The present invention relates to machines for the production of nonwovens, comprising one or more spun-bond towers and optionally one or more melt-blown heads depositing filaments and optionally fibres as a web onto a conveyor. The web thus deposited, and still fragile, is then sent to a water-jet consolidation station.
One drawback of these machines is that the web that emerges therefrom cannot be sent continuously to a product application unit.
The invention remedies this drawback.
The subject of the invention is therefore a machine for the continuous production of a nonwoven, comprising a spun-bond tower depositing filaments as a web onto a conveyor and a device for consolidating the web, characterized by a moisture-expressing means downstream, in the direction in which the web moves, of the consolidation device and by an applicator for applying a product to the web downstream of the expressing means.
According to one embodiment, the expressing means consists simply of a second conveyor over which the web passes, a vacuum device being provided between the upper and lower runs of said second conveyor, said device giving for example a vacuum of between 40 and 700 millibar and subjecting the web to a suction effect.
Thanks to this, it is now possible to make webs consisting of hydrophobic filaments, for example made of polypropylene, polyethylene or metallocene, to continuously undergo a subsequent treatment with a surfactant and/or a binder and/or a lubricant and/or a swelling agent and/or a dye, or a continuous printing operation, the expressing of the moisture being sufficient for the product applied by the applicator to be correctly applied to the web even if the latter consists of hydrophobic filaments.
The upper run of the second conveyor is given a length such that, depending on the speed with which the web passes, the moisture content of the web becomes less than 70% by weight, better still less than 50% and even better less than 20% upon exiting the second conveyor. This moisture content is in general between 10% and 70% by weight. Unlike what a drying unit would give, it is greater than 10%. In general, the residence time of the web on the second conveyor may be less than 2 seconds for a conveyor whose upper run has a length of for example 2m.
The machine may include, downstream of the product applicator, a device for drying the web, this drying device possibly being made less substantial by the fact that a good part of the moisture has already been expressed in the expressing means.
The product applicator is preferably a foam applicator or a lick-roll applicator or a spray applicator, these accommodating a residual moisture content of the web.
Preferably, for hygiene products, especially for nappies, the application takes place in longitudinal bands, thereby creating, for example, an alternation of hydrophilic and hydrophobic longitudinal regions.
In Patent Application EP-0 072 961 it is provided not to express the moisture from a nonwoven web, that is to say to expel some of the water by a mechanical means, but to dry a nonwoven web, that is to say to eliminate almost all of the water therefrom by a supply thermal energy.
The single FIGURE of the appended drawing illustrates the invention.
The FIGURE is a schematic sectional representation of a machine according to the invention.
It comprises a spun-bond tower having an extruder for extruding an organic polymer melt that feeds adie1 for producing a curtain of filaments F, acooling zone2 for solidifying the extruded filaments, at least on the surface, asuction device3 in the form of a chamber in which the curtain of filaments is subjected to the action of high-velocity streams of air that draw the filaments, and a diffuser4 allowing, at the exit of the suction device, the stream of air to be deflected and slowed down and the filaments F to be distributed in a random fashion as a web, which is deposited on theupper run5 of an endlessfirst conveyor6. The filaments are in the form of a bundle of filaments F, lying perpendicular to the plane of the FIGURE.
Mounted above theupper run5 is a horizontal drum7 with an internal vacuum device shown symbolically by the letter A. The lateral surface of the drum7 is perforated. The drum is rotated about its axis. The drum is surrounded by an apertured sleeve. Twoinjectors8 project pressurized water jets onto the lateral face of the drum, it being possible for the web of filaments to pass between the drum7 and theinjectors8 and thus to be consolidated. The jets may have a diameter of between 80 and 170 microns. The number of jets per metre may be between 1000 and 5000 and the water pressure in the injectors may be between 10 and 400 bar, while the vacuum in the drum7 may be betweenminus 20 millibar and minus 200 millibar, and the drum7 may be driven at a speed of between 1 and 400 m/min. The web then passes onto the upper run9 of asecond conveyor10 in order to reach asecond drum11 of the same structure and same operation as the drum7. From thedrum11, the web passes onto adrum12 provided, like thedrum11, with injectors. Thedrum12 is similar to thedrum11 in its structure and in its operation.
On leaving thedrum12, the web is sent directly to athird conveyor15 provided with a moisture-expressingdevice16, namely a box in which a 600-millibar vacuum is created, said box being interposed between the upper run and the lower run of thethird conveyor15. The upper face of the box has a slit extending transversely, facing the entire web passing over the conveyor and via which the moisture is sucked out therefrom. The upper run has a length of 3 m. The web passes along this at a speed of 200 m per minute.
Downstream of this conveyor is an applicator17 for applying an ennobling product, which comprises an actualproduct application station18, adrying station19 and a wind-upstation20.
A ready-to-use nonwoven is thus continuously obtained.