Plant and method for making continuous elastic yarns made of silicone material and continuous elastic yarn made of silicone material thus obtained

Abstract

A plant and method for making continuous yarns made of silicone material comprises at least an extrusion station, into which the material is introduced in an amorphous condition, and extrusion means which cause the material to exit from the extrusion station along an extrusion axis. The plant also comprises a vulcanization station, located downstream of the extrusion station, at a determinate distance therefrom, in which the continuous yarn is vulcanized in a direction of treatment. The plant also comprises a drawing unit, disposed downstream of the vulcanization station.

Claims

1. A method for making continuous elastic yarns of silicone material, comprising at least an extrusion step, wherein by means of an extrusion station comprising an extrusion body said material is made to exit along an extrusion axis, with a conditioned shaping, and at least a vulcanization station step carried out in a vulcanization oven disposed downstream of said extrusion body, wherein: in said extrusion step, said extrusion means confer on the extrusion axis a substantially vertical direction, in a segment between an exit from the extrusion body and an entrance into the vulcanization oven, that is variable between 400 and 1500 mm according to the final thickness of the elastic yarn to be obtained, the elastic yarn is subjected to a drawing action performed by a drawing unit disposed downstream of said vulcanization oven, in which a drawing ratio conferred on the elastic yarn before entering the vulcanization oven is comprised in a value between 2 and 6 (100-500%), reducing the section of the elastic yarn proportionally, before the elastic yarn enters said vulcanization oven, and in which the elastic yarn has a final thickness of less than 0.7 mm and has a desired orientation of the molecular chains, and wherein the vulcanization oven is selectively moved with respect to said extrusion station so as to vary said distance at least according to a desired value of final thickness to be conferred on the elastic yarn.

2. The method as in claim 1, wherein, in said vulcanization station, said extruded product is vulcanized along a processing direction parallel or coincident to the extrusion axis.

3. The method as in claim 1, wherein a collection unit is provided downstream of the vulcanization station to collect an extruded product, the collection unit comprising said drawing unit.

4. The method as in claim 1, further providing a controlled cooling of the yarn in a cooling station located downstream of the vulcanization station and upstream of the collection unit.

5. The method as in claim 1, further providing a heating and cooling step for heat regulation of the extrusion station.

Description

BRIEF DESCRIPTION OF THE SEVERAL VIEWS OF THE DRAWINGS

(1) These and other characteristics of the present invention will become apparent from the following description of a preferential form of embodiment, given as a non-restrictive example with reference to the attached drawing wherein:

(2) FIG. 1 is a lateral schematic view of a plant for making elastic yarns made of silicone material according to the present invention.

DETAILED DESCRIPTION OF THE INVENTION

(3) With reference to the attached drawing, a plant 10 according to the present invention is used to make extruded products of silicone material, in this case continuous elastic yarns 30, with a thickness of less than 0.7 mm, advantageously 0.3-0.4 mm, as little as 0.1 mm, of silicone rubber.

(4) The plant 10 comprises feed means 11, an extrusion station 12, a vulcanization station 16, a cooling station 17 and a drawing unit and collection 26 of the yarn 30.

(5) The feed means 11 feed the extrusion station 12 and are automatic.

(6) In this case, the feed means 11 comprise a hopper 22, dosing pumps, able to introduce into the hopper 22 the correct quantity of material according to the capacity of the plant, and static and dynamic mixers, able to mix the material so as to prevent the formation of air bubbles.

(7) The feed means 11 also provide a device able to keep the level of material inside the hopper 22 constant, so as to also keep constant the exit pressure of the material from the hopper 22.

(8) According to a variant, in the case of material in the form of paste, the feed means 11 comprise a roller or a pair of rollers cooperating with each other, which feed the material in the form of a strip.

(9) According to another variant, in the case of a continuous strip of material, the feed means 11 comprise a conveyor belt on which the strip is disposed.

(10) The extrusion station 12 comprises an extrusion body 31 and extrusion means 15.

(11) The extrusion body 31 is provided with compression means 13, dosing means 14 and a device 25 to distribute the material.

(12) The compression means 13 compress the material and thrust it toward the dosing means 14. In this case, the compression means 13 comprise a worm screw, sized according to the capacity of the plant 10, and a degassing zone, to eliminate the possible formation of air bubbles.

(13) According to a variant, the compression means 13 provide a piston device.

(14) The dosing means 14 are able to dose the material compressed by the compression means 13 so as to feed the device 25 to distribute the material in a uniform and continuous manner.

(15) In this case, the dosing means 14 comprise a dosing pump with gears and a plurality of pressure transducers, coordinated with the compression means 13.

(16) The transducers detect the pressure at entrance and at exit to/from the dosing means 14 and, according to this detection, send a signal to the compression means 13 to regulate the speed of the material and to keep a constant delivery through the dosing means 14.

(17) The device 25 to distribute the material feeds the extrusion means 15 uniformly. In this case, the extrusion body 31 has a vertical elbow-type conformation. The material enters the extrusion body 31 in a horizontal direction of feed, due to the effect of the pressure exerted by the compression means 13, and exits from the extrusion means 15 along an axis of extrusion D, with a substantially vertical direction, due to the effect of said pressure and the force of gravity.

(18) According to the conformation of the draw-plate, the yarn 30 obtained at exit from the extrusion means 15 can have a variable number of beads or filaments, for example comprised between 2 and 30.

(19) The draw-plate comprises corresponding perforations having a lead-in to facilitate the entry of the material and a bevel at exit to facilitate the detachment of the material.

(20) According to a variant, the extrusion body 31 has a horizontal conformation.

(21) According to a variant, the extrusion body 31 has a vertical conformation.

(22) According to a variant, upstream of the draw-plate the extrusion means 15 comprise at least a filter and at least a pre-drawing plate, advantageously two filters and two pre-drawing plates. This is particularly advantageous to prevent obstruction of the perforations of the draw-plate and to distribute the material better, in the case where the extrusion means 15 include a draw-plate each, equipped with a plurality of perforations for the simultaneous production of a corresponding plurality of elastic yarns.

(23) The presence of the filters upstream of the draw-plate is extremely important so as to be able to break the memory effect that the extrusion screw imparts to the material. The filters are chosen of a size such as to prevent the yarn, descending vertically, from twisting, knocking and from preventing the spinning.

(24) The extrusion station 12 also comprises a heating and cooling device 24 for the automatic heat-regulation of the various zones of the extrusion station 12, so as to keep the ideal conditions of extrusion temperature and pressure.

(25) The elastic yarn 30 exiting from the draw-plate advances vertically, drawn by the drawing and collection 26 unit. In this case, the collection unit 26 comprises drawing means 18, such as a motorized roller, which exert a predetermined drawing force on the extruded product 30 and guarantee that the extruded product 30 advances toward the vulcanization station 16, maintaining a substantially vertical direction, without horizontal displacements.

(26) Furthermore, as a consequence of the drawing force of the drawing means 18, the section of the continuous yarn 30 is reduced to the desired size, with a drawing factor that can vary, according to needs, from 2 to 6, in this way reducing the section of the elastic yarn 30 proportionally, yet keeping the quality and uniformity of the section shape high, and orienting the molecular chains in a more regular way.

(27) The vulcanization station 16 comprises a zonal oven 27, each zone being characterized by a heating system: high temperature, ultraviolet rays, or microwaves.

(28) Inside the oven 27, the elastic yarn 30 is treated in a direction of treatment T, substantially vertical and parallel to the axis of exit D of the yarn from the extrusion station 12.

(29) The oven 27 is selectively movable vertically, with known mechanical or pneumatic devices, to be positioned at different distances L from the draw-plate according to the type of elastic yarn 30 and the relative crystallization and vulcanization times thereof.

(30) In particular, the variation in the distance L between the exit from the extrusion station 15 and entry into the vulcanization oven 27 allows to vary the drawing conditions on the continuous yarn 30 according to the section to be obtained, both in the shape and thickness and also in orientation of the molecular chains, apart from, obviously the type of yarn 30 itself.

(31) In the case of continuous elastic yarns 30 according to the invention, the distance L typically varies between 400 and 1500 mm, in particular according to the final thickness of the elastic yarn 30 to be obtained.

(32) The vulcanization oven 27 is heat-adjustable so as to vary the vulcanization temperature according to the type of elastic yarn 30 treated.

(33) The cooling station 17, located downstream of the vulcanization station 16, is able to cool the elastic yarn 30 to a temperature near the environmental temperature so as to prevent the final product from continuing the crystallization process after collection and storage.

(34) The cooling station 17 is heat-regulated so as to guarantee that ideal cooling temperature conditions are maintained, according to the type of elastic yarn 30.

(35) The collection unit also comprises, apart from the afore mentioned drawing means 18, surface treatment means 19, control means 20 and collection means 21, of a known type.

(36) The surface treatment means 19 are able to treat the external surface of the extruded product 30 in order to confer upon it determinate physical characteristics.

(37) The control means 20 of the extruded product 30 comprise a roller associated with control devices and are able to control the physical characteristics of the extruded product 30, such as the thickness, uniformity of section, elasticity and others.

(38) The collection means 21 are able to collect and pack the elastic yarn 30 for storage. The collection means 21 comprise an automatic reel-winder or a device to cut the elastic yarn 30 and insert it into containers.

(39) It is clear, however, that modifications and/or additions of parts may be made to the 10 as described heretofore, without departing from the field and scope of the present invention.