Method for Manufacturing a Rubber Pellet, a Rubber Pellet as Well as a Product Manufactured from Such Rubber Pellet

Abstract

The invention relates to a method for manufacturing a pellet, comprising a) providing residual rubber powder from a rubber disintegration process; b) providing a pelletizing system, including a pelletizer and a cooling device; c) feeding the residual rubber powder as at least part of a feed material, into a pelletizer; d) providing the rubber powder in an amount between 50% and 100%; e) applying a pressure to the residual rubber for a predetermined process duration; f) releasing the pelletized rubber and cooling the pelletized rubber at a cooling rate dependent on the operational temperature of the pelletizer.

Claims

1. A method for manufacturing a pellet, comprising a. providing residual rubber powder from a rubber disintegration process; b. providing a pelletizing system, including a pelletizer and a cooling device; c. feeding the residual rubber powder as at least part of a feed material, into a pelletizer d. providing the residual rubber powder in an amount between 50% and 100%, e. applying a pressure to the residual rubber for a predetermined process duration; f. releasing the pelletized rubber, and g. cooling the pelletized rubber at a cooling rate dependent on the operational temperature of the pelletizer to a level below a certain critical temperature.

2. A method according to claim 1, where the rubber powder is added to the feed material with a grain size essentially between 0.0 mm and 1,0 mm.

3. A method according to claim 2, where further textile fibers, binding additives, vulcanizing chemicals, rubber granulate, minerals or further organic and/or inorganic chemicals are added to the rubber powder to form the feed material.

4. A method according to claim 1, where the method comprises heating the pelletizer to an operational temperature of at least 120 degrees Celsius.

5. A method according to claim 1, further comprising adding sulphur to the feed material prior to the introduction into the pelletizer.

6. A method according to claim 1, where the pelletizer temperature is maintained at a level resulting in a pellet temperature below 180 C., preferably below 170 C.

7. A method according to claim 1, the method comprising adding water to the pelletized rubber immediately after the pelletizing process in order to initialise cooling.

8. A method according to claim 6, where water is added in an amount suitable to reduce the temperature to a level below said certain critical temperature and allowing excess water to evaporate.

9. A pellet manufactured by a process as defined above, the pellet characterized by a vulcanized rubber powder, where the vulcanized powder comprises rubber particles of a size between 0,0 mm and 1,0 mm, where the pellet has a length between 5 mm and 80 mm, preferably between 10 mm and 40 mm and a thickness between 2 mm and 10 mm.

10. A pellet according to claim 9, where the pellet further comprises textile fibers, binding additives, vulcanizing chemicals, rubber granulate, minerals or further organic and/or inorganic chemicals.

11. A product manufactured from pellets according to claim 9, where the pellets are joined together, e.g. by adding a binder such as PUR.

Description

DESCRIPTION OF THE DRAWING

[0038] FIG. 1 schematically shows the process related to recycling rubber;

[0039] FIG. 2 shows the chemical reaction; and

[0040] FIG. 3 schematically shows a pellet according to the invention

DETAILED DESCRIPTION OF THE INVENTION

[0041] The invention relates to the area of producing rubber pellets from rubber powder and granulate generated by grinding of ELT (End of Life Tires) and other rubber products, such as rubber conveyors, for use in the industrial applications, e.g. in the steel industry, and as shock pads.

[0042] Industrial applications of the rubber pellets may be several. The typical application may be in industrial processes where a need exists for adding a carbon rich additive capable of removing O.sub.2. One example is the steel industry, which will be described in more detail in the following.

[0043] The Steel Industry Use

[0044] Today coke, coal or other carbon containing material are added to the melting pots used in the steel industry for producing cast iron. This provides for a desired layer on the melt while at the same time removing O.sub.2 by conversion to CO.sub.2.

[0045] Rubber pellets with a carbon content of more than 70% can substitute the existing technology. This is an environmentally sound solution as the product is recycled and therefore does not involve a burning of fossil carbon.

[0046] The Shock Pad Use

[0047] Shock pads are used as a substrate for artificial lawns, on play grounds, in fitness gyms, on roof surfaces and a number of other applications. Today these shock pads are manufactured from a rubber granulate bound by a glue, typically a PUR glue (Poly Urethane Resin)

[0048] By use of rubber pellets of a certain length (typically between 10 and 40 mm) it is possible to reduce the bulk density and hence reduce the amount of glue that needs to be used for binding the product. The result is that the material amount is reduced and hence the cost of the final product.

[0049] Further the rubber pellets have the advantage that they are overlapping and hence have more binding area in relation to neighbouring rubber pellets. This further increases the strength of the shock pad and reduces the risk of tearing of the shock pad when adding a load to the shock pad.

[0050] When grinding a tire, three different material groups are generated. These are steel, textile and rubber. The steel and the textile components are sorted from the rubber fraction, which is successively ground to a number of different size fractions. Some of these size fractions are less sought after in the market, where these typically are the smaller size fractions.

[0051] By manufacturing larger pellets from these smaller fractions the market will increase as the larger size rubber fractions are much more sought after.

[0052] The rubber powder is expected to contain a certain amount of accelerator and sulphur components that are not used during the original vulcanisation. At the same time a number of double bindings are present in the surface of the rubber powder. Subject to high pressure the powder is squeezed in such a manner that the surfaces are brought in contact with each other. The high temperature that arises as a consequence of the rubber powder friction with the steel surface of the pelletiser matrix will vulcanise the squeezed powder to a joined pellet.

[0053] The production of the pellets is done by squeezing the rubber powder through a pelletizer matrix having one or more holes or profiles with a size in the range 1-40 mm. As the material is subject to a significant pressure and a high temperature, caused by the friction, the rubber particles are cured together to form a solid pellet. A knife arrangement may be provided in case a reduction of the pellets to a smaller size in desired. Further additives, such as organic or inorganic substances may be added to change the characteristics of the pellets. The latter may alter the possible uses of the pellets and also have an effect on the desirability of the pellets and hence the price.

[0054] The Vulcanization Process

[0055] Vulcanization is a process where raw rubber is modified from a viscous and mouldable substance to a form stable elastic material. This is achieved through adding of heat whereby sulphur is forming cross-links or bridges between the polymer chains and hence forms an interconnected network. It is only a small fraction of the double-bonds in the polymer that are used in the vulcanization process. Therefore there are numerous double-bonds present in the surface of the rubber powder, which can form crosslinks with other rubber powder particles. A small fraction of sulphur is still present in the powder, which is the accelerator for the crosslinking formation, and further addition of sulphur may increase the speed of the crosslinking formation.

[0056] From FIG. 1 the process related to rubber recycling is schematically shown, The disintegration of the used rubber, such as tires, is as such well known and practised by many entities worldwide. The part of the process related to the invention is indicated by the area surrounded by the dashed line. The powder material and possibly additional material and substances as described previously are pelletized as likewise described and hence a product with a number of advantages is obtained.

[0057] In FIG. 2 the crosslinking process is illustrated. A number of chains of poly(isoprene) are crosslinked by the addition of sulphur.

[0058] The pellet obtained by the process is depicted in FIG. 3. The pellet is shown with a length L and a diameter D. L and D may vary as described in the previous description and will be dictated by the preferred use of the pellet. Although a diameter has been indicated, which will normally indicate a circular cross section it should be appreciated that other cross sectional shapes could be selected without deviating from the invention. The cross sectional measure D would then indicate a measure taken on the cross section of such other shape.

[0059] A number of tests have been carried out to demonstrate the feasibility of the technology. These are commented on in the following:

TABLE-US-00001 Test 1: Surface Fines < 0.2 Powder Pellet size temp. Output Bulk density mm 0.2-0.8 3.5 6 mm 156 C. 109 kg/h 0.486 g/cm3 0.5%

TABLE-US-00002 Test 2 Surface Fines < 0.2 Powder Pellet size temp. Output Bulk density mm 0.0-0.8 3.5 4 mm 140 C. 120 kg/h 0.475 g/cm3 3.3%

TABLE-US-00003 Test 3 Surface Fines < 0.2 Powder Pellet size temp. Output Bulk density mm 0.2-0.8 3.5 4 mm 148 C. 160 kg/h 0.497 g/cm3 1.9%

TABLE-US-00004 Test 4 Surface Fines < 0.2 Powder Pellet size temp. Output Bulk density mm 0.0-0.8 3.5 40 mm 150 C. ? kg/h 0.374 g/cm3 0.2%

[0060] It should be appreciated that the term pelletizer is to be understood broadly. On form of pelletizer may be a traditional rotational pelletizer, where matrices are shaped according to the desired pellet size. An extruder may be a further option for applying the necessary pressure to the rubber powder and pressing the rubber through the matrix to obtain the pellets.

[0061] It should further be appreciated that the pellets may have a wider use than in the shock pads as described and in the steel industry as described.