阅读说明：本技术 用于弹性体配混物的共挤出设备，以及用于制造成型元件条带的方法 (Co-extrusion device for elastomeric compounds, and method for manufacturing profiled element strips ) 是由 C·乌吉耶 H·欣茨 N·若内 A·勒托卡尔 于 2019-09-17 设计创作，主要内容包括：本发明涉及一种通过共挤出制造基于多个由弹性体配混物制成的挤出条带的成型元件条带(100)的设备(1),所述设备(1)包括具有流动管道(2a、2b、2c、2d)的挤出头(2),所述挤出头(2)的入口孔连接至至少两个挤出机(10、20、30、40)的出口,以供给由弹性体配混物制成的挤出条带,所述挤出头(2)的出口孔通向与辊(50)相邻的模头(3),该模头(3)被设计为与辊(50)配合以使成型元件条带(100)成形,所述辊(50)具有由外表面(52)包围的中心轴线和用于驱动辊围绕其中心轴线旋转的装置,所述外表面(52)用于接收成型元件条带(100)。根据本发明,流动管道(2a、2b、2c、2d)相互平行并垂直于辊(50)的周向方向,并且成型元件条带(100)沿至少700mm的等效长度接合至辊的接收表面。(The invention relates to a device (1) for producing a profiled element strip (100) by means of coextrusion, said strip being based on a plurality of extruded strips made of an elastomeric compound, the device (1) comprises an extrusion head (2) with flow conduits (2a, 2b, 2c, 2d), the inlet orifice of the extrusion head (2) is connected to the outlets of at least two extruders (10, 20, 30, 40), to feed an extruded strip made of elastomeric compound, the outlet orifice of the extrusion head (2) opening into a die (3) adjacent to a roller (50), the die (3) is designed to cooperate with a roller (50) to shape the profiled element strip (100), the roller (50) has a central axis surrounded by an outer surface (52) and means for driving the roller in rotation about its central axis, the outer surface (52) being for receiving a profiled element strip (100). According to the invention, the flow ducts (2a, 2b, 2c, 2d) are mutually parallel and perpendicular to the circumferential direction of the roll (50), and the profiled element strip (100) is joined to the receiving surface of the roll along an equivalent length of at least 700 mm.)

1. Apparatus (1) for manufacturing, by coextrusion, a profiled element strip (100) based on a plurality of extruded strips made of elastomeric compound, said apparatus (1) comprising an extrusion head (2) having flow ducts (2a, 2b, 2c, 2d), the inlet orifices of said extrusion head (2) being connected to the outlets of at least two extruders (10, 20, 30, 40) to supply extruded strips made of elastomeric compound, the outlet orifices of said extrusion head (2) opening into a die (3) adjacent to a roller (50), which die (3) is designed to cooperate with a roller (50) to shape the profiled element strip (100), said roller (50) having a central axis surrounded by an outer surface (52) for receiving the profiled element strip (100) and means for driving the roller in rotation about its central axis, characterized in that, the flow ducts (2a, 2b, 2c, 2d) are mutually parallel and perpendicular to the circumferential direction of the roll (50), and the profiled element strip (100) is joined to the receiving surface of the roll along an equivalent length of at least 700 mm.

2. The apparatus according to claim 1, characterized in that the outer surface (52) of the roller (50) is a cylinder with a diameter greater than or equal to 0.6 m.

3. An apparatus according to any one of the preceding claims, characterized in that it comprises a first cooling system for the outer surface (52) of the roll (50) and a second cooling system for the support bearings of the roll (50), the first and second cooling systems being connected to a control unit which controls the operation of both cooling systems according to the same set temperature.

4. The apparatus according to any of the preceding claims, characterized in that the profiled element strip (100) is brought into engagement with the outer surface (52) of the roll (50) along a distance at least equal to 1/2 circumferences, preferably 3/4 circumferences, of the roll (50) before the profiled element strip (100) is transferred to the conveying device.

5. The apparatus according to any of the preceding claims, wherein the roller (50) is arranged above the extrusion head (2).

6. The apparatus according to any one of claims 1 to 4, characterized in that the roller (50) is arranged below the extrusion head (2).

7. Apparatus according to claim 6, characterized in that it comprises direction-changing rollers (71, 72) interposed between the rollers and the conveying means for the profiled element strip.

8. The apparatus according to any one of claims 1 to 3, characterized in that a roller (50) drives an endless belt (80) interposed between the die head (3) and the roller, so that the die head (3) cooperates with the roller (50) to shape the strip of profiled elements through the belt.

9. Device according to claim 8, characterized in that the belt (80) is made of metal, preferably stainless steel.

10. Method for manufacturing profiled element strips (100) based on a plurality of elastomeric compounds by coextrusion using an apparatus comprising a plurality of extruders (10, 20, 30, 40), an extrusion head (2) and a roller (50) according to any one of the preceding claims, characterized in that:

-co-extruding the profiled element strips using an extrusion head, wherein the flow conduits (2a, 2b, 2c, 2d) of the extrusion head (2) are parallel to each other and perpendicular to the circumferential direction of the roller (50), and the profiled element strips are joined to the receiving surface of the roller along an equivalent length of at least 700 mm;

-then transferring the resulting profiled element strip by means of a transfer device.

Technical Field

The present invention relates to the field of the production of strips of coextruded viscoelastic products, such as elastomeric products for the manufacture of tyres. More particularly, the invention relates to the manufacture of co-extruded composite profiled elements based on elastomeric compounds and used for manufacturing tire treads or sidewalls.

Background

In a known manner, in the manufacture of composite profiles by extrusion (for example, by co-extrusion) of at least two strip-like products based on elastomeric compounds, a plurality of extruders is connected to a common extrusion head. Each extruder is formed by a fixed cylindrical body or barrel and has, inside the extruder, a screw coaxial with the longitudinal axis of the barrel and driven in rotation about this axis. The purpose of the screw is to homogenize the rubber mixture introduced into the extruder in the form of a strip and to drive the rubber mixture towards the outlet die. For composite products, the outlet die receives several elastomeric compounds of the same or different composition and determines the profile of the coextruded profiled element strip. The profile is defined by stationary profiled blades cooperating with rotating rollers or stationary walls.

Nowadays, there is an increasing demand for composite products of the type using composite profiled element strips, made of different individual profiles, extruded or superposed, to reduce the number of successive laying operations of the product during assembly, thus reducing costs and improving the quality of the final product. These composite products are preferably obtained by coextrusion, since this method provides better mutual bonding between the various components.

Co-extrusion allows combining multiple extruded strips of elastomeric compound into a single co-extruded product in a single co-extrusion apparatus. The multiple extruders are arranged together around a common extrusion head that includes a product flow conduit toward an exit die. In the coextrusion apparatuses of the prior art, the extruders used are arranged as "bellows", or in other words, so that the axes of rotation of their extrusion screws converge towards the extrusion head. This convergent arrangement causes higher stresses in the compound strip passing through the transfer pipe of the extrusion head. Due to the viscoelastic properties of the elastomer, after this convergent region of the transfer duct, there appear distinct contraction (in the longitudinal direction of the strip) and expansion (in the transverse direction of the strip). Thus, the coextruded profiled element strip may deform in both transverse directions after exiting the die and may thicken and narrow simultaneously, or vice versa.

To solve this problem, document US 6695606 proposes a solution that includes the use of a rotating roller close to the outlet die of the extrusion head. The rotating rolls participate in the flow of the composite product obtained after the exit from the die by reducing internal stresses that partially relax while the composite product remains attached to the rolls. These stresses are mainly elongation stresses due to the reduced cross-section of the pipe of the extrusion head. According to this document, the flow conduit is dimensioned such that the cross-section of the conduit can be gradually changed with the flow of the material. However, in addition to the complexity of the cross-sectional shape and the size of these tubes, there are problems with residual stresses in the coextruded composite product due to the convergence of the tubes in the extrusion head.

Document WO2018115797 in the name of the applicant describes a coextrusion device comprising a plurality of extruders arranged on both sides of an extrusion head. The extrusion head comprises mutually parallel transfer ducts leading to an outlet die. The solution proposed in this document can therefore solve the problem of elongation stresses caused by the "bellows" arrangement of the extruder of the plant. However, it has been found that expansion stresses are still present in the product obtained at the die exit.

For the production of tyres, it is necessary to use coextruded products having very precise geometries, with the aim of optimizing their properties.

The object of the present invention is to overcome said drawbacks.

Disclosure of Invention

The invention proposes an apparatus for manufacturing, by co-extrusion, a profiled element strip based on a plurality of extruded strips of elastomeric compound, said apparatus comprising an extrusion head having flow ducts, the inlet orifices of which are connected to the outlets of at least two extruders to supply extruded strips of elastomeric compound, and the outlet orifices of which open into a die adjacent to a roller designed to cooperate with the roller for shaping the profiled element strip, said roller having a central axis surrounded by an outer surface for receiving the profiled element strip and means for driving the roller in rotation about its central axis, characterized in that the flow ducts are parallel to each other and perpendicular to the circumferential direction of the roller, and in that the profiled element strip is joined to the receiving surface of the roller along an equivalent length of at least 700 mm.

The "radial" direction is the direction along the radius of the roll. The "axial" direction is a direction parallel to the axis of rotation of the roll. The "circumferential" direction is the direction perpendicular to both the radius of the roll and the axial direction.

According to the invention, the different strips of elastomeric compound are extruded through an extrusion head common to the flow ducts parallel to each other, using a roller die, also called "roller head". The die is adjacent to the roller and is designed to cooperate with the roller to form the strip of profiled elements. It will be appreciated that the die is disposed adjacent the outer surface of the roll and that the roll-facing surface of the die comprises a cylindrical surface which closely follows the contour of the roll surface. To this end, the cylindrical surface of the die comprises forming holes communicating with the flow ducts of the extrusion head, the function of which is to shape the different strips coming from the different ducts and to guide them as they are applied to the roller, so as to form a single strip of coextruded profiled elements through the cylindrical surface of the roller.

More particularly, the flow conduits supplying the mixture to the outlet die and hence to the roller are parallel and perpendicular to the circumferential direction of the roller. These ducts are not arranged converging towards the rolls as in the prior art documents, and therefore the stresses applied to the compound, mainly due to the holes passing through the outlet die, are low. Such extrusion through a roller head can inhibit two dimensions (length and width) of a coextruded profiled element strip, the bottom of which is attached to a receiving surface of the roller head. The third dimension (thickness) of the strip remains unchanged due to the principle of volume conservation. To better relax residual stresses, the coextruded profiled element strip must be held at a predetermined length on a roll. A length of at least 700mm is considered sufficient to relax the stress during laboratory testing with the tire tread and sidewalls. Thus, a coextruded profiled element strip with a very precise geometry is obtained.

Equivalent length refers to the contact distance between the coextruded profiled element strip exiting the die and the receiving surface of the roll. The receiving surface of the roller refers to the portion of the roller that is in contact with the coextruded profiled element strip, which is the outer surface of the roller when in direct contact with the profiled element strip, or the outer surface of the belt driven by the roller and interposed between the outer surface of the roller and the coextruded profiled element strip.

In a first embodiment of the invention, the roller is a cylinder with a diameter greater than or equal to 0.6 m.

Preferably, the apparatus comprises a first cooling system for the outer surface of the roll, and a second cooling system for the support bearings of the roll, said first and second cooling systems being connected to a control unit, said control unit controlling the operation of both cooling systems according to the same set temperature.

In a second embodiment, the profiled element strip is engaged with the receiving surface along a distance at least equal to 1/2 and preferably 3/4 revolutions of the roller prior to transferring the profiled element strip to the conveyor.

In a variant embodiment of the invention, the roller is arranged above the extrusion head.

In a variant embodiment of the invention, the roller is arranged below the extrusion head.

Preferably, the apparatus comprises a direction-changing roller interposed between the roller and the conveying device for the profiled element strip.

In a third embodiment, a roller drives an endless belt interposed between a die and the roller such that the die cooperates with the roller to form a strip of profiled elements through the belt.

Preferably, the band is made of metal, and preferably stainless steel.

The object of the invention is also achieved by a method for manufacturing a profiled element strip based on a plurality of elastomeric compounds by coextrusion using an apparatus according to the invention comprising a plurality of extruders, an extrusion head and a lay-up roller, characterized in that:

-co-extruding the profiled element strips using an extrusion head in which the flow conduits are parallel to each other and perpendicular to the circumferential direction of the laying roller, and the profiled element strips are joined to the receiving surface of the roller along an equivalent length of at least 700 mm;

-then transferring the resulting profiled element strip by means of a transfer device.

Drawings

The invention will be better understood by the remainder of the description on the basis of the following drawings:

figure 1 is a schematic cross-sectional view of the apparatus of the invention according to a first and a second embodiment;

figure 2 is a schematic cross-sectional view of a device according to a first embodiment;

figure 3 is a schematic cross-sectional view of a device according to a variant of the second embodiment;

figure 4 is a schematic cross-sectional view of a device according to a third embodiment.

In the various figures, identical or similar elements are provided with the same reference signs. Therefore, the description thereof will not be systematically repeated.

Detailed Description

The figures show a co-extrusion apparatus 1 for extruding a viscoelastic material of the elastomeric compound type to form a strip 100 of composite profiled elements, such as a tire tread or sidewall. The coextrusion device 1 comprises an extrusion head 2 connected to a plurality of extruders 10, 20, 30 and 40, each providing the extrusion head with a pressurized elastomeric compound. The pressurized elastomeric compound follows a flow conduit which passes through the extrusion head up to the outlet die 3.

The extruders 10, 20, 30, 40 have been schematically illustrated, depicting only their respective screws, but it will be understood that, in a generally known manner, the screw of each extruder rotates within a cylindrical barrel equipped with an inlet for supplying the elastomeric compound in the form of a strip of compound and an outlet which, when the extrusion head 2 is mounted in position, leads to the extrusion head 2. The screw 12, 22, 32, 42 of each extruder 10, 20, 30, 40 is driven to rotate about its longitudinal axis 11, 21, 31, 41 by a motor, located at the opposite end of the screw with respect to the screw, near the end of the extrusion head, so as to rotate the screw within the respective barrel, in order to supply the extrusion head 2 with the elastomeric compound that has been homogenized and is ready to be shaped by the head.

The extruders 10, 20, 30, 40 are arranged on both sides of the extrusion head 2, and so that the outlet of each extruder is in direct communication with an inlet conduit that conveys the compound to the extrusion head 2. In other words, extrusion head 2 is directly connected to extruders 10, 20, 30, 40 without any transfer duct of the elastomer-compound between the two. The extrusion head 2 aggregates all the size tools specific to a given profiled element (transfer ducts connecting them to the extruder and to the outlet of the extrusion die) into a single integral assembly, which is mounted so as to be removable. In the event of a change in the molded component product, such an integral component would be quickly removed and replaced with another component suitable for the new product.

The compound reaches the inlet orifices 15, 25, 35, 45 in the extrusion head 2, said extrusion head 2 also comprising flow ducts 2a, 2b, 2c, 2d, ensuring the transfer of the compound from the different extruders to the outlet die 3. The flow conduits 2a, 2b, 2c and 2d extend in a direction substantially perpendicular to the longitudinal axis of the extruders 10, 20, 30, 40. Substantially perpendicular means at an angle of 90 +/-20.

In a variant of the invention, the extruders 10, 20, 30, 40 are arranged with their longitudinal axes 11, 21, 31, 41 parallel to each other and perpendicular to the plane of the opposite face of the extrusion head forming the interface plane.

The coextrusion device 1 also comprises a roller 50 cooperating with the die 3. The roller 50 has a cylindrical outer surface 52 and is mounted for rotation about an axis of rotation passing through its cross-sectional centre of symmetry O. A motor (not shown in the drawings) is provided to drive the roller 50 to rotate at a predetermined speed via a motor gear unit and using a control device. The speed of rotation of the rolls is generally between 4 and 25 m/min and depends on the productivity of the plant. In operation, the roller 50 cooperates with the outlet die 3 and, while rotating, transports the coextruded profiled element strip 100 to a transfer device such as a conveyor belt 200.

The roller 50 is rigid and is preferably made of steel having a polished outer surface 52 and a roughness Ra < 0.4.

According to the invention, the flow ducts 2a, 2b, 2c, 2d are parallel to each other and perpendicular to the circumferential direction of the roller 50, and the strip of profiled elements co-extruded using the apparatus according to the invention is joined to the receiving surface along an equivalent length of at least 700 mm.

Equivalent length refers to the contact distance between the coextruded profiled element strip exiting die 3 and the outer receiving surface 52 of the roll. The coextruded profiled element strip 100 is held in contact with the rollers over a distance 54 of equivalent length greater than or equal to 700mm, which allows all exit stresses to relax when transferred by the conveyor belt 200 towards the assembly or towards a storage station.

The flow ducts 2a, 2b, 2c and 2d are parallel to each other and perpendicular to the circumferential direction of the roller 50 and are arranged on a vertical plane parallel to the rotational axis of the roller. Preferably, the median vertical plane parallel to the flow conduit of extrusion head 2 contains the axis of rotation of roller 50.

In a first embodiment of the invention, as best shown in fig. 2, the diameter or outer diameter of the roller 50 is equal to or greater than 0.6m, preferably between 0.6m and 4m, and even more preferably between 1 and 2.5 m. In laboratory tests, it was found that the large diameter rollers allowed the coextruded profiled element strip to remain longer on the rollers, while avoiding imposing too large a radius of curvature on the rollers, compared to the rollers of prior art extrusion devices (typically between 200mm and 500mm in diameter).

Such large diameter rigid rolls require a strong construction of the support bearings and the rotary bearings, as well as good accuracy of the roll positioning. Preferably, the roll comprises a first cooling system for its outer surface 52 (for example in the form of a temperature-controlled water circuit) capable of cooling the profiled element strip 100, and a second cooling system for its support bearings (not shown in the figures). It is advantageous to cool the cooling system for the outer surface 52 and the cooling system for the roller support bearings to the same temperature, so as to avoid differential expansion phenomena between the two and to obtain dimensional stability of the assembly in operation. The cooling circuit is connected to a control unit which controls the cooling system according to the same set temperature.

In a second mode of operation, as best shown in fig. 1 and 3, the strip of profiled elements 100 is engaged with the outer surface 52 of the roller 50 along a distance at least equal to the 1/2 and preferably 3/4 circumferences of the roller prior to transfer of the strip of profiled elements 100 to the strip conveyor.

Advantageously, therefore, the coextruded profiled element strip is held over at least 180 ° or preferably 270 ° of the circumference of the roll. For products that are not attached to the outer surface of the roll, retention on the 3/4 turns of the roll is a determining factor. In order to attach to the roll and thus relax the stress with a controlled geometry, the tension applied to the product at the roll exit must be low to avoid product deformation.

The retention at 3/4 turns of the roller allows the product to achieve such a low exit tension. Therefore, the following formula is used for calculation

T/T ═ exp (f.alpha), where

T is the traction force generated at the roll head exit (giving a contraction stress),

t is the tension at the exit of the roll, and should be as low as possible, so that the strip does not deform,

f is the coefficient of friction, and

alpha is the holding angle of the product on the roller (holding angle equals 90 deg. or Pi/2 radian for a quarter turn, or 180 deg. or Pi radian for a half turn, and 270 deg. or 1.5Pi radian for a three quarter turn),

reflecting this result (the table below of cells gives the ratio T/T):

thus, by remaining at 3/4 circumference of the roller 50, the profiled element strip 100 is driven primarily by friction with the roller surface (rather than by exit tension).

In the variant of fig. 1, the roller 50 is arranged above the assembly formed by the extruders 10, 20, 30, 40 and the extrusion head 2, which assembly is referred to hereinafter as "tool". This in turn allows for the ejection of a coextruded profiled element strip 100 with the "bottom" (flat portion) oriented towards the belt surface of the conveyor belt 200.

In the variant of fig. 3, the roller 50 is arranged above the tool for accessibility and ergonomic reasons. This requires an angular reversal to return the coextruded profiled element strip 100 to the optimum direction of transport on the discharge belt. For this purpose, direction-changing rollers 71 and 72 are disposed between the roller 50 and the conveyor belt 200.

In the second embodiment, when using a roller with a diameter equal to or greater than 1m, it was found that maintaining the coextruded product at an angular distance of between 180 ° and 210 ° of the outer surface 52 of the roller achieves very good results in terms of stress relaxation.

In a third embodiment and as shown more clearly in fig. 4, the roller 50 drives an endless belt 80 interposed between the die 3 and said roller, so that the die 3 cooperates with the roller 50 to shape the profiled element strip by said belt.

To address the problem of constructing large diameter rolls 50, it is advantageous to install a belt that holds the coextruded profiled element strip in a longer position to maximize stress relaxation. Such a belt 80 is mounted between two rollers, the first driven roller being formed by the roller 50 of the roller head, and the second roller 85 being mounted so as to be freely rotatable. In a variant embodiment, the rollers 50 and 85 have a diameter of about 300 mm.

To ensure optimal service life of the belt 80, the belt 80 is preferably made of stainless steel.

Controlling the speed of the belt is critical to achieving the desired geometry of the coextruded profiled element strip 100. In order to avoid slipping between the metal strip 80 and the roller 50, it is advantageous to arrange on the outer surface of the roller a zone coated with an adhesive material, for example rubber.

A cooling device 90 for the belt 80 may be provided. The cooling device 90 may comprise, in a known manner, atomizing nozzles for a cooling fluid above and/or below the belt 80.

The strip of co-extruded profiled elements 100 leaves the belt 80 at the level of the second roller 85 and is discharged by the conveyor belt 200 towards another location of the tyre manufacturing facility.

In the figures showing the plant of the invention, all the extruders 10, 20, 30, 40 of the plant 1 are extruders using archimedes screws. In another variant of the invention, at least one extruder of the apparatus 1 is a positive displacement extruder, for example of the positive displacement, counter-rotating, twin-screw extruder type, having closely meshing screw flights with matching profiles, of the type described in patent application WO2017/109419 in the name of the applicant. Furthermore, other types of positive displacement extruders may be used, such as gear pumps or piston pump types.

Other variations and embodiments of the invention may be envisaged without departing from the scope of the invention as claimed. Therefore, a combination of the embodiments may be considered, for example, the roller 50 of the first embodiment may be used in the second and third embodiments.