Machine for continuously mixing rubber with partially tangential and interpenetrating rotors

Abstract: Method for continuously mixing polymer materials by means of a continuous mixing machine which comprises a mixing chamber (5) provided with at least one opening (4a, 6a) for supplying the polymer and at least one mouth (5d) for discharging the mixture and having arranged inside it a pair of rotors (7) parallel with one another, said method comprising the stages of: supplying the material and any additives to the mixing chamber (5) through said supply mouth; taking up, by said pair of rotors (7), of the materials supplied for mixing and feeding thereof towards said outlet (5d); and involving the following: at least one pre-mixing stage performed by means of axial sections (7b) of said rotors (7) rotating tangentially with respect to one another and at least one subsequent mixing stage performed by means of axial sections (7c) of said rotors rotating in a mutually interpenetrating manner.

Description: The present invention relates to a method for continuously mixing rubber and an associated machine with parallel rotors, which method comprises at least one pre-mixing stage performed by means of corresponding axial sections of said rotors rotating tangentially with respect to one another and at least one subsequent mixing stage performed by means of corresponding axial sections of said rotors rotating in a mutually interpenetrating manner. In the technical sector relating to the mixing of polymer materials it is known of the possibility of performing said mixing operation by means of production cycles of the discontinuous or continuous type. The continuous process offers numerous advantages compared to the discontinuous process, both from a technological point of view and with regard to plant design. Technologically speaking, the continuous process allows the most important processing variables to be monitored at each moment, ensuring more constant quality of the processed product, with a consequent reduction in the number of product rejects which are not to specification. In addition, with continuous processing it is possible to eliminate entirely the dead time which is typical of discontinuous processing and which occurs in particular during charging of the raw materials and discharging of the mixture, but also during the operations involving cleaning of the charging hopper. In addition to the aforementioned advantages relating to monitoring, the continuous process also allows the parameters being monitored to be corrected more easily without major consequences, since this correction has an immediate effect and is not linked to the time variable which, on the other hand, is of fundamental importance in discontinuous cycles during which there are logic and time sequences to be respected during the cycle. From the point of view of plant design, a continuous processing line offers advantages because the installed power levels are lower since the machinery, as regards both the actual mixer and the auxiliary equipment (control units, compressors, metering scales, etc.), has smaller dimensions and is therefore lighter. The technology for the continuous mixing of rubber, however, is still in the early stages of development on account of the difficulties which are encountered in achieving, at the same time, good qualitative results in terms of dispersion of the components forming the mixture and a low discharge temperature of the mixture itself, necessary in order to avoid a premature action of the cross-linking agents present in the mixture, resulting in "scorching" of the mixture, which could no longer be used for the subsequent processing operations, such as extrusion, moulding and the like. In addition to the above, it is also known of the problems relating to the continuous supplying of materials in batches since, during metering, performed by means of gravimetric metering devices, a large quantity of air is introduced into the mixing chamber, causing an increase in the apparent volume of the mixture, preventing correct feeding thereof towards the mixing zones situated thereafter. In an attempt to find solutions to said problems, continuous machines equipped with a pair of rotors of the tangential type have been provided, said rotors being particularly suitable for the zone immediately adjacent to the supplying zone, but on the other hand of limited efficiency in the zones of the machine situated thereafter where it is required to incorporate the fillers into the elastomer matrix, while maintaining good control over the temperature of the mixture. Machines equipped with a pair of rotors of the interpenetrating type have also been provided, the choice of one or other machine depending on the degree of viscosity of the mixture to be processed, the physical state and the dimensions of the raw materials to be supplied. There also exist machines consisting of a single specially shaped screw rotating inside a cylinder with walls provided with circular pegs or fixed parts of various shapes, which however have the purpose of distributing the flows of material in several directions and providing a cutting action. These latter machines are used with a wide range of products of varying viscosity, but are able to mix efficiently the products only if the viscosity of the material is low and if the material has a purely thermoplastic behaviour. In the case of materials with a high viscosity, these single screws are able to exert only a distributive and homogenizing action on the material, without, however, providing the high shearing forces necessary for a good mixing action. In other words, it is not known in the technical sector relating to the continuous processing of rubber of the possibility of obtaining, in a single machine, complete mixing which comprises the following stages: reduction in the average diameter of the particles of the individual components of the mixture and incorporation of the particles thus reduced into the elastomer matrix (dispersive mixing); and uniform distribution and homogenization of the particles inside the mixture (distributive mixing); maintaining optimum control over the temperature of the mixture during all the mixing stages. Said prior art is disclosed in GB-1.468.481- EP-A-513 742 shows rotors of different diameters in a twin screw mixes. The technical problem which is posed, therefore, is that of providing a method for continuously mixing rubber and a machine equipped with a single pair of rotors designed to allow processing of any type of mixture, independently of its greater or lesser viscosity. Within the scope of said technical problem, it is required moreover that said machine should be provided with rotors which make it possible to obtain: a high transportation volume in the first zone situated immediately after the supply hopper; sufficient thrusting of the material towards the end orifice, resulting in the material emerging without pulsed flow effects; optimum mixing of all the ingredients of the mixture, both solid and liquid, by means of operations on the material which produce an optimum effect in terms of both dispersive mixing and distributive mixing; efficient control over the temperature of the mixture, in particular in the end zone of the machine close to the discharge point. These results are obtained by the present invention, which provides a machine according to the features of claim 1. Further details may be obtained from the following description of an example of embodiment of the invention, provided with reference to the accompanying drawings, in which: Figure 1 shows a side view of the continuous mixing machine according to the present invention; Figure 2 shows a plan view of the machine according to Fig. 1, open at the top; Figure 3 has been deleted. Figure 4 shows a cross-section along the plane indicated by IV-IV in Fig. 2; Figures 5a,5b show a perspective view and the associated planar development of the interpenetrating part of the two rotors; Figures 6a,6b show views, corresponding to those of Figs. 5a, 5b, of the other rotor of the pair; Figure 7 shows a schematic partial section through the end zone of the machine with a further embodiment of the device for adjusting discharging of the material; and Figure 8 shows a partial section along the plane indicated by VIII-VIII in Fig. 7; As shown in the Figures, a machine 1 for continuously mixing rubber 2 comprises a housing 3 which is supported by bases 3a resting on the ground and provided with a cover 4 which can be opened by means of rotation about associated hinges not shown. The inside of said housing is formed so as to provide a chamber 5 having a cross-section substantially in the form of an overturned figure-of-eight and extending over the entire axial length of the machine. At the end of the chamber 5 there is located a mouth 5d for discharging the material downwards, the aperture of which may be adjusted by means of associated devices described below. The upper surface of said cover 4 is provided with at least one opening 4a provided with an associated hopper 6a, for supplying the polymer 2 and the additives necessary for obtaining the particular chemicophysical characteristics required for each specific type of mixture. The chamber 5 has arranged inside it the pair of mixing rotors 7 operated by coaxial motors 8 which are arranged at one end of the container 3; each of said rotors 7 has external surface sections which extend axially from the said supply zone to the mouth 5d for discharging the mixture 2 and are differently formed depending on the different processing operation required in the corresponding chamber section. More particularly, the first rotor section 7a, corresponding to the chamber zone 5a close to the hopper 6 supplying the polymer 2, is formed in the manner of a screw designed to push the polymer towards the next section 5b of the chamber 5 inside which the rotors 7 have sections 7b with an external surface such that the two rotors remain tangential with respect to one another and hence designed to ensure a high capacity for feeding of the material as well as a high mixing capacity. In said chamber section 5a, therefore, efficient pre-mixing of the components is obtained under ambient pressure and controlled temperature conditions, such that said temperature is kept below 80°C in order to avoid scorching of the mixture. In the last section 7c of their axial extension, on the other hand, the rotors 7 have an external surface such that the two rotors are mutually interpenetrating and therefore favour dispersive mixing and homogenization of the mixture. In correspondence with the greater size of the rotors 7 in the end processing zone, the chamber 5 also has a section 5c with an axial length substantially corresponding to that of the section 7c of the interpenetrating rotors, but an increased cross-section. This increase in the size of the chamber 5 in said end section 5c involves a corresponding increase in the area of contact of the mixture with the metal surface of the chamber 5 inside the cavity of which the cooling liquid flows, thus favouring control and lowering of the temperature of the mixture before it emerges from the chamber 5 through the discharge mouth 5d. Said mouth 5d for discharging the mixture from the machine is provided with devices for adjusting its aperture, substantially consisting of a gate valve 9 which can be actuated so as to perform a translatory movement by means of associated operating means known per se and therefore not illustrated in detail. By means of said adjustment of the mixture discharge aperture it is also possible to obtain different filling of the mixing chamber and hence different energy transferred to the mixture itself. As illustrated in Figures 5a,5b and 6a,6b, the rotor section 5c with an interpenetrating configuration has, in a preferred embodiment, the flange 7d radially projecting from the rotor core and arranged in the manner of a helix with inclination of its axis by about 15° with respect to the longitudinal axis of the rotor. Said angle of inclination, however, may be comprised between 10° and 25° depending on the different characteristics of the rubber to be mixed. In the drawings illustrated and described, the rotors 5 are counter-rotating and have a symmetrical configuration with respect to the longitudinal axis of the machine; during assembly, however, one of the two rotors is offset with respect to the other one by a suitable angle, so as to prevent the interpenetrating sections from coming into contact and damaging the machine. In addition, the right-hand or left-hand configuration of the helix is obviously linked to the direction of rotation of the associated rotor so as to ensure correct feeding of the material from the supply mouth to the discharge mouth. As illustrated in Figures 7 and 8, a variation of embodiment of the means for adjusting the discharge opening 5d is also provided. In this embodiment said means consist of a cylindrical element 109, internally hollow at least over a suitable longitudinal section, where a opening 109a is formed on the side surface of the cylinder. Said cylinder is arranged transversely with respect to the mixture discharge mouth 5d and has mounted, at one of its ends, rotationally operating devices 109c which are known per se and hence only schematically shown in the Figures. By operating said cylinder and causing it to rotate it is possible to bring the opening 109a of the cylinder 109 into total/partial alignment with the discharge mouth 5d of the chamber 5, totally/partially opening the latter and allowing the material to flow out in a controlled manner. As shown in Fig. 7, the discharge cross-section of the opening 5d is frustoconical with the widest part directed downwards so as to favour flowing out of the material.

Claims: Machine for continuously mixing rubber comprising a mixing chamber (5) provided with at least one opening (4a,6a) for supplying the polymer and at least one mouth (5d) for discharging the mixture (2) and having arranged inside it a pair of counter rotating shafts (7) extending through the chamber (5), wherein said chamber is divided into longitudinal sections along the flowstream of the material, each chamber section identifiyng a first initial part of predetermined cross-section, into which the shaft (7) is configured in the manner of tangential screws (7a); at least one intermediate part having cross-section corresponding to the one of the initial part, into which said shafts (7) are configured in form of tangential rotors (7b); a final part having enlarged cross-section in respect of the previous ones, into which the shafts are configured in the manner of interpenetrating rotors (7c) having greater cross-section than the others. Machine according to Claim 1, characterized in that said interpenetrating rotor sections have flanges (7d) which are helically wound at angles of inclination of between 10 and 25 degrees with respect to the longitudinal axis. Machine according to Claims 1 and 2, characterized in that said angles are preferably comprised between 12 and 18 degrees. Machine according to Claim 1, characterized in that said mouth (5d) for discharging the mixture (2) has an aperture which can be adjusted by means of associated adjusting means (9;109). Machine according to Claims 1 and 4. characterized in that said means for adjusting the aperture for discharging the mixture (2) substantially consist of a gate valve (9) which can be actuated so as to perform a translatory movement for insertion/extraction into/from the discharge mouth itself. Machine according to Claims 1 and 4, characterized in that said means for adjusting the aperture for discharging the mixture (2) substantially consist of a cylinder (109) which is at least partially hollow and arranged transversely with respect to said discharge mouth and which has on its side surface an opening (109a) designed to be brought into alignment with said discharge mouth by means of rotation of said cylinder performed by associated operating means (109c). Machine according to Claim 1, characterized in that said discharge mouth has a substantially frustoconical vertical section with its larger base arranged below the smaller base.

Inventors: GHEORGHITA VICTOR, GHEORGHITA, VICTOR
Applicants: TECHINT SPA, TECHINT - COMPAGNIA TECNICA INTERNAZIONALE S.P.A.
Application year: 1997
Main classification: B29B7
IPC codes: B29B7, B29C47, B01F7