provide a viscose flat fiber which exhibits high transparency and is particularly suitable for the production of paper.
The object of the present invention is achieved by a regenerated cellulose fiber in the form of a solid viscose flat fiber having the following properties:
Furthermore, the invention relates to a fiber bundle containing the cellulose fiber according to the invention, a method of producing the cellulose fiber according to the invention and the fiber bundle, respectively, as well as the use of the cellulose fiber according to the invention and of the fiber bundle, respectively, for the production of nonwoven fabrics and paper.
In a further aspect, the present invention relates to a paper containing the cellulose fiber according to the invention.
The present invention relates to a solid viscose flat fiber having high transparency.
For the purposes of the present invention, solid “is understood to relate to a cellulose fiber which does not have a hollow or collapsed structure. In particular, the solid cellulose fiber according to the present invention exhibits no hollow spaces and no separating line resulting, for example, from the collapse of a hollow fiber.
Surprisingly, it has been found that it is possible to produce viscose flat fibers having high transparency which are solid and do not contain a noteworthy amount of swelling high-molecular substances.
Preferably, the fiber according to the invention consists essentially completely of cellulose. Essentially “is thereby understood to mean that, apart from conventional processing aids which are included in the final product within the scope of the viscose process, such as, e.g., finishing, no further components, in particular no high-molecular substances swelling in water, are included. A finishing overlay typically accounts for 0.1% and not more than 0.3%.
The surface of the flat fiber according to the invention is essentially smooth. The surface “is thereby understood to be the two faces which define the fiber's broadside.
Essentially smooth “is understood to mean in particular that the fiber, apart from its edge regions, features essentially no grooves in the longitudinal direction which have a groove thickness of more than 10%, in particular more than 5%, of the fiber thickness. Grooves “are thereby understood to be indentations in the longitudinal direction which are small relative to the width of the fiber and are typical for standard viscose fibers, as is apparent, for example, from
Due to the shrinking processes which are typical for viscose fibers, the presence of a relatively deep groove or arching, respectively, in the edge regions of the fiber is in most cases not preventable.
The two faces of the fiber which define the fiber's broadside are preferably parallel to each other across an area of at least 90% of the fiber surface.
Preferably, the ratio of width B to thickness D of the fiber according to the invention is 20:1 or higher.
The titer of the fiber according to the invention can range from 2 to 40 dtex, in particular from 2 to 28 dtex.
Preferably, the fiber can be provided as a short-cut fiber with a length of cut ranging from 2 to 20 mm, particularly preferably from 3 to 12 mm. In particular for the application in nonwoven fabrics and textiles, the fiber may also be provided as a staple fiber with lengths of cut ranging from 30 mm to 150 mm, in particular from 40 to 110 mm, particularly preferably of 40 mm (cotton type) and 70 mm (wool type).
In a further preferred embodiment of the present invention, the fiber according to the invention can be modified anionically.
It has been found that anionic modification of the fiber increases the strength of papers produced therefrom.
Preferably, the anionic modification of the fiber is achieved in that carboxymethyl cellulose (CMC) is incorporated in the fiber. The incorporation of CMC in viscose fibers is described, inter alia, in WO 2011/12423A.
The present invention also relates to a fiber bundle containing a plurality of cellulose fibers according to the invention.
A “Fiber bundle” is understood to be a plurality of fibers such as, e.g., artificial cell-wool (a plurality of staple fibers), a strand of continuous filaments or a bale of fibers.
In the fiber bundle according to the invention, the cross-sections of the cellulose fibers contained therein are preferably essentially the same.
The method of producing a cellulose fiber according to the invention and, respectively, a fiber bundle according to the invention comprises the following steps:
wherein
Surprisingly, it has been found that solid viscose flat fibers with excellent transparency can be produced by combining these process measures.
By adding a coagulation retarder (in particular PEG), a delayed coagulation of the viscose spinning dope in the spinning bath is effected. In this way, the period for the diffusion of the liquid out of the fiber is prolonged and the formation of a smooth surface is rendered possible. Likewise, the time during which gas bubbles can diffuse out of the fiber is thus prolonged.
Preferably, the viscose contains the coagulation retarder, in particular PEG, in an amount ranging from 1 to 6% by weight, preferably from 1 to 5% by weight, particularly preferably from 3 to 5% by weight, in particular from 3 to 4% by weight, based on cellulose.
However, the addition of a coagulation retarder also has the effect that the spun fiber has more time for reducing its surface area due to its surface tension. In the normal case, this causes the fiber to approach more and more the round shape.
According to the invention, this effect is counteracted in various ways:
The remaining processing parameters can be kept in ranges which are common for the viscose process. With regard to the spinning bath composition, a person skilled in the art will regard a content of sodium sulfate of 250-400 g/l and a content of zinc sulfate of 5-20 g/l as common A typical standard spinning viscose has a content of cellulose of 8-10% by weight and a content of NaOH of 5-9% by weight.
The processing parameters according to the invention cause the fiber to shrink preferably in the direction of its thickness (y-direction), whereby very thin fibers with a very high ratio of width to thickness and thus a large surface area, which is particularly desirable for paper production, are formed.
Accordingly, the fibers according to the invention are perfectly suitable for use in papers, in particular in transparent papers.
It has been found that a laboratory sheet of 80 grams (Rapid-Köthen, DIN EN ISO 5269-2), made by 100% of a fiber according to the invention which has been cut to 6 mm, can have a breaking length (DIN EN ISO 1924-2) of at least 750 m.
For the application in the production of paper, the length of the fiber according to the invention preferably amounts to 3-12 mm.
However, the fibers according to the invention are also perfectly suitable for the production of nonwoven fabrics, e.g., hydro-entangled nonwoven fabrics or needled nonwoven fabrics.
Viscose was spun through a spinneret having slot-shaped openings with a length of 1000 μm and a width of 60 μm and treated further as follows:
Cross-sections of the fibers thus obtained are illustrated in
The fiber cross-sections are very flat and thin. The two faces defining the fiber's broadside run parallel to each other virtually across the entire width of the fiber. Small protuberances are provided only at the fiber edge.
The width B of the fiber amounted to 230 μm, its thickness D was 6 μm. This results in a ratio B:D of 38:1 as well as a titer of 22 dtex.
A Rapid-Köthen sheet of 80 grams, which has been produced without use of additives, made by 100% of the fiber according to the invention already exhibits a breaking length of 1000 m, which enables good handling of the sheet. So far, such strengths have been achieved in viscose fibers only with a hollow fiber process which requires vastly higher production expenditures.
Viscose was spun through a spinneret having slot-shaped openings with a length of 700 μm and a width of 35 μm and treated further as follows:
The fiber cross-sections are very flat and thin. The two faces defining the fiber's broadside run parallel to each other virtually across the entire width of the fiber. Small protuberances are provided only at the fiber edge.
The width B of the fiber amounted to 150 μm, its thickness D was 4 μm. This results in a ratio B:D of 38:1 as well as a titer of 9 dtex.
As can be seen from
A Rapid-Köthen sheet of 80 grams, which has been produced without use of additives, made by 100% of the fiber according to the invention already exhibits a breaking length of 2600 m, which enables a very good handling of the sheet.
Viscose fibers were spun under conditions similar to those in Example 1, however, the spinning viscose did not contain PEG.
The fibers obtained exhibit (see
Viscose fibers were spun under conditions similar to those in Example 1, however, the slot-shaped openings of the spinneret had a length of 140 μm and a width of 25 μm, i.e., a ratio of length to width of less than 10:1. Accordingly, the titer amounted to 2.1 dtex.
The cross-sections of the fibers (see
Viscose fibers were spun under conditions similar to those in Example 1, however, the viscose spinning dope did not contain PEG and the spinning settings (draft, stretching, spinning bath composition) corresponded to those of a standard viscose process.
Again, the Fibers (
The longitudinal view of the fiber (see
Number | Date | Country | Kind |
---|---|---|---|
1191093 | Nov 2011 | EP | regional |
Filing Document | Filing Date | Country | Kind |
---|---|---|---|
PCT/EP2012/072387 | 11/12/2012 | WO | 00 |
Publishing Document | Publishing Date | Country | Kind |
---|---|---|---|
WO2013/079305 | 6/6/2013 | WO | A |
Number | Name | Date | Kind |
---|---|---|---|
2506046 | Steinlin | May 1950 | A |
3113828 | Geiger | Dec 1963 | A |
3156605 | Anderer | Nov 1964 | A |
3318990 | Kajitani | May 1967 | A |
3418405 | Kajitani | Dec 1968 | A |
3565652 | Burnet et al. | Feb 1971 | A |
4569343 | Kimura | Feb 1986 | A |
5047197 | Uneback | Sep 1991 | A |
7258764 | Mauler | Aug 2007 | B2 |
20060200103 | Schmidtbauer | Sep 2006 | A1 |
Number | Date | Country |
---|---|---|
41 397 | Sep 1965 | DE |
1 254 955 | Nov 1967 | DE |
14 94 762 | Apr 1970 | DE |
230 030 | Nov 1985 | DE |
2280099 | Feb 2011 | EP |
945 306 | Dec 1963 | GB |
1 063 217 | Mar 1967 | GB |
1 064 475 | Apr 1967 | GB |
1063217 | Apr 1967 | GB |
20060134132 | Dec 2006 | WO |
20100071906 | Jul 2010 | WO |
20110012423 | Feb 2011 | WO |
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Number | Date | Country | |
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20140308870 A1 | Oct 2014 | US |