EP1268888A1

EP1268888A1 - Method and device for the production of cellulose fibres and cellulose filament yarns

Info

Publication number: EP1268888A1
Application number: EP01957604A
Authority: EP
Inventors: Christoph Michels; Birgit Kosan
Original assignee: Thueringisches Institut fuer Textil und Kunststoff Forschung eV
Current assignee: Thueringisches Institut fuer Textil und Kunststoff Forschung eV
Priority date: 2000-03-11
Filing date: 2001-03-06
Publication date: 2003-01-02
Anticipated expiration: 2021-03-06
Also published as: KR20020081580A; EP1268888B1; DE50107999D1; US6887409B2; US20030116882A1; WO2001068958A1; CN1205364C; KR100760642B1; CN1416481A; DE10190965D2; AU2001281467A1; ATE309400T1

Abstract

A method for the production of cellulose fibers or filaments from cell material, by the dry-wet extrusion method with aqueous amine oxides, in particular, N-methylmorpholine-N-oxide as solve is described comprising the following steps: a) dispersion of a cell material, or a cell material mixture with a cuoxam DP from 250-3000, in aqueous amine oxide, b) transformation of the obtained dispersion, by water evaporation with shear, at elevated temperature, into a homogeneous solution with a zero shear viscosity of 600 to 6000 Pa.s and a relaxation time of 0.3 to 50 seconds all at 85° C., c) feeding the solution to a spinning jet, previous to which it is passed through flow chamber prior the jet(s), in which the retention time at the spinning temperature, d) forming the solution into at least one capillary in each spinning jet, drawing the capillary(ies) from each jet through anon-precipitating medium and then precipitating the cellulose fibers on drawing through a precipitating bath and e) at the end of the precipitating bath section drawing off the fibers by deflecting the precipitation flow. In stage d) the capillary bundle(s) are treated with a gas flow, just before the entry thereof into the precipitating bath, at an angle alpha to the capillary flow, wherein 45°<alpha<90°.

Description

Method and device for producing cellulose fibers and cellulose filament yarns

The main application relates to a process for producing cellulose fibers or filaments from cellulose by the dry-wet extrusion process with aqueous amine oxides, in particular N-methylmorpholine-N-oxide as solvent, in which a) cellulose or a cellulose mixture with a Cuoxam -DP dispersed in the range from 250 to 3000 in aqueous amine oxide, b) the dispersion obtained at elevated temperature with dehydration and shear in a homogeneous solution with a zero shear viscosity in the range from 600 to 6000 Pa-s and a relaxation time in the range from Transferred from 0.3 to 50 s at 85 ° C. in each case, c) the solution is fed to at least one spinneret and previously passed through a flow chamber common to the nozzle (s), in which its residence time is at least equal to its relaxation time at the spinning temperature, d) the solution in each spinneret is deformed into at least one capillary and the capillary (s) of each nozzle is distorted h leads a non-precipitating medium and then with precipitation of the cellulose threads through a precipitation bath, and e) separates the cellulose threads at the end of the precipitation bath section by deflection from the precipitation bath streams and withdraws the threads. Furthermore, the main application relates to a device for the production of cellulose fibers or filaments from cellulose by the dry-wet extrusion process with aqueous amine oxides as solvent with a spin pack with a spinneret plate, spinnerets and a common one arranged above the spinneret plate and the spinnerets arranged in a row Inflow chamber, the volume of which corresponds to the relationship V> vyλ, where V is the volume of the inflow chamber in cm 3, v is the volume flow of the cellulose solution in cm3 / s and Λ the

Relaxation time at the maximum frequency of the relaxation spectrum of the spinning solution, furthermore with a precipitation bath in two by one Precipitation bath pump connected containers, a gap between the spinnerets and the precipitation bath surface in the upper of the two containers, and a withdrawal godet.

The main application was based on the task of creating a method and a device by means of which the spinning of fibers and the multiple spinning of filament yarns with good mechanical fiber properties is possible with high capillary density, spinning security and take-off speed. In particular, the uniformity and uniformity of the volume flows through each nozzle should be increased compared to the known methods.

In the main application it is stated that the gap width a with the relaxation time the spinning solution at the frequency maximum of the relaxation time spectrum at the spinning temperature and the take-off speed v 3 (equation II) and on the other hand correlates with the distance x between two adjacent nozzle holes, the length of the precipitation bath path w and the nozzle hole diameter D (equation III). Since the relaxation time in seconds and the residence time of the deformed solution in gap a are in the millisecond range, it should be possible to achieve much larger gap widths than previously in practical operation. For the spinning of fibers and filaments, the maximum adjustable gap, ie the stretch on which the "solution thread" is more or less strongly oriented according to the draft ratio, is of particular importance. As the gap width increases, the rate of stretch and thus the thread tension decrease. This has a positive effect on the mechanical fiber parameters, in particular the elongation at break and the loop tearing force. On the other hand, the spinning security decreases with increasing gap width, since the risk of touching the capillaries increases. This is especially true when spinning fibers, where you work with the highest possible capillary density. It is therefore essential to set a maximum gap that does justice to spinning safety, but also results in optimal mechanical fiber parameters. The Decreasing the thread tension is also a prerequisite for increasing the take-off speed, especially when spinning filament yarns.

The object of the present invention is therefore in the sense of the main application to create a method and a device by which the spinning of fibers and the multiple spinning of filament yarns with good mechanical fiber properties is possible with high capillary density, spinning security and take-off speed. In particular, the mechanical fiber properties, namely the elongation at break and the loop tearing force, are to be improved while maintaining the spinning safety. In addition, an increase in the take-off speed is to be made possible, in particular when spinning filament yarns.

This object is achieved according to the invention in the method mentioned at the outset by, in stage d), the capillary family (s) shortly before they enter the precipitation bath with a gas at an angle ^κ to the ^{direction of} the capillary movement in the range 45 ° <* * 90 ° flows. Surprisingly, it has been shown that the gap width can be increased considerably, namely by 50 to 100% or more, without impairing the spinning security. The reduced stretching speed and thread tension in the gap due to the larger gap width leads to the desired improvement in the mechanical fiber parameters mentioned and the possibility of increasing the take-off speed.

In particular, the invention object is also achieved in ^that, in stage) d Kapillarenschar immediately prior to its entry into the coagulation bath with a gas flows against, wherein the coagulation bath at the interface to the air gap and the gas stream have the same direction of flow components. The effect of increasing the maximum gap width is thus also achieved if the gas flow and the precipitation bath flow have horizontal flow components which are in the same direction. Appropriately, the flow of capillaries is flown with a flat, flat gas stream that extends over the entire width of the row of capillary groups. It is important that the gas flow becomes effective at the immersion points of the capillary sheets in the precipitation bath. The spinning disturbances which impair spinning safety and which are caused almost exclusively by touching the capillaries when entering the spinning bath are substantially reduced. Surprisingly, it has been shown that, despite the flow of gas flowing into the capillary sheets, the movement of the surface of the spinning bath is calmed when the capillary sheets are immersed. In general, it can be said that the inflow of capillaries causes a mechanical effect at the immersion point; in particular, the cooling of the capillary sheets plays no role.

The object is further achieved according to the invention in the device mentioned at the outset in that in the gap a at least one slot nozzle with an angle * directed at an angle * to the direction of the capillary in the region 45 ° ^<c <90 ° for the inflow of capillaries before they enter the Precipitation bath is arranged. The slot width can be, for example, 0.05 to 5 mm, for example 1 mm. The slot length corresponds at least to the length of the row of capillary inflows. These are preferably arranged in a row (not in a plurality of rows which are staggered one behind the other) so that all the sheets are flowed through in the same way by the gas stream.

According to the invention, the device mentioned at the outset is preferably characterized in that the upper bath container on the one hand of the capillary sheets has at least one inlet opening for precipitation bath liquid and on the other hand the capillary sheets at least have an overflow and the slot die with respect to the row of capillary sheets is on the same side as the inlet opening (s) is arranged. As a result, the precipitation bath liquid and the gas stream in the gap have rectified horizontal flow components, which increases the maximum Gap width is conducive.

The slot die is preferably mechanically connected to the at least one overflow. The slot gas nozzle is therefore always at the same (small) distance from the precipitation bath surface regardless of the vertical setting of the overflow and thus the size of the gap width.

The device mentioned above for the production of cellulose fibers or filaments is further characterized according to the invention in that the width of the gap a and the relaxation time of the spinning solution satisfy the following relationship _{a <} { _{5 + 16} ^] y- ^m '- ^ (II.) in which a is the gap width in mm, λ is the relaxation time at the maximum frequency of the relaxation spectrum of the spinning solution, v is the withdrawal speed

-2 ^a speed in m / min N Düsenlochdurch- the diameter in mm mean capillary density in cm and D. The term 1 / rN-D added to equation II of the main application takes into account the enlargement of the gap width achieved according to the invention due to the flow against the capillary shares shortly before their contact with the precipitation bath. It can be seen that this gap widening decreases with increasing capillary density.

The dimensions of the spinnerets, the gap width a and the precipitation bath path w preferably satisfy the relationship

a + w x> - -3.5D (purple)

where x is the distance between two adjacent nozzle holes, a is the gap width, w is the length of the precipitation bath section and D is the nozzle diameter. From a comparison with relation III of the main application, it can be seen that the inflow of air into the capillary family (s) can reduce the distance between two adjacent nozzle holes of the nozzle by 1/8, without the objectives of the invention, namely maintaining the spinning safety while improving mechanical Fiber properties are affected. The invention is explained in more detail with reference to the drawing and the example. Show it

1 shows the relaxation time spectrum of a spinning solution with 12% by mass of cellulose (Cuoxam-DP 480) at the spinning temperature of 85.degree.

Figure 2 is a schematic representation of an apparatus for producing cellulose fibers and filaments; and

Figure 3 is a schematic plan view of the device shown in Figure 2.

FIGS. 2 and 3 show the upper precipitation bath container 1 of a spinning device according to the invention. The spinnerets 6, of which only one is visible in FIG. 2, are provided with inflow chambers, as is described and illustrated in more detail in the main application. The outlet sides of the spinnerets 6 are at a distance from the precipitation bath surface 7 which forms the air gap a. The bottom 10 of the precipitation bath container 1 is equipped, according to the arrangement of the nozzles 6, with a plurality of thread guide elements 11, through which the thread bundles 12 emerge from the container 1 together with precipitation bath liquid flows 14. The thread bundles 12 of all the thread guide elements 11 are deflected by the precipitation bath streams 14 at an angle and wound up with a suitable tension. The precipitation bath streams 14 enter the lower precipitation bath container (not shown) and are pumped back into the upper precipitation bath container 1 by means of a pump (not shown) via line 16. The precipitation bath path w passed by the thread bundles 12 extends from the bath surface to the point below the thread guide elements 11 where the thread bundles 12 separate from the precipitation bath liquid flows 14. The line 16 opens into a calming chamber 18 (not shown) partially filled with packing elements, from which the precipitation bath liquid flows through the openings 19 into the actual container 1. From Figure 3 it can be seen that the thread guide elements 11 are arranged in a row in the bottom 10 and the thread bundles 12 run parallel to one another parallel to the take-off godet (not shown). The precipitation bath container 1 has two overflows 9 which are vertically adjustable and thus determine the precipitation bath level and the width of the gap a. A nozzle tube 20 with a slot 21 extending over the row of nozzles 6 or the row of capillary sheets 26 is attached to the overflows 9 by means of the holder 23. A weak air flow is applied to the nozzle tube 20 on both sides via the line 24, which can be adjusted via a needle valve (not shown). The air stream 25 leaves the slot 21 (outlet opening 150 mm x 1 mm) linearly over the entire width and inclined to the bath surface 7, so that the capillary sheets come into contact with the air stream immediately before they enter the precipitation bath. The slot nozzle is about 10 mm above the surface of the precipitation bath.

It was found that using the device according to FIGS. 2 and 3, but initially without air blowing the capillary sheets by means 20, 21 in the direction of the immersion point of the capillaries in the spin bath, and using four monofilament nozzles, i.e. four cone nozzles (0 = 12.5 mm), each with only one bore with a diameter of 200 μm, the width of the gap a during spinning can be changed continuously between 10 and 300 mm, without any spinning disturbances being observed. The spinning apparatus did not allow a gap width a> 300 mm. The experiments were carried out with a 12% by mass cellulose solution in aqueous N-methylmorpholine-N-oxide (NMM0), the relaxation time spectrum of which is shown in FIG. 1 and whose λ was 3.0 s. For the determination of the relaxation time from the rheological data of the cellulose solution, reference is made to Ch. Michels, Das Papier, (1998) 1, pp. 3-8. The take-off speed was 100 m / min. Increasing the take-off speed to 300 m / min led to the same result. If you replace the cone nozzles with those with 30 bores each with a diameter of 140 µm, the maximum undisturbed gap a decreases to approx. 40 or 60 µm.

With the same arrangement, but with linear, sheet-like blowing of the capillary sheets shortly before entering the precipitation bath, a clear The increase in the maximum possible gap width a from about 40 to 65 mm or from about 60 to 100 mm can be determined. In addition to the increase in the maximum possible air gap, a significant calming of the capillary run when entering the precipitation bath can be observed. The frequency of capillary contact becomes significantly lower, and with it the likelihood of spinning disorders occurring.

When using nozzles with a nozzle hole diameter of 90 μm, the maximum operationally adjustable gap width a increases, and when using nozzles with a diameter of 200 μm, this gap width decreases. At the transition to cone nozzles (0 = 20 mm) with the same number of holes, i.e. decreasing capillary density, an increase in the maximum adjustable gap can be observed. With 30 holes per nozzle, the capillary

_2 density of the small cone nozzle N = 47 cm and that of the large cone nozzle

-2 -2

15 cm. With the capillary density of 15 cm, but otherwise the same conditions, the maximum possible gap width increases again from approx. 65 to 90 mm or from 95 to 130 mm. These changes can be adequately described by the modified equation Ha mentioned above. With the aid of the method according to the invention and the spinning device, the capillary density can therefore be increased without increasing the risk of spinning disturbances occurring. The empirical relationship purple then applies to the distance between two adjacent nozzle holes.

Closer investigations of the linear sheet-like blowing shortly before the capillary sheets enter the precipitation bath make it clear that the largely laminar flow of air in the direction of the capillary run is clearly disturbed. The transition at the capillary / gas or air and capillary / precipitation bath interfaces changes. The movement of the surface of the spinning bath when immersing the capillaries appears to be quieter. The spinning disturbances, which begin almost exclusively in the mutual contact of the capillaries when entering the spinning bath, are therefore much less likely. The invention is illustrated by the following example.

example

A press-moist mixture (dry content 50.2%) consisting of 188 g spruce sulfite pulp (Cuoxam-DP 480), 10 g cotton linters pulp (Cuoxam-DP 1907) and 0.4 g stabilizer is in 1850 g NMM0 ( Dry content 75%) dispersed, introduced into a kneader with a vertical kneader shaft, 1255 g of water were distilled off under vacuum and shear at a temperature of 90 ° C. and by further “shear stirring” into a microscopically homogeneous cellulose solution of the composition 11.0% cellulose, 77, 1% NMM0 and 11.9% water transferred. The relaxation time at a spinning temperature of 85 ° C was 3.0 s, the zero shear viscosity was 3450 Pa-s. The solution is formed into threads in a piston spinning apparatus, the hot water-heated spinneret holder of which can accommodate either four spinner cones with 12.5 mm (30 mm pitch from nozzle center to nozzle center) or 3 spinning cones with 20.0 mm diameter (40 mm pitch). The spinning box according to FIGS. 2 and 3 is located below the spinning part.

For each test, the maximum gap width a was without and inventive ^J max-making in accordance with established incident air flow. After spinning, the filaments were wound up, washed, cut into stacks of 50 mm, finished and dried. They were then subjected to the textile test. The results are shown in Tables 1 and 2. Air was applied in the manner described above with reference to FIGS. 2 and 3. The nozzle outlet opening was 150 mm x 1 mm. The capillaries were contacted with the air stream immediately before entering the precipitation bath. The air nozzle was slanted downward. The slot nozzle was approx. 10 mm above the surface of the precipitation bath.

From the tables it is seen that the quenching is possible by a fixed ^¬ Liche widening of the air gap A, namely by at least 50% to 200% maxi ^¬ times occur without interference with the spinning operation.

This leads to a significant improvement in the elongation at break, dry, and Looping tear force goes hand in hand.

Table 1

Table 2

Take-off speed of only 100 m / min

Claims

claims

1. A process for the production of cellulose fibers or filaments from cellulose by the dry-wet extrusion process with aqueous amine oxides, in particular N-methylmorpholine-N-oxide as the solvent, in which a) cellulose or a cellulose mixture with a Cuoxam-DP in the range of 250 to 3000 dispersed in aqueous amine oxide, b) the dispersion obtained at elevated temperature with dehydration and shear in a homogeneous solution with a zero shear viscosity in the range from 600 to 6000 Pa * s and with a relaxation time in the range from 0.3 to 50 s, in each case at 85 ° C., c) the solution is fed to at least one spinneret and previously passed through one of the flow chambers common to the nozzle (s), in which their residence time is at least equal to their relaxation time at the spinning temperature, d) the Solution in each spinneret is deformed into at least one capillary and the capillary (s) of each nozzle is distorted by a non-precipitating M edium and then with precipitation of the cellulose threads through a precipitation bath, and e) separating the cellulose threads at the end of the precipitation bath section by deflection from the precipitation streams and pulling off the threads, characterized in that in step d) the capillary sheet (s) are briefly before flows into the precipitation bath with a gas at an angle << • to the direction of the capillary flow in the range 45 ° < ^D <^" 90 °.

2. Process for the production of cellulose fibers or filaments from cellulose by the dry-wet extrusion process with aqueous amine oxides, in particular N-methylmorpholine-N-oxide as solvent, in which a) pulp or a pulp mixture with a Cuoxam-DP dispersed in the range from 250 to 3000 in aqueous amine oxide, b) the dispersion obtained at elevated temperature with dehydration and shear in a homogeneous solution with a zero shear viscosity in the range from 600 to 6000 Pa -s and with a relaxation time in the range from 0.3 to 50 s, in each case at 85 ° C., c) the solution is fed to at least one spinneret and previously passed through a flow chamber common to the nozzle (s), in whose residence time is at least equal to their relaxation time at the spinning temperature, d) the solution in each spinneret is deformed to form at least one capillary and the capillary (s) of each nozzle is distorted by a non-precipitating medium and then leads to a precipitation bath with the cellulose filament precipitating , and e) separating the cellulose threads at the end of the precipitation bath section by deflection from the precipitation streams and withdrawing the threads, therefore ch characterized in that in step d) the capillary sheets are flown with a gas immediately before they enter the precipitation bath, the gas stream and the precipitation bath having rectified flow components at the interface with the gas gap.

3. The method according to claim 1 or 2, characterized in that one flows against the capillary sheets with a flat, flat gas stream extending over the entire width of the capillary sheets.

4. The device for producing cellulose fibers or filaments from pulp by the dry-wet extrusion process with aqueous amine oxides as solvents, with a spinning package with a spinneret plate, spinning nozzles and arranged above the spinneret plate and the spinneret, mean ^¬ seed inflow chamber, the volume of the relationship vs≥ v _τ y

L m is sufficient, where V is the volume of the inflow chamber in cm3, v _{τ is} the volume flow of the cellulose solution in cm 3 / s and λm is the relaxation time on

Maximum frequencies of the relaxation spectrum of the spinning solution mean a precipitation bath in two containers connected by a precipitation bath pump, a gap a between the spinnerets (6) and the precipitation bath surface (7) in the upper of the two containers, and a take-off godet, characterized in that in the gap a at least one slot die is arranged with a nozzle slot (21) directed at an angle <X to the direction of the capillary running in the region 45 ^{0 <} c (. <90 ⁰ ) for the flow against the capillaries (26) before they enter the precipitation bath.

5. The device according to claim 4, characterized in that the upper bath tank (1) on the one hand the capillary sheets (26) has at least one inlet opening (19) and on the other hand the capillary sheets has at least one overflow (9) and the slot die with respect to the row of capillary sheets (26) is arranged on the same side as the inlet opening (s) (19).

6. The device according to claim 4 or 5, characterized in that the slot die is mechanically connected to at least one overflow (9).

7. Device according to one of claims 4 to 6, characterized in that the width of the gap a and the relaxation time of the spinning solution the relationship

in which a the gap width in mm, 1 ^ the relaxation time am

Frequency maximum of the relaxation spectrum of the spinning solution, the withdrawal speed v in mm mean capillary density in cm -2 and D ^a nd the nozzle hole diameter in m / min, N.

8. Device according to one of claims 4 to 7, characterized in that the dimensions of the spinnerets (6), the gap width a and the precipitation bath section w of the relationship

suffice in which x is the distance between two neighboring nozzle holes, a is the air gap width, w is the length of the precipitation bath section and D is the nozzle hole diameter.