Integrated system and method for recycling and processing compound materials

Abstract

This description relates to the reuse of waste materials based on synthetic resins and, more specifically relates to the reuse of disposable diapers, plastic packaging (PVC, PP, PET, and so on), for the production of raw material for extrusion, lamination, injection and rotational molding processes, among others. A system comprises a chopper, a mill for homogenization of particle size, a disc compactor employing frictional heating between a fixed disc and a rotating disc and cooling by circulation of cold water inside the discs.

Claims

1. An integrated system for recycling and processing compound materials comprising a material shredder, a particle size homogenizer mill, a friction compactor and particle cooler, wherein said friction compactor and particle cooler comprises a water-cooled disc compactor; wherein the particle size homogenizer mill and the friction compactor and particle cooler are downstream of the material shredder; the material shredder and the particle size homogenizer are located upstream of the friction compactor and particle cooler; and the material shredder comprises a knife mill.

2. A method for recycling and processing compound materials using, as raw materials disposable diapers, plastic packaging, as well as reduced proportions of non-plastic materials, comprising the following sequential steps of material selection, shredding, mixing, compaction and cooling, wherein said compaction is carried out by friction in a disc compactor, in which a first disc is kept fixed and a second disc moves with a rotation speed in the range of 400 to 500 RPM, wherein all of the steps are dry processes, wherein said shredding is carried out by a knife mill that produces shredded material comprising a thermoplastic, and wherein material being delivered to the mixing step comprises the shredded thermoplastic material to which are added non-plastic materials comprising cellulose, superabsorbent polymer and textile fibers.

3. A method according to claim 2, wherein the shredded material produced by the knife mill has a maximum size of 6 cm.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) Further advantages and features of the invention will become more evident from the description of an exemplary, non-limiting embodiment and the related figures, in which:

(2) FIGS. 1 and 2 illustrate a known system, specifically the object of patent application PI9203607-4.

(3) FIG. 3 is a simplified diagram of the proposed method, showing its main steps.

(4) FIG. 4 is a front view of the rotating compacting disc.

(5) FIG. 5 is a sectional view of the rotating compacting disc.

DETAILED DESCRIPTION OF THE INVENTION

(6) There are several barriers to recovering and reusing waste disposable items, mainly plastic packaging used for the packaging of beverages, milk products, softeners, cleaning materials, diapers and disposable absorbents, and so on.

(7) One problem is that such waste usually contains a mixture of materials that are joined together in conventional manufacturing processes. For example, waste may contain mixed plastics of different parts or different types of polymers. Mixed plastics can include fused polypropylene, elastomeric polypropylene and polyethylene, and superabsorbent polymers, among other plastics.

(8) Such materials end up being disposed of in landfills, generating considerable environmental impact since their decomposition can take tens or hundreds of years. The reuse of these materials, in addition to reducing contamination of the environment, has economic advantages since it reduces the need for raw material derived from non-renewable sources.

(9) The proposed system now comprises a materials shredder, a mill for homogenizing the particles size, a friction compactor, and a particle cooler, where the so-called shredder consists of a knife mill.

(10) The compactor consists of a disc compactor, cooled by circulation of water. The cooling water circulation arrangement, which cools the fixed disc and the rotating disc, comprises: in the fixed disc, an internal chamber where thermal exchange takes place; and at the rotator, a rotating joint containing an inlet duct leading to the respective inner chamber where the thermal exchange takes place, and a concentric outlet pipe, external to the inlet one.

(11) As depicted in the block diagram of FIG. 3, the method of invention comprises steps of material selection, chopping, mixing and dry processing, compaction and cooling.

(12) In the selection stage of materials to be processed, those with high melting temperature such as aramids, polyester, cardboard, rubber, ultra-high molecular weight polyethylene, leather and metals, among others, are eliminated.

(13) After selection, the material goes through a chopping step, in which cutting blades reduce the size of the selected material to bits with approximate fragment size of 6 centimeters or less, suitable for their introduction into the compacting device.

(14) Fragmented thermoplastics are introduced into the frictional disc compactor together with non-plastic materials such as cellulose, superabsorbent polymer (SAP) and textile fibers.

(15) The proportions of these materials used may vary according to the desired formulation. In a typical exemplifying and non-limiting embodiment of the invention, such proportions may be as follows: PE (polyethylene): 5% to 40%; TNT (nonwoven material, polypropylene based): 20% to 60%; PUE (elastane): 0% to 6%; Cellulose: 20% to 60%; Absorbent gel: 0% to 8%.

(16) According to the invention, processing uses friction between a first static disc and a second rotating disc, as illustrated in FIGS. 4 and 5. The rotation speed of said second disc is between 400 and 500 RPM, preferably between 440 and 450 RPM. According to the principles of the invention, the compacting operation is a dry process, that is, without adding water or steam in contact with the material submitted to the process. In the stage of compacting the friction of the material between said disc increases the temperature producing the softening of thermoplastics and the homogenization of the processed material without, however, reaching the degradation temperature of these polymers. For most applications, the temperature range should be adjusted according to the nature of the polymers used. Thus, the temperatures of the discs range from 110? C. to 150? C. in the case of the disposable diapers and polyethylene. In the case of polyolefins the maximum temperature is about 130? C.

(17) Once homogenized, the material can then be extruded, or subjected to injection or rotational molding process, or further, be pelletized for storage and subsequent processing by known methods such as extrusion, thermo-molding, and so on.