Patent Application
20240018721
The invention relates to a device for producing a fibrous web, in particular a tissue web according to the preamble of claim 1, and to a corresponding method according to the preamble of claim 7.
For some time, there has been a trend, particularly in the tissue paper market, toward tissue papers with an even higher bulk and tissue papers which are structured. However, this market is not yet so large that it is profitable for many manufacturers to convert the entire production of a tissue machine to such high-quality products. There is therefore a desire on the part of the manufacturers of such tissue products for a flexible production plant that is capable of producing both high-quality products and standard grades with a moderate conversion effort.
Under the product name “NTT”, the Valmet company offers a machine concept that promises a solution to this dilemma (htps://www.valmet.com/NTT/). A central element in this “NTT” concept is that the fibrous web is pressed between a felt and an NTT belt and then transported by means of this NTT belt to a drying device in the form of a Yankee cylinder. If a structured NTT belt is used, high-quality, textured grades can be produced while, if a smooth belt is used, standard grades can be produced.
However, a disadvantage of this concept is that a comparatively expensive NTT belt must be used even for the production of simple tissue products.
It is therefore an object of the present invention to further develop the prior art in such a way that lower-cost production of tissue papers becomes possible.
In particular, it is an object of the present invention to propose an alternative to the use of the NTT belt.
These objects are fully achieved by a device for producing a fibrous web, in particular a tissue web according to the characterizing clause of claim 1, as well as a method for producing a fibrous web, in particular a tissue web according to the characterizing clause of claim 7.
Further advantageous embodiments of the present invention can be found in the dependent claims.
As regards the device, the object is achieved by a device for producing a fibrous web, in particular a tissue web, comprising a first press, which has a first felt and a second felt, which are both guided through the press nip of the first press, and also a Yankee cylinder for drying the fibrous web and a transfer press for transferring the fibrous web to the Yankee cylinder. According to the invention, it is envisaged here that the second felt is also guided through the press nip of the transfer press, and the paper-contacting side of the second felt consists of a nonwoven layer which comprises at least 80 wt. %, in particular at least 90 wt. %, of nonwoven fibers which consist of a polyamide or of polyamides and have a fineness of 6.7 dtex and less, in particular 3.3 dtex or less.
Thus, in the invention described here, the NTT belt is replaced by a second felt. Until now, the use of felts at this position had not been considered since it is not possible to achieve the same surface properties, in particular smoothness and impermeability to water, with felts as with the coating of NTT belts.
However, the inventors have realized that this is not necessary for the operation of the process. By virtue of the extremely high fiber fineness of the nonwoven layer of a maximum of 6.7 dtex, advantageously even 3.3 dtex or less, a comparatively dense surface is produced, so that only slight dewatering by the second felt takes place in the press nip of the first press, and instead most or all of the dewatering is performed by the first felt, as in the conventional NTT method.
Furthermore, the paper-contacting side of the second felt has a smoothness which, although below that of normal NTT belts, is significantly above that of conventional felt. In particular, such a second felt is smoother than the first felt that is likewise used in the machine. This has the effect that, after the press nip of the first press, the fibrous web adheres to the smooth surface of the second felt and not to the first felt.
Thus, while the slight disadvantages of the felt in the form of poorer smoothness and slightly higher permeability to water are acceptable when compared with the NTT belt, the use of the felt offers a number of advantages.
Among other things, it is advantageous that the polyamide fibers on the paper side of the second felt are hydrophilic, while the customary polyurethane coatings of NTT belts are hydrophobic. This hydrophilic surface reduces the re-moistening of the fibrous web on the path between the first press and the Yankee cylinder.
Various polyamides can be used for the nonwoven fibers, for example PA 6, PA 6.6, PA 10, PA 12, etc. It is also possible to envisage that the nonwoven fibers of the second felt comprise various polyamides. In particular, “bicomponent fibers” (bico fibers) can be provided, which, for example, in addition to a PA 6/PA 6.6, also comprise a low-melting PA copolymer. There are many possibilities for the felt designer when choosing the polyamide or polyamides.
However, a probably even greater advantage is the fact that such a felt is significantly less expensive than a conventional NTT belt. The same plants can be used for production as for the production of conventional felts, and the production rate is significantly higher for a felt than for a coated belt. As already mentioned, this cost advantage is a significant argument, particularly in the production of standard grade tissue paper.
In advantageous embodiments, provision can be made for the second felt also to comprise further nonwoven layers, and for at least 90 wt. % of the nonwoven fibers of all the nonwoven layers to have a fineness of 6.7 dtex and less, in particular 3.3 dtex or less. These further nonwoven layers can also be nonwoven layers which are provided on the running side of the second felt.
In particularly preferred embodiments, all the nonwoven fibers of the second felt can have finenesses of 6.7 dtex and less, in particular 3.3 dtex or less. Particular preference can also be given to all nonwoven fibers made of polyamide.
In preferred embodiments, provision can be made for the paper-contacting side of the first felt to consist of a nonwoven layer which comprises at least 80 wt. % of nonwoven fibers which have a fineness of more than 6.7 dtex, in particular 11 dtex and more. In this embodiment, reliable transfer of the fibrous web from the first felt to the second felt can be ensured without special adaptation of the first press since the differences in the surface smoothness of the two felts are large enough.
It may be advantageous if, in at least one nonwoven layer, in particular all the nonwoven layers of the second felt, at least some of the nonwoven fibers are materially bonded to one another, in particular adhesively bonded, welded or fused. Since the nonwoven fibers on the surface of the second felt are very fine, there is a risk that these fibers or parts thereof will become detached from the nonwoven layer during the operation of the device, and this can lead to accelerated wear of the felt. By the material bonding of nonwoven fibers, this wear can be counteracted, making it possible to increase the service life of the felts.
One possibility of obtaining these bonds is the addition of bicomponent fibers (“bico fibers”) to the nonwoven layer, the sheath of which consists of an easily fusible polymer (preferably a PA copolymer), making it possible, with suitable heating and, if appropriate, a suitable pressure, to produce the bonds between fibers.
In advantageous embodiments, provision can be made for a large proportion of the nonwoven fibers or at least of the nonwoven layer of the paper-contacting side of the second felt to consist of bico fibers. Thus, for example, more than 25 wt. %, in particular between 30 wt. % and 60 wt. %, preferably between 49 wt. % and 50 wt. %, of the nonwoven fibers of one layer or of all the layers can consist of bico fibers.
As an alternative or in addition, however, nonwoven fibers can also be bonded in a different way, being welded for example. Transmission welding using a proportion of absorbent fibers is an advantageous method for producing such welded joints.
In order to keep the dewatering of the fibrous web by the second felt as low as possible, it can be advantageous if the second felt has an air permeability of less than 5 cfm (approximately 142 1/min), in particular of 0 cfm. In order to achieve these low values, the provision of large proportions of bico fibers as described above is very helpful, for example.
In the first press, significant dewatering of the fibrous web takes place. It is advantageous if the first press is designed as a shoe press. In contrast, the main function of the transfer press is to ensure the transfer of the fibrous web from the second felt to the surface of the Yankee cylinder. Here, a complicated shoe press—although possible—is not necessary and does not make economic sense. A simple roll nip is usually sufficient for the transfer press.
As regards the method, the object is achieved by a method for producing a fibrous web, in particular a tissue web, comprising the following steps
The pressing in the first press—which, in particular, can be embodied as a shoe press—can advantageously be carried out at more than 200 kN/m, in particular between 400 kN/m and 600 kN/m.
The invention is explained below by means of schematic figures; however, the invention is not limited to the examples shown here. In particular:
After leaving the press nip of the first press 2, the fibrous web 1—in particular a thin tissue web 1—does not adhere to the first felt 10 but to the second felt 20. This is due to the surface of the second felt 20, which is comparatively smooth for a felt. In the example shown in
In the schematic illustration of
From a headbox 40, the fibrous suspension is brought into a forming section, where the initial dewatering takes place. In this case, the formation of the fibrous web 1 takes place between the first felt 10 and a dewatering screen 30. Dewatering elements, such as a suction roll 50 or suction boxes (not shown in the figure), are usually provided here. The fibrous web 1 is then transported on the first felt 10 with a still relatively high moisture content to the first press 2. As described with regard to
By means of a transfer press 3, the fibrous web 1 is transferred to the surface of the Yankee cylinder 4. Further drying of the fibrous web 1, that is to say in this case the tissue web 1, is performed by means of the usually steam-heated Yankee cylinder 4. In most cases, a hood 5 is provided, through which hot air is blown onto the tissue web 1. After the tissue web 1 has been removed from the Yankee cylinder 4—usually by means of crepe scrapers (not shown explicitly here)—the tissue web 1 is wound up with a reel 60 to form rolls, which can undergo further processing.
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/EP2021/084125 | 12/3/2021 | WO |
| Number | Date | Country | |
|---|---|---|---|
| 63122225 | Dec 2020 | US |
